Math cad d-l governing load combination case selector algorithm
Load Cases and Combination
22
• • • • WI KHARG ETHYLENE PLANT KHARG Olefin Complex 1300 000 I 0 I 1/13 --- INSTRUCTIONS FOR STRESS ANALYSIS LOAD CASES .. - Pl'TROCIWM 1 CAL INDUSTRIES MANAOIlMllNT co. 1 1(u1 ,11 FOR INFORMATION ONLY , ' . WI 1 l ANG . ,.... A.ICH AAC UE ...lOAOCASCS_O. dO(:
-
Upload
oluwachidi -
Category
Documents
-
view
91 -
download
5
description
Brief description of load case combination that are requiredd for pipe stress analysis.
Transcript of Load Cases and Combination
bull
bull
bull
bull
WI
KHARG ETHYLENE PLANT KHARG Olefin Complex
1300 000 I 0 I 113
--shyINSTRUCTIONS FOR STRESS ANALYSIS
LOAD CASES
-~
PlTROCIWM 1CAL INDUSTRIES DEVFIOPMr~T MANAOIlMllNT co
11(u111
FOR INFORMATION ONLY
WI 1 l ANG AICHAACUElOAOCASCS_OdO(
bull Techn ip
000
KHARG ETHYLENE PLANT KHARG Olefin Complex
CONTENT
2113
l Load C bullbullbull bull bull bullbullbullbullbullbullbullbullbullbullbullbull+ J
11 For Lines Carrying Heavy Fluid ( Hydropoundarboll Waler J I J2 For Lines Carrying Gas Steam or Vapnr + Jj For Unef Connected to Rotating Eqpm + 14 FOR LOW TEMPERATURE CARBON STEEL (LTCS) Error Bokak lot dJlUud
IA 1 Load Cases 10 be calculated to comply with ASME B3 13 Code ea I 15 S ao -I 8
2 CONFIGURAnON FILES USING CAESAR n+ 10
2 1 Unit System (7273F FIL)
22 Setup File ( CAESARCFG) 1 II
bull
bull
I
bull
bull
bull
Technip
KHARG ETHYLENE PLANT KHARG Olefin Complex
CONTRACTOR DOCUMENT N OWNER OCXUMENT Ndeg
p Ndeg Unil Doc T Matetlal coo Serial Ndeg Rev Pa B PIN Unit Doc T Malerial Code Serial Ndeg Rev Pa
7273F 3 13313
1 LOAD CASES
Loads and stress types to be considered in the computer analysis are
Loads Stress types
-W Deadweight - (EXP) EXPANSION
-WNC Weight (No Contents) - (SUS) SUSTAINED
- WW Weight full of water - (OPE) OPERATING
- P Pressure Set 1 bull (OCC) OCCASIONAL
-P2 Pressure Set 2
- T1 Thennal Set 1
- T2 Thermal Set 2
- T3 Thermal Set 3
- 01 D2 03 Displacements (thermal effect)
- Fl F2 F3 External Forces ( used for slug surge p~v and rupture disk) bull- H Spring hanger fqrces
- Ul U2 U3 Uniform Loads
- WIN Wind ~oad 1
-WIN2 WinCl Load 2
The following load cases description assume that all calculated cases are lineaf (Le no n linear restraints gaps or friction)
Combination loads in the computer analysis can be the following assumin the calibration toad 01 s rin han er ha b en detin in a revious run 137 and the value defined in the s readshee s rin hanger
Technip
bull KHARG ETHYLENE PLANT
KHARG Olefin Complex
7273F WI
Case
(OCC) Sustained plus Wind Z combined absolutely
11 For Lines Carrying Heavy Fluid (Hydrocarbon Water )
a - Example File 2_00CA_O_A (Unit 20 Calculation Number 001 Load Case File AIKev 0)
bull
exposed to wind hydrostatic test spring supports No Yes_No CASE I W+~I+IJ+PI+H (O~E) Operating
CASE 2 W+PI+H (SUS) Deadweight + Pressure
CASE 3 U I (OCC) Seismic Load X
CASE 4 U2 (OCC) Seismic Load Y
CASES U3 (OCC) Seismic Load Z
CASE 6 L1 -L2 (EXP) Expansion range Code Case
CASE 7 W +lA+L5 (OCC) Resultant seismic load SRSS combination
CASE8 L2+L7 (OCC) Suslalncd plus Seismic Combined Case
b - Example File 2_002_A_O_A (Unil 20 Calculation Number 002 Load Case File A
exposed to wind hydrostatic test spring supports Noy Ye
bull
CASE I W+D1+T1+Pl+H
CASE 2 W+Pl+H
CASE 3 WIN I
CASE4 WIN2
CASES UI
CASE6 U2
CASE 7 U3
CASE 8 LI -L2
CASE 9 L5+ L6+L 7
CASE 10 L2+L3
CASE II L2+lA
CASE 12 L2+L9
(OPE) Operang
(SUS) Deadweight + Pressure
(SUS) Wind along X (Instead or oce 10 avoid Snbbe ivoio~ irany)
(SUS) Wind along Z Onslead oroce to avoid Snubber ifi(lY)
(OCC) Seismic Load X
(OCC) Sesmc Load Y
(OCC) Seismic Load Z
(EXP) Expansion range Code Case
(OCC) Resultant seismic load SRSS combination
(OCC) Sustained plus Wind X combined absolutely
Case
(OCC) Sustained plus Seismic Combined absolutely Case
Technip
P eel N
7273F
KHARG ETHYLENE PLANT KHARG Olefin Complex
CONTRACTOR DOCUMENT Ndeg
Malellal Code Selia N Rev Pa p
1300 000 0 513
PETItOCHllMrCAL IN ST1UES DEVELOPMENT MANG MENT CO
OW NER DOCUMENT Ndeg
Material Code Serial Ndeg Rev Pa
513
12 For Lines Carrying Gas Steam or Vapor
bull
Examplelr~~~~~+-_ex~po_S_ed~0 ~nd_ ~Wi __~_h~yd_~__I~a~____tic es1-_s~pn_n~g~s~u~ppo~rts__~ Line criteria No shy Yes Yes
a - Example File 2_003_A_O_A File A RevD)
CASE I WNC+DI+TI+PI+H
CASE 2 WNC+PI+H
CASE3UI
CASE 4 U2
CASES U3
(Unit 20 Calculation Number 003 Operating Loa Cases
(OPE) Operating
(SUS) Deadweight (No contents) + Pressure PI
(OCC) Seismic Load X
(OCC) Se ismic Load Y
(ccq Seismic Load Z
CASE 6 LImiddotL2 (EXP) Expansion range Code Case
CASE 7 L3+L4+LS (CCe) R~sultant seismic load SRSS combination
CASE 8 L2+L7 (OCC) Sustalfled plus SeIsmic Combined absolutely C e Case
b Example File 2_003_B_O_A (Unot 20 Calculation Number 003 Hydrotest LcJCase Fi le B RevD) lftested in place
CASE I WW+PI (SUS) Deadweight Full of water + Hydrotest Pressure PI
bull 4 -gt fv
L1 --1- r
Igt 0
bull Technip
P ec(Ndeg
n73F
KHARG ETHYLENE PLANT KHARG Olefin Complex
CONTRACTOR DOCUMENT N
P N
613
PETROCHEMICAL IN USTRJpoundS DEVElOPMENT MANA EMENT CO
OWNER DOCUMENT Ndeg
Material Code Sertal Ndeg Rev Pa
613
Example 2 r-~~~~~~~XP~osed~to~w~i~nd~~h~~=r~ost~at=ic~t==st~~sp=n=n~g~su=ppo==rt=s~ line criteria Yes Yes Yes
a Example File S_OOS_A_Obullfi (Uuil50 Calculation Number 00) Operating Load Case Fi e ArevO) J7LLA A_A
CASE 1 WNC+QI+Tt+PI+H (OPE) Operating
CASE 2 WNC+PI+H
CASE 3 WIN I
CASE 4 WlN2
CASE 5 VI
CASE 6 U2
CASE 7V3
CASE 8 Ll -L2
CASE 9 L5+L6+L7
CASE 10 L2+L3-shyCASE II L2+L4
CASE 12 L2+L9
(SUS) Deadweight (No contents) + Pressure
(SUS) Wind along X (1nstcad oroce 10 avoid Snubber activatio if any)
(SUS) Wind along Z (Instead ofoce to avoid Snubberactivarion ifany)
(OCe) Seismic Load X
(OCC) Seismic Load Y
(OCC) Seismic Load Z
(EXP) Ex pansion range Code Case
(ocq Resultant seismic load SRSS combination gt
(OCe) Sustained plus Wind X combined absolutely C I Case
(OCC) Sustained plus Wind Z combined absolutely Codf Case
(aCe) Sustained plus Seismic Combined absolutely Cod Case
b Example File S_OOSJl_O bull A (Unit 5OCalculation Number 005Hydrostatic Load case fil B
revO) 4-OlL ~ _A_A
CASE 1 WW+PI (SUS) Deadweight full of water + Hydrotest Pressure PI
bull WI I bull AHa bull_ Amiddot KHARGJELOAOCASESOdDc
bull
bull
RevO)
CASE I W+PI +TI+DI+H
CASE 2 W+PI+T2+DI+H
CASE 3 W+PI+T3+DI+H
CASE 4 W+Pl+H
CASE 5 WNC+H
CASE6UI
CASE U2
CASE 8 U3
CASE 9 L6+L+L8
CASE 10 LimiddotL4
CASE I I L2middotL4
CASE 12 L3middotL4
CASE 13 L4+L9
Technip
KHARG ETHYLENE PLANT KHARG Olefin Complex
PET1IOCJiEMCAL INOUSTIUES DEVElOfMENT MANA EMENT co
7273F
Nmiddot UtIiI Doe T
1300 000 0 713
File A
1-1 For Lines Connected to Rotating Equipmenl
Example File 002_007 _A_O_A (Unit 002 Calculation Number 007 Load ea
(OPE)
(OPE)
(OPE)
(SUS)
(SUS)
(OCC)
(OCC)
(OCC)
Operating Pump A operating 380degC
Pump B Standby 21degC (Ambient)
Operating Pump B operating 380degC
Pump A Standby 21degC (Ambient)
Operating Pump A and B hot 380ltgtlt
Deadweight + Pressure
Weight (No contents)
Seismic X
Seismic Y
Seismic Z
(ocq Resultant seismic load SRSS combination
(EXP) Thermal T 1 Pump A operating 380degC
Pump B Standby 21degC (Ambient)
(EXP) ThennaJ 12 Pump B operating 380degC
Pump A Standby 21degC (Ambient)
(EXP) Therma1 13 Pump A and B hot 380degC
(OCC) Sustained plus Seismic Combined absolutely C e Case
Note Load Case 5 is used to calrulate shop calibration of spring support instaJled above pump nozzle
- - - -
bull Technip
KHARG ETHYLENE PLANT KHARG Olefin Complex
CONTRACTOR OOCUIoENT N OWNER DOCUMENT
P N IJnIt Doc T lMtecW eoo Serial N Rev P p unit Doe T Material Code Serial Rev P
7273F 000 WI 1300 000 0 813
131 Load Cases to be calculated to comply wjtb ASME 831 3 Code Cases
~xample
CASE I W+DI+TI+P I(OPE)Operaling CASE 2 W+Pl(SUS) Deadweight + Pressure
CASE 3 U I (OCC) Seismic Load X
CASE 4 U2(OCC) Seismic Load Y
CASE 5 U3(OCC) Seismic load Z
CASE 6 LI -L2(EXP) Expansion range Code Ca~
CASE 7 W+L4+L5(OCC) Resultanl seismic load SRSS combination
ASE 8 L2+L7(OCC) Sustained plus Seismic Combined absolutelyCode Case
CASE 9 LI+L7(OCC) Operating plus Seismic combined absolutely hOI restraint (Optional)
813
CASE 10 L9+~(OCC) Maximum restrai nt loads (Optional)~ 14 FOR LOW TEMPERATURE CARBON STEEL (LTCS)
141 Stress criteria
The point (3) of the figure 3232B imposes to take into account the following load cases
Permanent static loads
bull W Weight (signed load)
bull bull P Pressure (signed load)
bull T low Temperature (signed load)
bull F exlemal loads (signed load)
Occasional static and dynamic loads
bull U seismic accelerations Corresponding to the SASS combination of the Ul (X dyion) U2 (Y direction) and U3 (Z direction) components
bull WIN Wind (unsigned load)
Remarks
I) In Caesar load case it is necessary to have by load case line only one of load cases d~=ibed her-under
2) In Caesar input all stress intensification factors shal l be equal to 1
TIle criteria is
W + P +T + F + U or WIN lt O3Sh - 413 Mpa combined in ABS( ~ shy
bull
9113
Technip
bull KHARG ETHYLENE PLANT
KHARG Olefin Complex
QVoINEA OClCUME NT N
P bull p N Unit Doc T Malerial Code Serial Ndeg Rw
913
142 Examples
Examplelr-~__~~-+~e~x~po=s~ed~to~W~ind=-~~h~~~r~o~st=a=t~~te=s~t~=s~ ~ po~rt~s-+pr=ing~s~u~p~line criteria Yes Yes Yes
bull Example File 002_01O-A_O_A (Unit 002 Calculation Number OlD Load Case File A evD)
CASE 1 W+Tl+PI+H (OPE) Operating cold condition
CASE 2 W+T2+P2+H (OPE) Operating hot conditions
CASE 3 W+PI +H (SUS) Deadweight + Pressure
CASE 4 WINl (SUS) Wind along X (Instead of OCC to avoid Snubber activation if I y)
CASES WIN2 (SUS) Wind along Z (Instead of OCC to avoid Snubber activation if y)
CASE 6 Ul (OCC) Seismic Lcentad X
CASE 7 U2 (OCe) Seismic Load Y
CASES U3 (OCC) Seismic Load Z
CASE9W+H (SUS) Deadweight + Spring hanger
CASE 10 PI (SUS) Pressure
CASE J 1 Tl (EXP) Temperarure
CASE 12 LI -L2 (EXP) thermal stress range Code Case
CASE 13 Ll -L3 (EXP) thermal suess range Code Case
CASE 14 LlI+Ll2 (EXP) full thermal stress range checking ABS combination
CASE 15 L6+L7+LS (OCC) Resultant seismic load SRSS combination CASE 16 ~9+L10+L1I+L3 (OCC) Sustained plus Wind X combined absolutely Code Ease CASE 17 L9+LI0+L11+L4 (OCC) Sustained plus Wind Z combined absolutely Code tase CASE 18 L9+L10+Lll+L15 (OCC) Sustained plus Seismic Combined absolutely Code ase
bull
bull
bull
bull
bull
Technip
KHARG ETHYLENE PLANT KHARG Olefin Complex
COHTAACTOR DOCUMENT N
-~
PEJROCHEMICAI IES DBVELOPMENT MANAG co
OWNER DOCUMENT Ndeg Unit Doe T P N
7273F 000 WI 1300 006 813 1 813 1
8 SNOW WAD (Ws)
I Emiddot~middotv O
Snow loads shall 00 applied only for cold outside lines for which design T is below 0 C and which are not protected by floor equ ipment or others
The hereafter calculated vaJue (Ws) will be classed as unifonn load foUowing Y axis (U ) in a separate Caesar input file See 7273F_OOO_CN3_CN2_1370_SAMPLlC AXLS
Design snow load 25 kgll1l2
The distribution of snow remaining on the horizontal pipe will take the shape hereu dec a reducljon factor of 072 may be applied
Ws = ( lx 051gt In x h 022D ) 25
Ws = (Ix 072 x D ) 25
Ws = 18 x D Kflrsi= 180 x D NIP Where 0 = outside diameter of pipe o r outside diameter of pipe + insulation if exist( m)
70middot
9120
o
bull Technip -D KHARG ETHYLENE PLANT ~
KHARG Olefin Complex
middot INmiddot I A~ I P~ UNo I 7273F 000 WI 1300 I 006 I A I 115 I 115
APPENDIX IV
L bull WIND PRESSURE I ELEVATION
11 Wind Basic nata I Wind pressure calcuJation
As per Project Basic Engineering 7273F-30-PP-206 Bask Design Data
Basic wind speed 160km h (44 5 m s)
Exposure Category 0
According to UBC 97 the design wind loading shall be
p= CxCxqX
where
P =Design wind pressure allevel 10 III
C~ =156 at leve1 10 m (EIIposure and gust factor-Table I6-G)
Cq I for DNlt= 50 nun
= 08 for DNgt 50 mm (Exposure and gust factor-Table I6-H)
qs= 1226 kNm2 ( Wind stagnation pressure at 10 m -Table J6-F)
lw = 1 15 (Importance factor - Table 16-K)
p = 220 xC (kNl m)
Height Above Wind pressure Ground Level
(m) PI eq (kNlm2 )
Oto 10 22
10 (0 20 247
20 to 30 264
30 10 40 276
40 to 50 286
50 to 60 289
60 to 70 293
70 1080 299
80 to 90 312
bull
bull
bull
bull
CONTRACTOR OOCUIENT bull N UniI Doc T Milttl CoOl srI N Rev Pa p
7273F 000 WI 1300 000 0 ()J 13
2 CONFIGURATION FILES USING CAESAR II
21 Unit System (7273FFIL)
CAE S A R liVERS 430
INPUT UNITS USED
UNITS 7273F NOMISCH INPUT ON
LENGTH inches
FORCE pounds
MASS(dynamics) pounds
MOMENTS(INPUn inch-pounds
MOMENTS(OUTPUT) inch-pounds
STRESS Ibssqin
TEMP SCALE degrees F
PRESSURE psig
ELASTIC MODULUS Ibslsqin
PI PE DENSITY Ibslcuin
INSULATION DENS Ibslcuin
FLUID DENSITY Ibslcuin
TRANSL STI F Ibslin
ROTATIONAL STiF inlbldeg
UNIFORM LOAD Jblin
GLOAD gs
WIND LOAD IbsJsqin
ELEVATION inches
COMPOUND LENGTH inches
DIAMETER inches
WALL THICKNESS inches
OWNER DOCUMENT Ndeg
~ Doc T Malerial CoOa Serial Ndeg Rev
1013
x 25400 mm
x 4448 N
x 0454 kg
x 0113 Nm
x 0113 Nm
x 0007 MPa
x 0556 C
x 0069 bars
x 0007 MPa
x 27680000 kgCrmiddotm
x 27680000 kgJcum
x 27680000 kgci m
x 0175 Nm
x 0113
l x 175127 NJm
x 1000 gs
x 6894757 NJ m
x 0025 m
x 25400 mm
x 1000 inch
x 25400 mm
bull bull
Technip
KHARG ETHYLENE PLANT KHARG Olefin Complex
PETROCHlMlCAL IND JES DIiVElOPMENT MANGEMENT CO
11113
Technip bull
KHARG ETHYLENE PLANT ~ KHARG Olefin Complex
iETltOCHEMICtl OEVEIOPMENT MANArCO
CONTRACTOR DOCUMENT N OWNER DOCUMENT Nmiddot ProIecl N p U Doe TwalMrolerial Code ISen N ReI P_ Proiect N I UNt Doo T~ I ~eriIII Code
7273F 000 WI I 1300 I 000 I 0 I 11113 I I I
22 Setup File ( CAESARCFG )
C A E SAR II VERS450
SETUP FILE PARAMETERS
CONNECT GEOMETRY THRU CNODES YES I MIN ALLOWED BEND ANGLE 500000 I MAXjLLOWED BEND ANGLE bull 135000 I BEND LENGTH ATIACHMENT PERCENT 100000 I MINjNGLE TO ADJACENT BEND PT 500000
LOOP CLOSURE TOLERANCE 254000mm
THERMAL BOWING HORZ TOLERANCE 100000E-04
AUTO NODE NUMBER INCREMENT 100000
ZJXIS UP NO
USE PRESSURE STIFFENING DEFAULT
ALPHA TOLERANCE 500000E-02
RESLDmiddotFORCE NO
HGR_DEF RESWGT STIF
bull 01751200E+12 Nlmm
DECOMP SNG TOL 01 OOOOOOE+ 11
BEND_AXIAL SHAPE NO
FRICT STIF 875600 Ni mm I FRICT NORM FORCE VAR 025000 I FRICT ANGLE VAR 300000 I FRICT SLIDE MULT 100000
ROD TOLERANCE 100000
ROD INC 200000
INCORE NUMERICAL CHECK NO
OUTCORE NUMERICAL CHECK NO
DEFAULT TRANS RESTRAINT STIFF 0175120E+12 Nlmm
DEFAULT ROT RESTRAINT STIFF 0112980E+12 Nmi deaJ
IGNORE SPRING HANGER STIFFNESS bull NO I
WI I middot AiHG bull _ KtVRCUE LOoO CAS ES_Odoc
rmiddot
bull
bull
Technip
KHARG ETHYLENE PLANT KHARG Olefin Complex
Setup File (
CONNECT_GEOMETRY _ THRU_CNODES
WRC-07 VERSION
WRC- 07
DEFAULT
831
WI I middot AIlaquo) Amiddot KHARGJUOAD CASFsOdoc
T
F
YES
NO
181 281
NO
DEFAULT
02206272E+OSbull
bullbull
bull
bull
Thchnip bull
KHARG ETHYLENE PLANT ~ KHARG Olefin Complex
PFffiOCHEMICAL INO bull DEVELOPMENT MANAG ~ENTCO_
CONTRACTOR DOCUMENT Ndeg OWNER DOCUMENT N
Proioct Ndeg Unit Doc TIIDEII Material Code Serial Ndeg Rev I Paae Proiect N Unit Doc Type Material Code Serial N A~ 7273F I 000 I WI I 1300 I 000 I a I 13 13 I 1313
FRP Ratio GmodlEmo(Uaxial) O2500000E+OO
FRP EalEhVhla O1527272E+OO
SetuD File (CAESARCFG Continuation)
FRP Lamina1e Type THREE
FRP Alpha O2159827E+02 C
FRP Density O1660800E+04 kocum bullEXCLUDE 12 FROM UKOOA BENDI NG NO
OUTPUT REPORTS BY LOAD CASE YES
DISPLACEMENT NODAL SORTING YES
DYNAMIC INPUT EXAMPLE TEXT MAX
TIME HIST ANIMATE YES
ENABLE AUTOSAVE YES
AUTOSAVE TIME INTERVAL O3000000E+02
PROMPTED AUTOSAVE YES
DISABLE UNDOREDO NO
STRUCTURAL DATABASE AISC89BIN
VALVE amp FLANGE GENERIC VHD
EXPANSION JT DBASE FLEXPATHJHD
PI PING SIZE SPECIFICATION ANSI
DEFAULT SPRING HANGER TABLE O5000000E+01
SYSTEM DIRECTORY NAME SYSTEM
UNITS FILE NAME 7273FFIL
ENABLE ODBC OUTPUT NO
DEFAULT SPRING HANGER TABLE LlSEGA
- bull -
WI 1 ANG bull IV IlHAAG_IELOAD CAS ES_OdOC
SRMPL6 LOf]) C(15euro5 S V REfK Ti O-l FOeC e- JlUE TO PSv oPttvlNG
bull Sldlle Aymmiddot [CIDO(UMpoundNTS AllD SETIINGSVhBACONI7173FmiddotMBACONICAESAR FILESICNj016_REV ~
bull
bull
bull
Edt
+ t
loadCose Edlcr LoadCoseOptiom Loads WlNeLoads
loads Oefned n IrtJIA loed Casu Stress Type
W -Woltllt L1 W+D1 +T1 +P1 +H Of 01 middot Displcmnt Case ~ L2 wO-iT2+P1 +H-- Of T1 middot Thermal Case tn l3 W~D1~T3~P1H ~(]S-oiit~~ Of LltgtOd e T2 Thermal Case 2 -- - _- ------- -__- T3 Thermal Case U3
l4 W+P1+H SUS __ _- -----PI middot Pr euUle Case 1 LS Wt-P1t-H-t-F1 OCC Hp middot Hydlo Prenae L6 Ul OCC --- ---- _----- H middot Hanger l oads 17 U2 OCC UI middot Unf Load eMe 11 La U3 OCC U2 -UriloodlAse 12 L9 F1 OCC U3 Uri l oad Case 13 L10 L1-l4 EXP F1 middot Cone FOIct Case 11 1 Ll1 L2-l4 J EXP Vlllet Fled W WNC middot W~ no corieris L12 L3-lS EXP
L13 LS+l7+l8 OCC L1 4 L-4+l13 ----l ~~ IL15 L1 lt-l1 3 L1 6 LJl9 (fD lO(ll ch 011 (f~tnlh OCC
STATIQUE LoR)) I- Ill
1
FW FRANCE NDG SHT16F I
CliENT
PROJECT
CPNo
EXXON
18KTA E5000 Expansion
CALCNo ISV 3310
CALC BY BEP
CHKD BY
DATE 13012006
RELIEF VALVE LOADINGS vapour
RV Nos ISV 3310
SIZE 4x3
RATING 150xlSO
ORIFICE L
bull DATA DESCRIPTION
RV SET PRESSURE
PERCENT OVERPRESSURE
Ps (l+PolOO) + 147
REliEF TEMPERATURE
1195492
RATIO OF SPECIFIC HEATS SIZING FLOW
SElECTED ORIFICE AREA
CALCULATED ORIFICE AREA
FACTORED SIZING flOW
MAX No OF WORKING VALVES
SIZING flOW PER VALVE
113600
MOLECULAR WEIGHT
GAS CONSTANT 1544M
SYMBOl UNITS
Ps BARG
Po
P PSIA T1 DegC
T Oeg R
k WI Kg h A sqin Ac sqin W2 Kgh N
W Ib h w Ibsec M
R ftlblb Oeg
bull GRAVITY IQ ftS2
FI=
2 W RI
gPA
VALUE
7 10 F2
12635 256
9528 105
- shyFl
t~ --+
~ middotFI FI
t5489 rTABIJSmn Ow COiiOmON
2853 NOn IIQRIZOllTAL IOItCIS Kt MtA CEil
2853 15489 F2
1 341532 +shy948701 F3
885 174463 ltV AT POICONllIll0N
322 AampUMING IMPACT CTOII OYl
260496 Ib 1159 N
128894 Ib 573 N
520993 Ib 2318 N -
bullbull
SARASIN-lltJ l7Technical amp Calculation Data Sheet ZI 8olto R~62IKI _____ J40 11ap11M GnlCMl
VAlVH e COlTllOlS Safety Valve
e Bomel lype Opened
Project KHARG OLEfiN COMPLEX ~A
Tag No PSV 6 453A C-Quote Ref 3A30880IOOO Sales Engineer Abdeljalill Baigar W de Commande
Operating ondl tlons Connect ons
19 InlelON shy1 fluid type Superheated Stetlm
20 Inlet Finish ANSt600 RF (125-250 AARH) 2 Capacity 78500 Kglh 21 Outlet DN J Set ptesSUe br eft 22 Outlet Finish ANSI 150 ftF 1125-250 AARH) Ol$charoe Tom p J7S C Accordinn 10 ASME 616-5
5 Variable bad pressure 0 bar eft
Cold (If lest lXess 47 bar eft 8111 of material 7 Overpressure 11 () 16 floltfv SA216 wee
SA2115WCC2 Ylt8 Operating Pressure 40 bar eft
SA216 wee Tight Closing pressUIe (MAOP) 423 bar eft 26 NoWe Stllited AlSl410 1~ 27 174 PH Stainless SteelMechanical Tomp J7S middotC ~ 28 Gaskets Stalnl St1
29 SPfinQ Chromium Allov Steel 30 AlSI431c31 Adusitina Rlna SA351 CF3M 32 Stud Al1lQrB7 JJ Alt4i1r2H Accessories
Regular Levr 35 51etUted nozzl
ReqUIred Area 31 927 om Test Gag 495 s q InIl Selected Area 41 2 om
I 839 sq in 15 Onfice p
Reaction loroe DN~ t Flow capacity 101299 Kglh 18 Noise at 30 m acc to APt521 120 dB
apprO)flTlate noise level at 30 m according to API521 (mouth noiso) )perl dlsctlarge
Customer Name TECHNIP FRANCE evlslon ~ lion ate
890 4 20-juin-2005
Cust Item Numb 7U3F RFQ 1545-01 a ely a ype pflllg a a ely alve ea1T
I I J7 Standard API 520 I )
Commercial code S46P3530AmiddotDmiddotVMM I shyI Dimensions
A- 2254 mm B- 2540 mm W - 11800 mrnIA 525PlKd~KnKb Kshl ~ Welghl() s 1523 Kg I A- 89 Inch I bullB- 100 Inch
Dati 01 calcul w - 4115 Inch Mass Capaatv W 18500 KgIh Weight( ) 3357 Pound
P1 5553 bar abs r~ C Gase Constant 143843
() Indicative Values 0 now ooeIficient Kd 0915 0
Ksn 0865 Remarks Napier equation correction Kn 1
~ 2 valves are necessary 10 reach the required capacity
Back pressure correcUon Kb 1a BUlHmiddotup back pressureO 1 berg Same calculallO1 heet lor the 1st va lve and the spare one bull
N
~
GENERAl
PEO
PROCESS
CONDITONS
bull DESIGN
DATA
bull MATERIALS
I
OPT IONS
1 T Nu~
2 Service 3 Line NUrMer 4 P amp to Numbef
5 6 Conform to 961231EC 7 Fluid T
8 NJ licable rED Table 9
0 11
12
13
14
15 16
17 19
20 21 22
PED Cal
Fluid Fluid Servlc Required Capaci
MoltcullWe hI
ratln PrtSi ur
tlll TIm tUri
Badlt Prl$IIure
AJlovtabie Ova sure
Ov esslI10 FactOI Com esslbU Latenl Heal 01 V lion
o Tl 1012812005 Pour Commenta ires
Equipment
Fluid Groo
Fluid S~I
5 cltle Gl1Ivl Set Pressure
Col
HC+H20
15489
5 02
ReHov Temperatlyene 212
Constant Varia1je Total
23 Specific Hnt RItIo lC 24 Relief Densi
25 Relief Viscosity
26 Barometric Pressure 27 28 Nozzle Flit Semi
29 Design Saely Reflef Sale -Relief 30 Type Conventional BelloIN Plot Opefatad 31 BonnetT 32 n Code
33 Sizing Basis 34 Calcula ted Area
35 Selected Area 36 Orifice De nation
37 Size Rating -Inlel 38 Size Rat - Outlet
39 40 41 42 43 Stt 44 Fla es
45 Resilient Seat Seal 46 Guide
471 Spfing 46 Wtted Material
49 50
Bonnt Disc
Ri s Bellows
51 Cap Screwed or Bolted 52 Lever Plain or Packed 53 TestGag
54 55
22-ISV 3310 0 331fD332 SHCOO20150A1A 1 l -Q2S)(l2
y Gaseous Group 1
0 1
0
09
105
4
Note 10
k
C
k p
Safety Corrventlonal
hI Solted
ASME Delaut eau de refroldissement
1812 em
L 3 150 RF 450 RF
A2 16 WCB
NOlet A216WCB
NOle 1
Note 1
NOIot
NOIel
(Note 1
No
No
INSTRUMENT SPECIFICATION
Valve Safety Pressure Relief
oxicFlammable
GasIVapo
7
2564 C
A21 6WCB SS 316 Mini
Note 1
EJflt0nMobil Chemic
Sheet 5middot11 of 46
f
No 8 Date Revision Code 2831 No C3 1052 Amiddot163 1middottVOl Rev 0
i (
II Technical amp Calculation Data Sheet SARASIN-Agt Zllloa-R~
Safety Valve Nt BiOPUIle Gt1wtI bull bull 2110 1-1_
IN I ICustomer Name TECHNIP FRANCE
891 I 4 I bull s~ I
Cuslllem Numb 7273F RFQ 1545-01
Project KHARG OLEFIN COMPLEX I Opened
I 1 I
Quote Ref Tag No PSV pound I Nde Sales Abdeljalill Baigar I
I I uperatIng onaltons
Fluid ~e Superheated Steam 19 tnle ON shy
capaci ty 78500 Kgn 20 Inlet Finish ANSI 600 RF (125-250 AARH)
3 Set presMKC 21 Outlet ON
4935 bar eM 22 OtItlet Finish ANSI 150 RF (125-250 AARH)
DiSCharge Temp 375 middotC ASME B16-5 5 Variable back presslJe bull bar eft
Cold dilf lesc press 4935 bar eft I Bill 01 I
OverptesslKe B() 10 Bod SAl16 wee a Operating ProsslKe bar elf 24 Yoke SA216 wee
25 cabull SA216 weebull bull Tlglt Closing presSlKe (MAOP) 44 415 bar eff 26 Nozzle Sellited AlSI410 bullMlaquohBnIcaI Temp J15 C 21 Disc 174 PH Stilinless Steel 28 Gaskets Stainless $t1 bullSDOM Chromium Alloy Steel 30 Golde AlSI431 31 AcluslthQRinP SAl51 CF3M 32 Stud A183flr81 33 Nul Al94gr2H
gt0 Revulr Lever
Reqllif~ Afea 32023 om 35 middot SlelUted noule
12 496 sq in TU I Gag
1 Sellcl(l(l AIel 41 2 om
I 839 sq in Orirooe p
I ReactIon loree 3016 D I Flow capacity 100996 KgIh
I Noise ill 30 m ace to AP152 1 126 dB approxmate noise level at 30 m aCCOfding to APl521 (mtluth noise) open discharge
II 37 j API52 I I I
Commercial code S46P3530A-D-VMM I
IA= 525 PlKd~Kn KbKsh I I~-middot 2254 mm 2540 mm
11800 mm
bull 1523 Kg
lA shy 89 InCh
Dab 01 COI lcul I ~ - 100 Inch
IH- 465 Inch -jshyMa55 Capaoty W 18500 KgIh 3351 Pound -IP I 553 barabs C C-ase Constant 341143 I () Indicative Values 0 now coeffiCIent Kd 09150
N Ksh 0866 w- Napier equation coffeclion Kn bull 2 valves afe necessary to reach the required capacity lt Back Pfessure correcllon Kb
BUIItmiddotup back pressurecO 1 barg 2nd Ialve set at 05 of set pranure with 10 olelpreSSure in accordill1Ce With API 520
bullbulliii
bull 11 Load cases Ioad case combinations
The following load cases f load case combinations shall be analyzed 1) always or 2) on a casemiddot to-case basis
Static load cases for operating design and pressure test conditions
L6 jillL7 I
I --shy
I --shyI I I I I
L L
I Ll 9 L20
bull ~--
Load types (iC a pplicable load types should be added) W Dead weight (pipe weight + fluid weight + insulation weight) D Displacement T Design temperature P Design internal pressure U Uniform loads (eg snow load seismic load) F External forces (forces andor moments) HP Hydro test pressure H Hanger loads WIN Wind loads (for the main wind directions) WNC Dead weight without contents (pipe weight + insulation weight) WW Water-filled weight for pressure test
bull bull bull
bull
bull ~-
bull Techn ip
000
KHARG ETHYLENE PLANT KHARG Olefin Complex
CONTENT
2113
l Load C bullbullbull bull bull bullbullbullbullbullbullbullbullbullbullbullbull+ J
11 For Lines Carrying Heavy Fluid ( Hydropoundarboll Waler J I J2 For Lines Carrying Gas Steam or Vapnr + Jj For Unef Connected to Rotating Eqpm + 14 FOR LOW TEMPERATURE CARBON STEEL (LTCS) Error Bokak lot dJlUud
IA 1 Load Cases 10 be calculated to comply with ASME B3 13 Code ea I 15 S ao -I 8
2 CONFIGURAnON FILES USING CAESAR n+ 10
2 1 Unit System (7273F FIL)
22 Setup File ( CAESARCFG) 1 II
bull
bull
I
bull
bull
bull
Technip
KHARG ETHYLENE PLANT KHARG Olefin Complex
CONTRACTOR DOCUMENT N OWNER OCXUMENT Ndeg
p Ndeg Unil Doc T Matetlal coo Serial Ndeg Rev Pa B PIN Unit Doc T Malerial Code Serial Ndeg Rev Pa
7273F 3 13313
1 LOAD CASES
Loads and stress types to be considered in the computer analysis are
Loads Stress types
-W Deadweight - (EXP) EXPANSION
-WNC Weight (No Contents) - (SUS) SUSTAINED
- WW Weight full of water - (OPE) OPERATING
- P Pressure Set 1 bull (OCC) OCCASIONAL
-P2 Pressure Set 2
- T1 Thennal Set 1
- T2 Thermal Set 2
- T3 Thermal Set 3
- 01 D2 03 Displacements (thermal effect)
- Fl F2 F3 External Forces ( used for slug surge p~v and rupture disk) bull- H Spring hanger fqrces
- Ul U2 U3 Uniform Loads
- WIN Wind ~oad 1
-WIN2 WinCl Load 2
The following load cases description assume that all calculated cases are lineaf (Le no n linear restraints gaps or friction)
Combination loads in the computer analysis can be the following assumin the calibration toad 01 s rin han er ha b en detin in a revious run 137 and the value defined in the s readshee s rin hanger
Technip
bull KHARG ETHYLENE PLANT
KHARG Olefin Complex
7273F WI
Case
(OCC) Sustained plus Wind Z combined absolutely
11 For Lines Carrying Heavy Fluid (Hydrocarbon Water )
a - Example File 2_00CA_O_A (Unit 20 Calculation Number 001 Load Case File AIKev 0)
bull
exposed to wind hydrostatic test spring supports No Yes_No CASE I W+~I+IJ+PI+H (O~E) Operating
CASE 2 W+PI+H (SUS) Deadweight + Pressure
CASE 3 U I (OCC) Seismic Load X
CASE 4 U2 (OCC) Seismic Load Y
CASES U3 (OCC) Seismic Load Z
CASE 6 L1 -L2 (EXP) Expansion range Code Case
CASE 7 W +lA+L5 (OCC) Resultant seismic load SRSS combination
CASE8 L2+L7 (OCC) Suslalncd plus Seismic Combined Case
b - Example File 2_002_A_O_A (Unil 20 Calculation Number 002 Load Case File A
exposed to wind hydrostatic test spring supports Noy Ye
bull
CASE I W+D1+T1+Pl+H
CASE 2 W+Pl+H
CASE 3 WIN I
CASE4 WIN2
CASES UI
CASE6 U2
CASE 7 U3
CASE 8 LI -L2
CASE 9 L5+ L6+L 7
CASE 10 L2+L3
CASE II L2+lA
CASE 12 L2+L9
(OPE) Operang
(SUS) Deadweight + Pressure
(SUS) Wind along X (Instead or oce 10 avoid Snbbe ivoio~ irany)
(SUS) Wind along Z Onslead oroce to avoid Snubber ifi(lY)
(OCC) Seismic Load X
(OCC) Sesmc Load Y
(OCC) Seismic Load Z
(EXP) Expansion range Code Case
(OCC) Resultant seismic load SRSS combination
(OCC) Sustained plus Wind X combined absolutely
Case
(OCC) Sustained plus Seismic Combined absolutely Case
Technip
P eel N
7273F
KHARG ETHYLENE PLANT KHARG Olefin Complex
CONTRACTOR DOCUMENT Ndeg
Malellal Code Selia N Rev Pa p
1300 000 0 513
PETItOCHllMrCAL IN ST1UES DEVELOPMENT MANG MENT CO
OW NER DOCUMENT Ndeg
Material Code Serial Ndeg Rev Pa
513
12 For Lines Carrying Gas Steam or Vapor
bull
Examplelr~~~~~+-_ex~po_S_ed~0 ~nd_ ~Wi __~_h~yd_~__I~a~____tic es1-_s~pn_n~g~s~u~ppo~rts__~ Line criteria No shy Yes Yes
a - Example File 2_003_A_O_A File A RevD)
CASE I WNC+DI+TI+PI+H
CASE 2 WNC+PI+H
CASE3UI
CASE 4 U2
CASES U3
(Unit 20 Calculation Number 003 Operating Loa Cases
(OPE) Operating
(SUS) Deadweight (No contents) + Pressure PI
(OCC) Seismic Load X
(OCC) Se ismic Load Y
(ccq Seismic Load Z
CASE 6 LImiddotL2 (EXP) Expansion range Code Case
CASE 7 L3+L4+LS (CCe) R~sultant seismic load SRSS combination
CASE 8 L2+L7 (OCC) Sustalfled plus SeIsmic Combined absolutely C e Case
b Example File 2_003_B_O_A (Unot 20 Calculation Number 003 Hydrotest LcJCase Fi le B RevD) lftested in place
CASE I WW+PI (SUS) Deadweight Full of water + Hydrotest Pressure PI
bull 4 -gt fv
L1 --1- r
Igt 0
bull Technip
P ec(Ndeg
n73F
KHARG ETHYLENE PLANT KHARG Olefin Complex
CONTRACTOR DOCUMENT N
P N
613
PETROCHEMICAL IN USTRJpoundS DEVElOPMENT MANA EMENT CO
OWNER DOCUMENT Ndeg
Material Code Sertal Ndeg Rev Pa
613
Example 2 r-~~~~~~~XP~osed~to~w~i~nd~~h~~=r~ost~at=ic~t==st~~sp=n=n~g~su=ppo==rt=s~ line criteria Yes Yes Yes
a Example File S_OOS_A_Obullfi (Uuil50 Calculation Number 00) Operating Load Case Fi e ArevO) J7LLA A_A
CASE 1 WNC+QI+Tt+PI+H (OPE) Operating
CASE 2 WNC+PI+H
CASE 3 WIN I
CASE 4 WlN2
CASE 5 VI
CASE 6 U2
CASE 7V3
CASE 8 Ll -L2
CASE 9 L5+L6+L7
CASE 10 L2+L3-shyCASE II L2+L4
CASE 12 L2+L9
(SUS) Deadweight (No contents) + Pressure
(SUS) Wind along X (1nstcad oroce 10 avoid Snubber activatio if any)
(SUS) Wind along Z (Instead ofoce to avoid Snubberactivarion ifany)
(OCe) Seismic Load X
(OCC) Seismic Load Y
(OCC) Seismic Load Z
(EXP) Ex pansion range Code Case
(ocq Resultant seismic load SRSS combination gt
(OCe) Sustained plus Wind X combined absolutely C I Case
(OCC) Sustained plus Wind Z combined absolutely Codf Case
(aCe) Sustained plus Seismic Combined absolutely Cod Case
b Example File S_OOSJl_O bull A (Unit 5OCalculation Number 005Hydrostatic Load case fil B
revO) 4-OlL ~ _A_A
CASE 1 WW+PI (SUS) Deadweight full of water + Hydrotest Pressure PI
bull WI I bull AHa bull_ Amiddot KHARGJELOAOCASESOdDc
bull
bull
RevO)
CASE I W+PI +TI+DI+H
CASE 2 W+PI+T2+DI+H
CASE 3 W+PI+T3+DI+H
CASE 4 W+Pl+H
CASE 5 WNC+H
CASE6UI
CASE U2
CASE 8 U3
CASE 9 L6+L+L8
CASE 10 LimiddotL4
CASE I I L2middotL4
CASE 12 L3middotL4
CASE 13 L4+L9
Technip
KHARG ETHYLENE PLANT KHARG Olefin Complex
PET1IOCJiEMCAL INOUSTIUES DEVElOfMENT MANA EMENT co
7273F
Nmiddot UtIiI Doe T
1300 000 0 713
File A
1-1 For Lines Connected to Rotating Equipmenl
Example File 002_007 _A_O_A (Unit 002 Calculation Number 007 Load ea
(OPE)
(OPE)
(OPE)
(SUS)
(SUS)
(OCC)
(OCC)
(OCC)
Operating Pump A operating 380degC
Pump B Standby 21degC (Ambient)
Operating Pump B operating 380degC
Pump A Standby 21degC (Ambient)
Operating Pump A and B hot 380ltgtlt
Deadweight + Pressure
Weight (No contents)
Seismic X
Seismic Y
Seismic Z
(ocq Resultant seismic load SRSS combination
(EXP) Thermal T 1 Pump A operating 380degC
Pump B Standby 21degC (Ambient)
(EXP) ThennaJ 12 Pump B operating 380degC
Pump A Standby 21degC (Ambient)
(EXP) Therma1 13 Pump A and B hot 380degC
(OCC) Sustained plus Seismic Combined absolutely C e Case
Note Load Case 5 is used to calrulate shop calibration of spring support instaJled above pump nozzle
- - - -
bull Technip
KHARG ETHYLENE PLANT KHARG Olefin Complex
CONTRACTOR OOCUIoENT N OWNER DOCUMENT
P N IJnIt Doc T lMtecW eoo Serial N Rev P p unit Doe T Material Code Serial Rev P
7273F 000 WI 1300 000 0 813
131 Load Cases to be calculated to comply wjtb ASME 831 3 Code Cases
~xample
CASE I W+DI+TI+P I(OPE)Operaling CASE 2 W+Pl(SUS) Deadweight + Pressure
CASE 3 U I (OCC) Seismic Load X
CASE 4 U2(OCC) Seismic Load Y
CASE 5 U3(OCC) Seismic load Z
CASE 6 LI -L2(EXP) Expansion range Code Ca~
CASE 7 W+L4+L5(OCC) Resultanl seismic load SRSS combination
ASE 8 L2+L7(OCC) Sustained plus Seismic Combined absolutelyCode Case
CASE 9 LI+L7(OCC) Operating plus Seismic combined absolutely hOI restraint (Optional)
813
CASE 10 L9+~(OCC) Maximum restrai nt loads (Optional)~ 14 FOR LOW TEMPERATURE CARBON STEEL (LTCS)
141 Stress criteria
The point (3) of the figure 3232B imposes to take into account the following load cases
Permanent static loads
bull W Weight (signed load)
bull bull P Pressure (signed load)
bull T low Temperature (signed load)
bull F exlemal loads (signed load)
Occasional static and dynamic loads
bull U seismic accelerations Corresponding to the SASS combination of the Ul (X dyion) U2 (Y direction) and U3 (Z direction) components
bull WIN Wind (unsigned load)
Remarks
I) In Caesar load case it is necessary to have by load case line only one of load cases d~=ibed her-under
2) In Caesar input all stress intensification factors shal l be equal to 1
TIle criteria is
W + P +T + F + U or WIN lt O3Sh - 413 Mpa combined in ABS( ~ shy
bull
9113
Technip
bull KHARG ETHYLENE PLANT
KHARG Olefin Complex
QVoINEA OClCUME NT N
P bull p N Unit Doc T Malerial Code Serial Ndeg Rw
913
142 Examples
Examplelr-~__~~-+~e~x~po=s~ed~to~W~ind=-~~h~~~r~o~st=a=t~~te=s~t~=s~ ~ po~rt~s-+pr=ing~s~u~p~line criteria Yes Yes Yes
bull Example File 002_01O-A_O_A (Unit 002 Calculation Number OlD Load Case File A evD)
CASE 1 W+Tl+PI+H (OPE) Operating cold condition
CASE 2 W+T2+P2+H (OPE) Operating hot conditions
CASE 3 W+PI +H (SUS) Deadweight + Pressure
CASE 4 WINl (SUS) Wind along X (Instead of OCC to avoid Snubber activation if I y)
CASES WIN2 (SUS) Wind along Z (Instead of OCC to avoid Snubber activation if y)
CASE 6 Ul (OCC) Seismic Lcentad X
CASE 7 U2 (OCe) Seismic Load Y
CASES U3 (OCC) Seismic Load Z
CASE9W+H (SUS) Deadweight + Spring hanger
CASE 10 PI (SUS) Pressure
CASE J 1 Tl (EXP) Temperarure
CASE 12 LI -L2 (EXP) thermal stress range Code Case
CASE 13 Ll -L3 (EXP) thermal suess range Code Case
CASE 14 LlI+Ll2 (EXP) full thermal stress range checking ABS combination
CASE 15 L6+L7+LS (OCC) Resultant seismic load SRSS combination CASE 16 ~9+L10+L1I+L3 (OCC) Sustained plus Wind X combined absolutely Code Ease CASE 17 L9+LI0+L11+L4 (OCC) Sustained plus Wind Z combined absolutely Code tase CASE 18 L9+L10+Lll+L15 (OCC) Sustained plus Seismic Combined absolutely Code ase
bull
bull
bull
bull
bull
Technip
KHARG ETHYLENE PLANT KHARG Olefin Complex
COHTAACTOR DOCUMENT N
-~
PEJROCHEMICAI IES DBVELOPMENT MANAG co
OWNER DOCUMENT Ndeg Unit Doe T P N
7273F 000 WI 1300 006 813 1 813 1
8 SNOW WAD (Ws)
I Emiddot~middotv O
Snow loads shall 00 applied only for cold outside lines for which design T is below 0 C and which are not protected by floor equ ipment or others
The hereafter calculated vaJue (Ws) will be classed as unifonn load foUowing Y axis (U ) in a separate Caesar input file See 7273F_OOO_CN3_CN2_1370_SAMPLlC AXLS
Design snow load 25 kgll1l2
The distribution of snow remaining on the horizontal pipe will take the shape hereu dec a reducljon factor of 072 may be applied
Ws = ( lx 051gt In x h 022D ) 25
Ws = (Ix 072 x D ) 25
Ws = 18 x D Kflrsi= 180 x D NIP Where 0 = outside diameter of pipe o r outside diameter of pipe + insulation if exist( m)
70middot
9120
o
bull Technip -D KHARG ETHYLENE PLANT ~
KHARG Olefin Complex
middot INmiddot I A~ I P~ UNo I 7273F 000 WI 1300 I 006 I A I 115 I 115
APPENDIX IV
L bull WIND PRESSURE I ELEVATION
11 Wind Basic nata I Wind pressure calcuJation
As per Project Basic Engineering 7273F-30-PP-206 Bask Design Data
Basic wind speed 160km h (44 5 m s)
Exposure Category 0
According to UBC 97 the design wind loading shall be
p= CxCxqX
where
P =Design wind pressure allevel 10 III
C~ =156 at leve1 10 m (EIIposure and gust factor-Table I6-G)
Cq I for DNlt= 50 nun
= 08 for DNgt 50 mm (Exposure and gust factor-Table I6-H)
qs= 1226 kNm2 ( Wind stagnation pressure at 10 m -Table J6-F)
lw = 1 15 (Importance factor - Table 16-K)
p = 220 xC (kNl m)
Height Above Wind pressure Ground Level
(m) PI eq (kNlm2 )
Oto 10 22
10 (0 20 247
20 to 30 264
30 10 40 276
40 to 50 286
50 to 60 289
60 to 70 293
70 1080 299
80 to 90 312
bull
bull
bull
bull
CONTRACTOR OOCUIENT bull N UniI Doc T Milttl CoOl srI N Rev Pa p
7273F 000 WI 1300 000 0 ()J 13
2 CONFIGURATION FILES USING CAESAR II
21 Unit System (7273FFIL)
CAE S A R liVERS 430
INPUT UNITS USED
UNITS 7273F NOMISCH INPUT ON
LENGTH inches
FORCE pounds
MASS(dynamics) pounds
MOMENTS(INPUn inch-pounds
MOMENTS(OUTPUT) inch-pounds
STRESS Ibssqin
TEMP SCALE degrees F
PRESSURE psig
ELASTIC MODULUS Ibslsqin
PI PE DENSITY Ibslcuin
INSULATION DENS Ibslcuin
FLUID DENSITY Ibslcuin
TRANSL STI F Ibslin
ROTATIONAL STiF inlbldeg
UNIFORM LOAD Jblin
GLOAD gs
WIND LOAD IbsJsqin
ELEVATION inches
COMPOUND LENGTH inches
DIAMETER inches
WALL THICKNESS inches
OWNER DOCUMENT Ndeg
~ Doc T Malerial CoOa Serial Ndeg Rev
1013
x 25400 mm
x 4448 N
x 0454 kg
x 0113 Nm
x 0113 Nm
x 0007 MPa
x 0556 C
x 0069 bars
x 0007 MPa
x 27680000 kgCrmiddotm
x 27680000 kgJcum
x 27680000 kgci m
x 0175 Nm
x 0113
l x 175127 NJm
x 1000 gs
x 6894757 NJ m
x 0025 m
x 25400 mm
x 1000 inch
x 25400 mm
bull bull
Technip
KHARG ETHYLENE PLANT KHARG Olefin Complex
PETROCHlMlCAL IND JES DIiVElOPMENT MANGEMENT CO
11113
Technip bull
KHARG ETHYLENE PLANT ~ KHARG Olefin Complex
iETltOCHEMICtl OEVEIOPMENT MANArCO
CONTRACTOR DOCUMENT N OWNER DOCUMENT Nmiddot ProIecl N p U Doe TwalMrolerial Code ISen N ReI P_ Proiect N I UNt Doo T~ I ~eriIII Code
7273F 000 WI I 1300 I 000 I 0 I 11113 I I I
22 Setup File ( CAESARCFG )
C A E SAR II VERS450
SETUP FILE PARAMETERS
CONNECT GEOMETRY THRU CNODES YES I MIN ALLOWED BEND ANGLE 500000 I MAXjLLOWED BEND ANGLE bull 135000 I BEND LENGTH ATIACHMENT PERCENT 100000 I MINjNGLE TO ADJACENT BEND PT 500000
LOOP CLOSURE TOLERANCE 254000mm
THERMAL BOWING HORZ TOLERANCE 100000E-04
AUTO NODE NUMBER INCREMENT 100000
ZJXIS UP NO
USE PRESSURE STIFFENING DEFAULT
ALPHA TOLERANCE 500000E-02
RESLDmiddotFORCE NO
HGR_DEF RESWGT STIF
bull 01751200E+12 Nlmm
DECOMP SNG TOL 01 OOOOOOE+ 11
BEND_AXIAL SHAPE NO
FRICT STIF 875600 Ni mm I FRICT NORM FORCE VAR 025000 I FRICT ANGLE VAR 300000 I FRICT SLIDE MULT 100000
ROD TOLERANCE 100000
ROD INC 200000
INCORE NUMERICAL CHECK NO
OUTCORE NUMERICAL CHECK NO
DEFAULT TRANS RESTRAINT STIFF 0175120E+12 Nlmm
DEFAULT ROT RESTRAINT STIFF 0112980E+12 Nmi deaJ
IGNORE SPRING HANGER STIFFNESS bull NO I
WI I middot AiHG bull _ KtVRCUE LOoO CAS ES_Odoc
rmiddot
bull
bull
Technip
KHARG ETHYLENE PLANT KHARG Olefin Complex
Setup File (
CONNECT_GEOMETRY _ THRU_CNODES
WRC-07 VERSION
WRC- 07
DEFAULT
831
WI I middot AIlaquo) Amiddot KHARGJUOAD CASFsOdoc
T
F
YES
NO
181 281
NO
DEFAULT
02206272E+OSbull
bullbull
bull
bull
Thchnip bull
KHARG ETHYLENE PLANT ~ KHARG Olefin Complex
PFffiOCHEMICAL INO bull DEVELOPMENT MANAG ~ENTCO_
CONTRACTOR DOCUMENT Ndeg OWNER DOCUMENT N
Proioct Ndeg Unit Doc TIIDEII Material Code Serial Ndeg Rev I Paae Proiect N Unit Doc Type Material Code Serial N A~ 7273F I 000 I WI I 1300 I 000 I a I 13 13 I 1313
FRP Ratio GmodlEmo(Uaxial) O2500000E+OO
FRP EalEhVhla O1527272E+OO
SetuD File (CAESARCFG Continuation)
FRP Lamina1e Type THREE
FRP Alpha O2159827E+02 C
FRP Density O1660800E+04 kocum bullEXCLUDE 12 FROM UKOOA BENDI NG NO
OUTPUT REPORTS BY LOAD CASE YES
DISPLACEMENT NODAL SORTING YES
DYNAMIC INPUT EXAMPLE TEXT MAX
TIME HIST ANIMATE YES
ENABLE AUTOSAVE YES
AUTOSAVE TIME INTERVAL O3000000E+02
PROMPTED AUTOSAVE YES
DISABLE UNDOREDO NO
STRUCTURAL DATABASE AISC89BIN
VALVE amp FLANGE GENERIC VHD
EXPANSION JT DBASE FLEXPATHJHD
PI PING SIZE SPECIFICATION ANSI
DEFAULT SPRING HANGER TABLE O5000000E+01
SYSTEM DIRECTORY NAME SYSTEM
UNITS FILE NAME 7273FFIL
ENABLE ODBC OUTPUT NO
DEFAULT SPRING HANGER TABLE LlSEGA
- bull -
WI 1 ANG bull IV IlHAAG_IELOAD CAS ES_OdOC
SRMPL6 LOf]) C(15euro5 S V REfK Ti O-l FOeC e- JlUE TO PSv oPttvlNG
bull Sldlle Aymmiddot [CIDO(UMpoundNTS AllD SETIINGSVhBACONI7173FmiddotMBACONICAESAR FILESICNj016_REV ~
bull
bull
bull
Edt
+ t
loadCose Edlcr LoadCoseOptiom Loads WlNeLoads
loads Oefned n IrtJIA loed Casu Stress Type
W -Woltllt L1 W+D1 +T1 +P1 +H Of 01 middot Displcmnt Case ~ L2 wO-iT2+P1 +H-- Of T1 middot Thermal Case tn l3 W~D1~T3~P1H ~(]S-oiit~~ Of LltgtOd e T2 Thermal Case 2 -- - _- ------- -__- T3 Thermal Case U3
l4 W+P1+H SUS __ _- -----PI middot Pr euUle Case 1 LS Wt-P1t-H-t-F1 OCC Hp middot Hydlo Prenae L6 Ul OCC --- ---- _----- H middot Hanger l oads 17 U2 OCC UI middot Unf Load eMe 11 La U3 OCC U2 -UriloodlAse 12 L9 F1 OCC U3 Uri l oad Case 13 L10 L1-l4 EXP F1 middot Cone FOIct Case 11 1 Ll1 L2-l4 J EXP Vlllet Fled W WNC middot W~ no corieris L12 L3-lS EXP
L13 LS+l7+l8 OCC L1 4 L-4+l13 ----l ~~ IL15 L1 lt-l1 3 L1 6 LJl9 (fD lO(ll ch 011 (f~tnlh OCC
STATIQUE LoR)) I- Ill
1
FW FRANCE NDG SHT16F I
CliENT
PROJECT
CPNo
EXXON
18KTA E5000 Expansion
CALCNo ISV 3310
CALC BY BEP
CHKD BY
DATE 13012006
RELIEF VALVE LOADINGS vapour
RV Nos ISV 3310
SIZE 4x3
RATING 150xlSO
ORIFICE L
bull DATA DESCRIPTION
RV SET PRESSURE
PERCENT OVERPRESSURE
Ps (l+PolOO) + 147
REliEF TEMPERATURE
1195492
RATIO OF SPECIFIC HEATS SIZING FLOW
SElECTED ORIFICE AREA
CALCULATED ORIFICE AREA
FACTORED SIZING flOW
MAX No OF WORKING VALVES
SIZING flOW PER VALVE
113600
MOLECULAR WEIGHT
GAS CONSTANT 1544M
SYMBOl UNITS
Ps BARG
Po
P PSIA T1 DegC
T Oeg R
k WI Kg h A sqin Ac sqin W2 Kgh N
W Ib h w Ibsec M
R ftlblb Oeg
bull GRAVITY IQ ftS2
FI=
2 W RI
gPA
VALUE
7 10 F2
12635 256
9528 105
- shyFl
t~ --+
~ middotFI FI
t5489 rTABIJSmn Ow COiiOmON
2853 NOn IIQRIZOllTAL IOItCIS Kt MtA CEil
2853 15489 F2
1 341532 +shy948701 F3
885 174463 ltV AT POICONllIll0N
322 AampUMING IMPACT CTOII OYl
260496 Ib 1159 N
128894 Ib 573 N
520993 Ib 2318 N -
bullbull
SARASIN-lltJ l7Technical amp Calculation Data Sheet ZI 8olto R~62IKI _____ J40 11ap11M GnlCMl
VAlVH e COlTllOlS Safety Valve
e Bomel lype Opened
Project KHARG OLEfiN COMPLEX ~A
Tag No PSV 6 453A C-Quote Ref 3A30880IOOO Sales Engineer Abdeljalill Baigar W de Commande
Operating ondl tlons Connect ons
19 InlelON shy1 fluid type Superheated Stetlm
20 Inlet Finish ANSt600 RF (125-250 AARH) 2 Capacity 78500 Kglh 21 Outlet DN J Set ptesSUe br eft 22 Outlet Finish ANSI 150 ftF 1125-250 AARH) Ol$charoe Tom p J7S C Accordinn 10 ASME 616-5
5 Variable bad pressure 0 bar eft
Cold (If lest lXess 47 bar eft 8111 of material 7 Overpressure 11 () 16 floltfv SA216 wee
SA2115WCC2 Ylt8 Operating Pressure 40 bar eft
SA216 wee Tight Closing pressUIe (MAOP) 423 bar eft 26 NoWe Stllited AlSl410 1~ 27 174 PH Stainless SteelMechanical Tomp J7S middotC ~ 28 Gaskets Stalnl St1
29 SPfinQ Chromium Allov Steel 30 AlSI431c31 Adusitina Rlna SA351 CF3M 32 Stud Al1lQrB7 JJ Alt4i1r2H Accessories
Regular Levr 35 51etUted nozzl
ReqUIred Area 31 927 om Test Gag 495 s q InIl Selected Area 41 2 om
I 839 sq in 15 Onfice p
Reaction loroe DN~ t Flow capacity 101299 Kglh 18 Noise at 30 m acc to APt521 120 dB
apprO)flTlate noise level at 30 m according to API521 (mouth noiso) )perl dlsctlarge
Customer Name TECHNIP FRANCE evlslon ~ lion ate
890 4 20-juin-2005
Cust Item Numb 7U3F RFQ 1545-01 a ely a ype pflllg a a ely alve ea1T
I I J7 Standard API 520 I )
Commercial code S46P3530AmiddotDmiddotVMM I shyI Dimensions
A- 2254 mm B- 2540 mm W - 11800 mrnIA 525PlKd~KnKb Kshl ~ Welghl() s 1523 Kg I A- 89 Inch I bullB- 100 Inch
Dati 01 calcul w - 4115 Inch Mass Capaatv W 18500 KgIh Weight( ) 3357 Pound
P1 5553 bar abs r~ C Gase Constant 143843
() Indicative Values 0 now ooeIficient Kd 0915 0
Ksn 0865 Remarks Napier equation correction Kn 1
~ 2 valves are necessary 10 reach the required capacity
Back pressure correcUon Kb 1a BUlHmiddotup back pressureO 1 berg Same calculallO1 heet lor the 1st va lve and the spare one bull
N
~
GENERAl
PEO
PROCESS
CONDITONS
bull DESIGN
DATA
bull MATERIALS
I
OPT IONS
1 T Nu~
2 Service 3 Line NUrMer 4 P amp to Numbef
5 6 Conform to 961231EC 7 Fluid T
8 NJ licable rED Table 9
0 11
12
13
14
15 16
17 19
20 21 22
PED Cal
Fluid Fluid Servlc Required Capaci
MoltcullWe hI
ratln PrtSi ur
tlll TIm tUri
Badlt Prl$IIure
AJlovtabie Ova sure
Ov esslI10 FactOI Com esslbU Latenl Heal 01 V lion
o Tl 1012812005 Pour Commenta ires
Equipment
Fluid Groo
Fluid S~I
5 cltle Gl1Ivl Set Pressure
Col
HC+H20
15489
5 02
ReHov Temperatlyene 212
Constant Varia1je Total
23 Specific Hnt RItIo lC 24 Relief Densi
25 Relief Viscosity
26 Barometric Pressure 27 28 Nozzle Flit Semi
29 Design Saely Reflef Sale -Relief 30 Type Conventional BelloIN Plot Opefatad 31 BonnetT 32 n Code
33 Sizing Basis 34 Calcula ted Area
35 Selected Area 36 Orifice De nation
37 Size Rating -Inlel 38 Size Rat - Outlet
39 40 41 42 43 Stt 44 Fla es
45 Resilient Seat Seal 46 Guide
471 Spfing 46 Wtted Material
49 50
Bonnt Disc
Ri s Bellows
51 Cap Screwed or Bolted 52 Lever Plain or Packed 53 TestGag
54 55
22-ISV 3310 0 331fD332 SHCOO20150A1A 1 l -Q2S)(l2
y Gaseous Group 1
0 1
0
09
105
4
Note 10
k
C
k p
Safety Corrventlonal
hI Solted
ASME Delaut eau de refroldissement
1812 em
L 3 150 RF 450 RF
A2 16 WCB
NOlet A216WCB
NOle 1
Note 1
NOIot
NOIel
(Note 1
No
No
INSTRUMENT SPECIFICATION
Valve Safety Pressure Relief
oxicFlammable
GasIVapo
7
2564 C
A21 6WCB SS 316 Mini
Note 1
EJflt0nMobil Chemic
Sheet 5middot11 of 46
f
No 8 Date Revision Code 2831 No C3 1052 Amiddot163 1middottVOl Rev 0
i (
II Technical amp Calculation Data Sheet SARASIN-Agt Zllloa-R~
Safety Valve Nt BiOPUIle Gt1wtI bull bull 2110 1-1_
IN I ICustomer Name TECHNIP FRANCE
891 I 4 I bull s~ I
Cuslllem Numb 7273F RFQ 1545-01
Project KHARG OLEFIN COMPLEX I Opened
I 1 I
Quote Ref Tag No PSV pound I Nde Sales Abdeljalill Baigar I
I I uperatIng onaltons
Fluid ~e Superheated Steam 19 tnle ON shy
capaci ty 78500 Kgn 20 Inlet Finish ANSI 600 RF (125-250 AARH)
3 Set presMKC 21 Outlet ON
4935 bar eM 22 OtItlet Finish ANSI 150 RF (125-250 AARH)
DiSCharge Temp 375 middotC ASME B16-5 5 Variable back presslJe bull bar eft
Cold dilf lesc press 4935 bar eft I Bill 01 I
OverptesslKe B() 10 Bod SAl16 wee a Operating ProsslKe bar elf 24 Yoke SA216 wee
25 cabull SA216 weebull bull Tlglt Closing presSlKe (MAOP) 44 415 bar eff 26 Nozzle Sellited AlSI410 bullMlaquohBnIcaI Temp J15 C 21 Disc 174 PH Stilinless Steel 28 Gaskets Stainless $t1 bullSDOM Chromium Alloy Steel 30 Golde AlSI431 31 AcluslthQRinP SAl51 CF3M 32 Stud A183flr81 33 Nul Al94gr2H
gt0 Revulr Lever
Reqllif~ Afea 32023 om 35 middot SlelUted noule
12 496 sq in TU I Gag
1 Sellcl(l(l AIel 41 2 om
I 839 sq in Orirooe p
I ReactIon loree 3016 D I Flow capacity 100996 KgIh
I Noise ill 30 m ace to AP152 1 126 dB approxmate noise level at 30 m aCCOfding to APl521 (mtluth noise) open discharge
II 37 j API52 I I I
Commercial code S46P3530A-D-VMM I
IA= 525 PlKd~Kn KbKsh I I~-middot 2254 mm 2540 mm
11800 mm
bull 1523 Kg
lA shy 89 InCh
Dab 01 COI lcul I ~ - 100 Inch
IH- 465 Inch -jshyMa55 Capaoty W 18500 KgIh 3351 Pound -IP I 553 barabs C C-ase Constant 341143 I () Indicative Values 0 now coeffiCIent Kd 09150
N Ksh 0866 w- Napier equation coffeclion Kn bull 2 valves afe necessary to reach the required capacity lt Back Pfessure correcllon Kb
BUIItmiddotup back pressurecO 1 barg 2nd Ialve set at 05 of set pranure with 10 olelpreSSure in accordill1Ce With API 520
bullbulliii
bull 11 Load cases Ioad case combinations
The following load cases f load case combinations shall be analyzed 1) always or 2) on a casemiddot to-case basis
Static load cases for operating design and pressure test conditions
L6 jillL7 I
I --shy
I --shyI I I I I
L L
I Ll 9 L20
bull ~--
Load types (iC a pplicable load types should be added) W Dead weight (pipe weight + fluid weight + insulation weight) D Displacement T Design temperature P Design internal pressure U Uniform loads (eg snow load seismic load) F External forces (forces andor moments) HP Hydro test pressure H Hanger loads WIN Wind loads (for the main wind directions) WNC Dead weight without contents (pipe weight + insulation weight) WW Water-filled weight for pressure test
bull bull bull
bull
bull ~-
I
bull
bull
bull
Technip
KHARG ETHYLENE PLANT KHARG Olefin Complex
CONTRACTOR DOCUMENT N OWNER OCXUMENT Ndeg
p Ndeg Unil Doc T Matetlal coo Serial Ndeg Rev Pa B PIN Unit Doc T Malerial Code Serial Ndeg Rev Pa
7273F 3 13313
1 LOAD CASES
Loads and stress types to be considered in the computer analysis are
Loads Stress types
-W Deadweight - (EXP) EXPANSION
-WNC Weight (No Contents) - (SUS) SUSTAINED
- WW Weight full of water - (OPE) OPERATING
- P Pressure Set 1 bull (OCC) OCCASIONAL
-P2 Pressure Set 2
- T1 Thennal Set 1
- T2 Thermal Set 2
- T3 Thermal Set 3
- 01 D2 03 Displacements (thermal effect)
- Fl F2 F3 External Forces ( used for slug surge p~v and rupture disk) bull- H Spring hanger fqrces
- Ul U2 U3 Uniform Loads
- WIN Wind ~oad 1
-WIN2 WinCl Load 2
The following load cases description assume that all calculated cases are lineaf (Le no n linear restraints gaps or friction)
Combination loads in the computer analysis can be the following assumin the calibration toad 01 s rin han er ha b en detin in a revious run 137 and the value defined in the s readshee s rin hanger
Technip
bull KHARG ETHYLENE PLANT
KHARG Olefin Complex
7273F WI
Case
(OCC) Sustained plus Wind Z combined absolutely
11 For Lines Carrying Heavy Fluid (Hydrocarbon Water )
a - Example File 2_00CA_O_A (Unit 20 Calculation Number 001 Load Case File AIKev 0)
bull
exposed to wind hydrostatic test spring supports No Yes_No CASE I W+~I+IJ+PI+H (O~E) Operating
CASE 2 W+PI+H (SUS) Deadweight + Pressure
CASE 3 U I (OCC) Seismic Load X
CASE 4 U2 (OCC) Seismic Load Y
CASES U3 (OCC) Seismic Load Z
CASE 6 L1 -L2 (EXP) Expansion range Code Case
CASE 7 W +lA+L5 (OCC) Resultant seismic load SRSS combination
CASE8 L2+L7 (OCC) Suslalncd plus Seismic Combined Case
b - Example File 2_002_A_O_A (Unil 20 Calculation Number 002 Load Case File A
exposed to wind hydrostatic test spring supports Noy Ye
bull
CASE I W+D1+T1+Pl+H
CASE 2 W+Pl+H
CASE 3 WIN I
CASE4 WIN2
CASES UI
CASE6 U2
CASE 7 U3
CASE 8 LI -L2
CASE 9 L5+ L6+L 7
CASE 10 L2+L3
CASE II L2+lA
CASE 12 L2+L9
(OPE) Operang
(SUS) Deadweight + Pressure
(SUS) Wind along X (Instead or oce 10 avoid Snbbe ivoio~ irany)
(SUS) Wind along Z Onslead oroce to avoid Snubber ifi(lY)
(OCC) Seismic Load X
(OCC) Sesmc Load Y
(OCC) Seismic Load Z
(EXP) Expansion range Code Case
(OCC) Resultant seismic load SRSS combination
(OCC) Sustained plus Wind X combined absolutely
Case
(OCC) Sustained plus Seismic Combined absolutely Case
Technip
P eel N
7273F
KHARG ETHYLENE PLANT KHARG Olefin Complex
CONTRACTOR DOCUMENT Ndeg
Malellal Code Selia N Rev Pa p
1300 000 0 513
PETItOCHllMrCAL IN ST1UES DEVELOPMENT MANG MENT CO
OW NER DOCUMENT Ndeg
Material Code Serial Ndeg Rev Pa
513
12 For Lines Carrying Gas Steam or Vapor
bull
Examplelr~~~~~+-_ex~po_S_ed~0 ~nd_ ~Wi __~_h~yd_~__I~a~____tic es1-_s~pn_n~g~s~u~ppo~rts__~ Line criteria No shy Yes Yes
a - Example File 2_003_A_O_A File A RevD)
CASE I WNC+DI+TI+PI+H
CASE 2 WNC+PI+H
CASE3UI
CASE 4 U2
CASES U3
(Unit 20 Calculation Number 003 Operating Loa Cases
(OPE) Operating
(SUS) Deadweight (No contents) + Pressure PI
(OCC) Seismic Load X
(OCC) Se ismic Load Y
(ccq Seismic Load Z
CASE 6 LImiddotL2 (EXP) Expansion range Code Case
CASE 7 L3+L4+LS (CCe) R~sultant seismic load SRSS combination
CASE 8 L2+L7 (OCC) Sustalfled plus SeIsmic Combined absolutely C e Case
b Example File 2_003_B_O_A (Unot 20 Calculation Number 003 Hydrotest LcJCase Fi le B RevD) lftested in place
CASE I WW+PI (SUS) Deadweight Full of water + Hydrotest Pressure PI
bull 4 -gt fv
L1 --1- r
Igt 0
bull Technip
P ec(Ndeg
n73F
KHARG ETHYLENE PLANT KHARG Olefin Complex
CONTRACTOR DOCUMENT N
P N
613
PETROCHEMICAL IN USTRJpoundS DEVElOPMENT MANA EMENT CO
OWNER DOCUMENT Ndeg
Material Code Sertal Ndeg Rev Pa
613
Example 2 r-~~~~~~~XP~osed~to~w~i~nd~~h~~=r~ost~at=ic~t==st~~sp=n=n~g~su=ppo==rt=s~ line criteria Yes Yes Yes
a Example File S_OOS_A_Obullfi (Uuil50 Calculation Number 00) Operating Load Case Fi e ArevO) J7LLA A_A
CASE 1 WNC+QI+Tt+PI+H (OPE) Operating
CASE 2 WNC+PI+H
CASE 3 WIN I
CASE 4 WlN2
CASE 5 VI
CASE 6 U2
CASE 7V3
CASE 8 Ll -L2
CASE 9 L5+L6+L7
CASE 10 L2+L3-shyCASE II L2+L4
CASE 12 L2+L9
(SUS) Deadweight (No contents) + Pressure
(SUS) Wind along X (1nstcad oroce 10 avoid Snubber activatio if any)
(SUS) Wind along Z (Instead ofoce to avoid Snubberactivarion ifany)
(OCe) Seismic Load X
(OCC) Seismic Load Y
(OCC) Seismic Load Z
(EXP) Ex pansion range Code Case
(ocq Resultant seismic load SRSS combination gt
(OCe) Sustained plus Wind X combined absolutely C I Case
(OCC) Sustained plus Wind Z combined absolutely Codf Case
(aCe) Sustained plus Seismic Combined absolutely Cod Case
b Example File S_OOSJl_O bull A (Unit 5OCalculation Number 005Hydrostatic Load case fil B
revO) 4-OlL ~ _A_A
CASE 1 WW+PI (SUS) Deadweight full of water + Hydrotest Pressure PI
bull WI I bull AHa bull_ Amiddot KHARGJELOAOCASESOdDc
bull
bull
RevO)
CASE I W+PI +TI+DI+H
CASE 2 W+PI+T2+DI+H
CASE 3 W+PI+T3+DI+H
CASE 4 W+Pl+H
CASE 5 WNC+H
CASE6UI
CASE U2
CASE 8 U3
CASE 9 L6+L+L8
CASE 10 LimiddotL4
CASE I I L2middotL4
CASE 12 L3middotL4
CASE 13 L4+L9
Technip
KHARG ETHYLENE PLANT KHARG Olefin Complex
PET1IOCJiEMCAL INOUSTIUES DEVElOfMENT MANA EMENT co
7273F
Nmiddot UtIiI Doe T
1300 000 0 713
File A
1-1 For Lines Connected to Rotating Equipmenl
Example File 002_007 _A_O_A (Unit 002 Calculation Number 007 Load ea
(OPE)
(OPE)
(OPE)
(SUS)
(SUS)
(OCC)
(OCC)
(OCC)
Operating Pump A operating 380degC
Pump B Standby 21degC (Ambient)
Operating Pump B operating 380degC
Pump A Standby 21degC (Ambient)
Operating Pump A and B hot 380ltgtlt
Deadweight + Pressure
Weight (No contents)
Seismic X
Seismic Y
Seismic Z
(ocq Resultant seismic load SRSS combination
(EXP) Thermal T 1 Pump A operating 380degC
Pump B Standby 21degC (Ambient)
(EXP) ThennaJ 12 Pump B operating 380degC
Pump A Standby 21degC (Ambient)
(EXP) Therma1 13 Pump A and B hot 380degC
(OCC) Sustained plus Seismic Combined absolutely C e Case
Note Load Case 5 is used to calrulate shop calibration of spring support instaJled above pump nozzle
- - - -
bull Technip
KHARG ETHYLENE PLANT KHARG Olefin Complex
CONTRACTOR OOCUIoENT N OWNER DOCUMENT
P N IJnIt Doc T lMtecW eoo Serial N Rev P p unit Doe T Material Code Serial Rev P
7273F 000 WI 1300 000 0 813
131 Load Cases to be calculated to comply wjtb ASME 831 3 Code Cases
~xample
CASE I W+DI+TI+P I(OPE)Operaling CASE 2 W+Pl(SUS) Deadweight + Pressure
CASE 3 U I (OCC) Seismic Load X
CASE 4 U2(OCC) Seismic Load Y
CASE 5 U3(OCC) Seismic load Z
CASE 6 LI -L2(EXP) Expansion range Code Ca~
CASE 7 W+L4+L5(OCC) Resultanl seismic load SRSS combination
ASE 8 L2+L7(OCC) Sustained plus Seismic Combined absolutelyCode Case
CASE 9 LI+L7(OCC) Operating plus Seismic combined absolutely hOI restraint (Optional)
813
CASE 10 L9+~(OCC) Maximum restrai nt loads (Optional)~ 14 FOR LOW TEMPERATURE CARBON STEEL (LTCS)
141 Stress criteria
The point (3) of the figure 3232B imposes to take into account the following load cases
Permanent static loads
bull W Weight (signed load)
bull bull P Pressure (signed load)
bull T low Temperature (signed load)
bull F exlemal loads (signed load)
Occasional static and dynamic loads
bull U seismic accelerations Corresponding to the SASS combination of the Ul (X dyion) U2 (Y direction) and U3 (Z direction) components
bull WIN Wind (unsigned load)
Remarks
I) In Caesar load case it is necessary to have by load case line only one of load cases d~=ibed her-under
2) In Caesar input all stress intensification factors shal l be equal to 1
TIle criteria is
W + P +T + F + U or WIN lt O3Sh - 413 Mpa combined in ABS( ~ shy
bull
9113
Technip
bull KHARG ETHYLENE PLANT
KHARG Olefin Complex
QVoINEA OClCUME NT N
P bull p N Unit Doc T Malerial Code Serial Ndeg Rw
913
142 Examples
Examplelr-~__~~-+~e~x~po=s~ed~to~W~ind=-~~h~~~r~o~st=a=t~~te=s~t~=s~ ~ po~rt~s-+pr=ing~s~u~p~line criteria Yes Yes Yes
bull Example File 002_01O-A_O_A (Unit 002 Calculation Number OlD Load Case File A evD)
CASE 1 W+Tl+PI+H (OPE) Operating cold condition
CASE 2 W+T2+P2+H (OPE) Operating hot conditions
CASE 3 W+PI +H (SUS) Deadweight + Pressure
CASE 4 WINl (SUS) Wind along X (Instead of OCC to avoid Snubber activation if I y)
CASES WIN2 (SUS) Wind along Z (Instead of OCC to avoid Snubber activation if y)
CASE 6 Ul (OCC) Seismic Lcentad X
CASE 7 U2 (OCe) Seismic Load Y
CASES U3 (OCC) Seismic Load Z
CASE9W+H (SUS) Deadweight + Spring hanger
CASE 10 PI (SUS) Pressure
CASE J 1 Tl (EXP) Temperarure
CASE 12 LI -L2 (EXP) thermal stress range Code Case
CASE 13 Ll -L3 (EXP) thermal suess range Code Case
CASE 14 LlI+Ll2 (EXP) full thermal stress range checking ABS combination
CASE 15 L6+L7+LS (OCC) Resultant seismic load SRSS combination CASE 16 ~9+L10+L1I+L3 (OCC) Sustained plus Wind X combined absolutely Code Ease CASE 17 L9+LI0+L11+L4 (OCC) Sustained plus Wind Z combined absolutely Code tase CASE 18 L9+L10+Lll+L15 (OCC) Sustained plus Seismic Combined absolutely Code ase
bull
bull
bull
bull
bull
Technip
KHARG ETHYLENE PLANT KHARG Olefin Complex
COHTAACTOR DOCUMENT N
-~
PEJROCHEMICAI IES DBVELOPMENT MANAG co
OWNER DOCUMENT Ndeg Unit Doe T P N
7273F 000 WI 1300 006 813 1 813 1
8 SNOW WAD (Ws)
I Emiddot~middotv O
Snow loads shall 00 applied only for cold outside lines for which design T is below 0 C and which are not protected by floor equ ipment or others
The hereafter calculated vaJue (Ws) will be classed as unifonn load foUowing Y axis (U ) in a separate Caesar input file See 7273F_OOO_CN3_CN2_1370_SAMPLlC AXLS
Design snow load 25 kgll1l2
The distribution of snow remaining on the horizontal pipe will take the shape hereu dec a reducljon factor of 072 may be applied
Ws = ( lx 051gt In x h 022D ) 25
Ws = (Ix 072 x D ) 25
Ws = 18 x D Kflrsi= 180 x D NIP Where 0 = outside diameter of pipe o r outside diameter of pipe + insulation if exist( m)
70middot
9120
o
bull Technip -D KHARG ETHYLENE PLANT ~
KHARG Olefin Complex
middot INmiddot I A~ I P~ UNo I 7273F 000 WI 1300 I 006 I A I 115 I 115
APPENDIX IV
L bull WIND PRESSURE I ELEVATION
11 Wind Basic nata I Wind pressure calcuJation
As per Project Basic Engineering 7273F-30-PP-206 Bask Design Data
Basic wind speed 160km h (44 5 m s)
Exposure Category 0
According to UBC 97 the design wind loading shall be
p= CxCxqX
where
P =Design wind pressure allevel 10 III
C~ =156 at leve1 10 m (EIIposure and gust factor-Table I6-G)
Cq I for DNlt= 50 nun
= 08 for DNgt 50 mm (Exposure and gust factor-Table I6-H)
qs= 1226 kNm2 ( Wind stagnation pressure at 10 m -Table J6-F)
lw = 1 15 (Importance factor - Table 16-K)
p = 220 xC (kNl m)
Height Above Wind pressure Ground Level
(m) PI eq (kNlm2 )
Oto 10 22
10 (0 20 247
20 to 30 264
30 10 40 276
40 to 50 286
50 to 60 289
60 to 70 293
70 1080 299
80 to 90 312
bull
bull
bull
bull
CONTRACTOR OOCUIENT bull N UniI Doc T Milttl CoOl srI N Rev Pa p
7273F 000 WI 1300 000 0 ()J 13
2 CONFIGURATION FILES USING CAESAR II
21 Unit System (7273FFIL)
CAE S A R liVERS 430
INPUT UNITS USED
UNITS 7273F NOMISCH INPUT ON
LENGTH inches
FORCE pounds
MASS(dynamics) pounds
MOMENTS(INPUn inch-pounds
MOMENTS(OUTPUT) inch-pounds
STRESS Ibssqin
TEMP SCALE degrees F
PRESSURE psig
ELASTIC MODULUS Ibslsqin
PI PE DENSITY Ibslcuin
INSULATION DENS Ibslcuin
FLUID DENSITY Ibslcuin
TRANSL STI F Ibslin
ROTATIONAL STiF inlbldeg
UNIFORM LOAD Jblin
GLOAD gs
WIND LOAD IbsJsqin
ELEVATION inches
COMPOUND LENGTH inches
DIAMETER inches
WALL THICKNESS inches
OWNER DOCUMENT Ndeg
~ Doc T Malerial CoOa Serial Ndeg Rev
1013
x 25400 mm
x 4448 N
x 0454 kg
x 0113 Nm
x 0113 Nm
x 0007 MPa
x 0556 C
x 0069 bars
x 0007 MPa
x 27680000 kgCrmiddotm
x 27680000 kgJcum
x 27680000 kgci m
x 0175 Nm
x 0113
l x 175127 NJm
x 1000 gs
x 6894757 NJ m
x 0025 m
x 25400 mm
x 1000 inch
x 25400 mm
bull bull
Technip
KHARG ETHYLENE PLANT KHARG Olefin Complex
PETROCHlMlCAL IND JES DIiVElOPMENT MANGEMENT CO
11113
Technip bull
KHARG ETHYLENE PLANT ~ KHARG Olefin Complex
iETltOCHEMICtl OEVEIOPMENT MANArCO
CONTRACTOR DOCUMENT N OWNER DOCUMENT Nmiddot ProIecl N p U Doe TwalMrolerial Code ISen N ReI P_ Proiect N I UNt Doo T~ I ~eriIII Code
7273F 000 WI I 1300 I 000 I 0 I 11113 I I I
22 Setup File ( CAESARCFG )
C A E SAR II VERS450
SETUP FILE PARAMETERS
CONNECT GEOMETRY THRU CNODES YES I MIN ALLOWED BEND ANGLE 500000 I MAXjLLOWED BEND ANGLE bull 135000 I BEND LENGTH ATIACHMENT PERCENT 100000 I MINjNGLE TO ADJACENT BEND PT 500000
LOOP CLOSURE TOLERANCE 254000mm
THERMAL BOWING HORZ TOLERANCE 100000E-04
AUTO NODE NUMBER INCREMENT 100000
ZJXIS UP NO
USE PRESSURE STIFFENING DEFAULT
ALPHA TOLERANCE 500000E-02
RESLDmiddotFORCE NO
HGR_DEF RESWGT STIF
bull 01751200E+12 Nlmm
DECOMP SNG TOL 01 OOOOOOE+ 11
BEND_AXIAL SHAPE NO
FRICT STIF 875600 Ni mm I FRICT NORM FORCE VAR 025000 I FRICT ANGLE VAR 300000 I FRICT SLIDE MULT 100000
ROD TOLERANCE 100000
ROD INC 200000
INCORE NUMERICAL CHECK NO
OUTCORE NUMERICAL CHECK NO
DEFAULT TRANS RESTRAINT STIFF 0175120E+12 Nlmm
DEFAULT ROT RESTRAINT STIFF 0112980E+12 Nmi deaJ
IGNORE SPRING HANGER STIFFNESS bull NO I
WI I middot AiHG bull _ KtVRCUE LOoO CAS ES_Odoc
rmiddot
bull
bull
Technip
KHARG ETHYLENE PLANT KHARG Olefin Complex
Setup File (
CONNECT_GEOMETRY _ THRU_CNODES
WRC-07 VERSION
WRC- 07
DEFAULT
831
WI I middot AIlaquo) Amiddot KHARGJUOAD CASFsOdoc
T
F
YES
NO
181 281
NO
DEFAULT
02206272E+OSbull
bullbull
bull
bull
Thchnip bull
KHARG ETHYLENE PLANT ~ KHARG Olefin Complex
PFffiOCHEMICAL INO bull DEVELOPMENT MANAG ~ENTCO_
CONTRACTOR DOCUMENT Ndeg OWNER DOCUMENT N
Proioct Ndeg Unit Doc TIIDEII Material Code Serial Ndeg Rev I Paae Proiect N Unit Doc Type Material Code Serial N A~ 7273F I 000 I WI I 1300 I 000 I a I 13 13 I 1313
FRP Ratio GmodlEmo(Uaxial) O2500000E+OO
FRP EalEhVhla O1527272E+OO
SetuD File (CAESARCFG Continuation)
FRP Lamina1e Type THREE
FRP Alpha O2159827E+02 C
FRP Density O1660800E+04 kocum bullEXCLUDE 12 FROM UKOOA BENDI NG NO
OUTPUT REPORTS BY LOAD CASE YES
DISPLACEMENT NODAL SORTING YES
DYNAMIC INPUT EXAMPLE TEXT MAX
TIME HIST ANIMATE YES
ENABLE AUTOSAVE YES
AUTOSAVE TIME INTERVAL O3000000E+02
PROMPTED AUTOSAVE YES
DISABLE UNDOREDO NO
STRUCTURAL DATABASE AISC89BIN
VALVE amp FLANGE GENERIC VHD
EXPANSION JT DBASE FLEXPATHJHD
PI PING SIZE SPECIFICATION ANSI
DEFAULT SPRING HANGER TABLE O5000000E+01
SYSTEM DIRECTORY NAME SYSTEM
UNITS FILE NAME 7273FFIL
ENABLE ODBC OUTPUT NO
DEFAULT SPRING HANGER TABLE LlSEGA
- bull -
WI 1 ANG bull IV IlHAAG_IELOAD CAS ES_OdOC
SRMPL6 LOf]) C(15euro5 S V REfK Ti O-l FOeC e- JlUE TO PSv oPttvlNG
bull Sldlle Aymmiddot [CIDO(UMpoundNTS AllD SETIINGSVhBACONI7173FmiddotMBACONICAESAR FILESICNj016_REV ~
bull
bull
bull
Edt
+ t
loadCose Edlcr LoadCoseOptiom Loads WlNeLoads
loads Oefned n IrtJIA loed Casu Stress Type
W -Woltllt L1 W+D1 +T1 +P1 +H Of 01 middot Displcmnt Case ~ L2 wO-iT2+P1 +H-- Of T1 middot Thermal Case tn l3 W~D1~T3~P1H ~(]S-oiit~~ Of LltgtOd e T2 Thermal Case 2 -- - _- ------- -__- T3 Thermal Case U3
l4 W+P1+H SUS __ _- -----PI middot Pr euUle Case 1 LS Wt-P1t-H-t-F1 OCC Hp middot Hydlo Prenae L6 Ul OCC --- ---- _----- H middot Hanger l oads 17 U2 OCC UI middot Unf Load eMe 11 La U3 OCC U2 -UriloodlAse 12 L9 F1 OCC U3 Uri l oad Case 13 L10 L1-l4 EXP F1 middot Cone FOIct Case 11 1 Ll1 L2-l4 J EXP Vlllet Fled W WNC middot W~ no corieris L12 L3-lS EXP
L13 LS+l7+l8 OCC L1 4 L-4+l13 ----l ~~ IL15 L1 lt-l1 3 L1 6 LJl9 (fD lO(ll ch 011 (f~tnlh OCC
STATIQUE LoR)) I- Ill
1
FW FRANCE NDG SHT16F I
CliENT
PROJECT
CPNo
EXXON
18KTA E5000 Expansion
CALCNo ISV 3310
CALC BY BEP
CHKD BY
DATE 13012006
RELIEF VALVE LOADINGS vapour
RV Nos ISV 3310
SIZE 4x3
RATING 150xlSO
ORIFICE L
bull DATA DESCRIPTION
RV SET PRESSURE
PERCENT OVERPRESSURE
Ps (l+PolOO) + 147
REliEF TEMPERATURE
1195492
RATIO OF SPECIFIC HEATS SIZING FLOW
SElECTED ORIFICE AREA
CALCULATED ORIFICE AREA
FACTORED SIZING flOW
MAX No OF WORKING VALVES
SIZING flOW PER VALVE
113600
MOLECULAR WEIGHT
GAS CONSTANT 1544M
SYMBOl UNITS
Ps BARG
Po
P PSIA T1 DegC
T Oeg R
k WI Kg h A sqin Ac sqin W2 Kgh N
W Ib h w Ibsec M
R ftlblb Oeg
bull GRAVITY IQ ftS2
FI=
2 W RI
gPA
VALUE
7 10 F2
12635 256
9528 105
- shyFl
t~ --+
~ middotFI FI
t5489 rTABIJSmn Ow COiiOmON
2853 NOn IIQRIZOllTAL IOItCIS Kt MtA CEil
2853 15489 F2
1 341532 +shy948701 F3
885 174463 ltV AT POICONllIll0N
322 AampUMING IMPACT CTOII OYl
260496 Ib 1159 N
128894 Ib 573 N
520993 Ib 2318 N -
bullbull
SARASIN-lltJ l7Technical amp Calculation Data Sheet ZI 8olto R~62IKI _____ J40 11ap11M GnlCMl
VAlVH e COlTllOlS Safety Valve
e Bomel lype Opened
Project KHARG OLEfiN COMPLEX ~A
Tag No PSV 6 453A C-Quote Ref 3A30880IOOO Sales Engineer Abdeljalill Baigar W de Commande
Operating ondl tlons Connect ons
19 InlelON shy1 fluid type Superheated Stetlm
20 Inlet Finish ANSt600 RF (125-250 AARH) 2 Capacity 78500 Kglh 21 Outlet DN J Set ptesSUe br eft 22 Outlet Finish ANSI 150 ftF 1125-250 AARH) Ol$charoe Tom p J7S C Accordinn 10 ASME 616-5
5 Variable bad pressure 0 bar eft
Cold (If lest lXess 47 bar eft 8111 of material 7 Overpressure 11 () 16 floltfv SA216 wee
SA2115WCC2 Ylt8 Operating Pressure 40 bar eft
SA216 wee Tight Closing pressUIe (MAOP) 423 bar eft 26 NoWe Stllited AlSl410 1~ 27 174 PH Stainless SteelMechanical Tomp J7S middotC ~ 28 Gaskets Stalnl St1
29 SPfinQ Chromium Allov Steel 30 AlSI431c31 Adusitina Rlna SA351 CF3M 32 Stud Al1lQrB7 JJ Alt4i1r2H Accessories
Regular Levr 35 51etUted nozzl
ReqUIred Area 31 927 om Test Gag 495 s q InIl Selected Area 41 2 om
I 839 sq in 15 Onfice p
Reaction loroe DN~ t Flow capacity 101299 Kglh 18 Noise at 30 m acc to APt521 120 dB
apprO)flTlate noise level at 30 m according to API521 (mouth noiso) )perl dlsctlarge
Customer Name TECHNIP FRANCE evlslon ~ lion ate
890 4 20-juin-2005
Cust Item Numb 7U3F RFQ 1545-01 a ely a ype pflllg a a ely alve ea1T
I I J7 Standard API 520 I )
Commercial code S46P3530AmiddotDmiddotVMM I shyI Dimensions
A- 2254 mm B- 2540 mm W - 11800 mrnIA 525PlKd~KnKb Kshl ~ Welghl() s 1523 Kg I A- 89 Inch I bullB- 100 Inch
Dati 01 calcul w - 4115 Inch Mass Capaatv W 18500 KgIh Weight( ) 3357 Pound
P1 5553 bar abs r~ C Gase Constant 143843
() Indicative Values 0 now ooeIficient Kd 0915 0
Ksn 0865 Remarks Napier equation correction Kn 1
~ 2 valves are necessary 10 reach the required capacity
Back pressure correcUon Kb 1a BUlHmiddotup back pressureO 1 berg Same calculallO1 heet lor the 1st va lve and the spare one bull
N
~
GENERAl
PEO
PROCESS
CONDITONS
bull DESIGN
DATA
bull MATERIALS
I
OPT IONS
1 T Nu~
2 Service 3 Line NUrMer 4 P amp to Numbef
5 6 Conform to 961231EC 7 Fluid T
8 NJ licable rED Table 9
0 11
12
13
14
15 16
17 19
20 21 22
PED Cal
Fluid Fluid Servlc Required Capaci
MoltcullWe hI
ratln PrtSi ur
tlll TIm tUri
Badlt Prl$IIure
AJlovtabie Ova sure
Ov esslI10 FactOI Com esslbU Latenl Heal 01 V lion
o Tl 1012812005 Pour Commenta ires
Equipment
Fluid Groo
Fluid S~I
5 cltle Gl1Ivl Set Pressure
Col
HC+H20
15489
5 02
ReHov Temperatlyene 212
Constant Varia1je Total
23 Specific Hnt RItIo lC 24 Relief Densi
25 Relief Viscosity
26 Barometric Pressure 27 28 Nozzle Flit Semi
29 Design Saely Reflef Sale -Relief 30 Type Conventional BelloIN Plot Opefatad 31 BonnetT 32 n Code
33 Sizing Basis 34 Calcula ted Area
35 Selected Area 36 Orifice De nation
37 Size Rating -Inlel 38 Size Rat - Outlet
39 40 41 42 43 Stt 44 Fla es
45 Resilient Seat Seal 46 Guide
471 Spfing 46 Wtted Material
49 50
Bonnt Disc
Ri s Bellows
51 Cap Screwed or Bolted 52 Lever Plain or Packed 53 TestGag
54 55
22-ISV 3310 0 331fD332 SHCOO20150A1A 1 l -Q2S)(l2
y Gaseous Group 1
0 1
0
09
105
4
Note 10
k
C
k p
Safety Corrventlonal
hI Solted
ASME Delaut eau de refroldissement
1812 em
L 3 150 RF 450 RF
A2 16 WCB
NOlet A216WCB
NOle 1
Note 1
NOIot
NOIel
(Note 1
No
No
INSTRUMENT SPECIFICATION
Valve Safety Pressure Relief
oxicFlammable
GasIVapo
7
2564 C
A21 6WCB SS 316 Mini
Note 1
EJflt0nMobil Chemic
Sheet 5middot11 of 46
f
No 8 Date Revision Code 2831 No C3 1052 Amiddot163 1middottVOl Rev 0
i (
II Technical amp Calculation Data Sheet SARASIN-Agt Zllloa-R~
Safety Valve Nt BiOPUIle Gt1wtI bull bull 2110 1-1_
IN I ICustomer Name TECHNIP FRANCE
891 I 4 I bull s~ I
Cuslllem Numb 7273F RFQ 1545-01
Project KHARG OLEFIN COMPLEX I Opened
I 1 I
Quote Ref Tag No PSV pound I Nde Sales Abdeljalill Baigar I
I I uperatIng onaltons
Fluid ~e Superheated Steam 19 tnle ON shy
capaci ty 78500 Kgn 20 Inlet Finish ANSI 600 RF (125-250 AARH)
3 Set presMKC 21 Outlet ON
4935 bar eM 22 OtItlet Finish ANSI 150 RF (125-250 AARH)
DiSCharge Temp 375 middotC ASME B16-5 5 Variable back presslJe bull bar eft
Cold dilf lesc press 4935 bar eft I Bill 01 I
OverptesslKe B() 10 Bod SAl16 wee a Operating ProsslKe bar elf 24 Yoke SA216 wee
25 cabull SA216 weebull bull Tlglt Closing presSlKe (MAOP) 44 415 bar eff 26 Nozzle Sellited AlSI410 bullMlaquohBnIcaI Temp J15 C 21 Disc 174 PH Stilinless Steel 28 Gaskets Stainless $t1 bullSDOM Chromium Alloy Steel 30 Golde AlSI431 31 AcluslthQRinP SAl51 CF3M 32 Stud A183flr81 33 Nul Al94gr2H
gt0 Revulr Lever
Reqllif~ Afea 32023 om 35 middot SlelUted noule
12 496 sq in TU I Gag
1 Sellcl(l(l AIel 41 2 om
I 839 sq in Orirooe p
I ReactIon loree 3016 D I Flow capacity 100996 KgIh
I Noise ill 30 m ace to AP152 1 126 dB approxmate noise level at 30 m aCCOfding to APl521 (mtluth noise) open discharge
II 37 j API52 I I I
Commercial code S46P3530A-D-VMM I
IA= 525 PlKd~Kn KbKsh I I~-middot 2254 mm 2540 mm
11800 mm
bull 1523 Kg
lA shy 89 InCh
Dab 01 COI lcul I ~ - 100 Inch
IH- 465 Inch -jshyMa55 Capaoty W 18500 KgIh 3351 Pound -IP I 553 barabs C C-ase Constant 341143 I () Indicative Values 0 now coeffiCIent Kd 09150
N Ksh 0866 w- Napier equation coffeclion Kn bull 2 valves afe necessary to reach the required capacity lt Back Pfessure correcllon Kb
BUIItmiddotup back pressurecO 1 barg 2nd Ialve set at 05 of set pranure with 10 olelpreSSure in accordill1Ce With API 520
bullbulliii
bull 11 Load cases Ioad case combinations
The following load cases f load case combinations shall be analyzed 1) always or 2) on a casemiddot to-case basis
Static load cases for operating design and pressure test conditions
L6 jillL7 I
I --shy
I --shyI I I I I
L L
I Ll 9 L20
bull ~--
Load types (iC a pplicable load types should be added) W Dead weight (pipe weight + fluid weight + insulation weight) D Displacement T Design temperature P Design internal pressure U Uniform loads (eg snow load seismic load) F External forces (forces andor moments) HP Hydro test pressure H Hanger loads WIN Wind loads (for the main wind directions) WNC Dead weight without contents (pipe weight + insulation weight) WW Water-filled weight for pressure test
bull bull bull
bull
bull ~-
Technip
bull KHARG ETHYLENE PLANT
KHARG Olefin Complex
7273F WI
Case
(OCC) Sustained plus Wind Z combined absolutely
11 For Lines Carrying Heavy Fluid (Hydrocarbon Water )
a - Example File 2_00CA_O_A (Unit 20 Calculation Number 001 Load Case File AIKev 0)
bull
exposed to wind hydrostatic test spring supports No Yes_No CASE I W+~I+IJ+PI+H (O~E) Operating
CASE 2 W+PI+H (SUS) Deadweight + Pressure
CASE 3 U I (OCC) Seismic Load X
CASE 4 U2 (OCC) Seismic Load Y
CASES U3 (OCC) Seismic Load Z
CASE 6 L1 -L2 (EXP) Expansion range Code Case
CASE 7 W +lA+L5 (OCC) Resultant seismic load SRSS combination
CASE8 L2+L7 (OCC) Suslalncd plus Seismic Combined Case
b - Example File 2_002_A_O_A (Unil 20 Calculation Number 002 Load Case File A
exposed to wind hydrostatic test spring supports Noy Ye
bull
CASE I W+D1+T1+Pl+H
CASE 2 W+Pl+H
CASE 3 WIN I
CASE4 WIN2
CASES UI
CASE6 U2
CASE 7 U3
CASE 8 LI -L2
CASE 9 L5+ L6+L 7
CASE 10 L2+L3
CASE II L2+lA
CASE 12 L2+L9
(OPE) Operang
(SUS) Deadweight + Pressure
(SUS) Wind along X (Instead or oce 10 avoid Snbbe ivoio~ irany)
(SUS) Wind along Z Onslead oroce to avoid Snubber ifi(lY)
(OCC) Seismic Load X
(OCC) Sesmc Load Y
(OCC) Seismic Load Z
(EXP) Expansion range Code Case
(OCC) Resultant seismic load SRSS combination
(OCC) Sustained plus Wind X combined absolutely
Case
(OCC) Sustained plus Seismic Combined absolutely Case
Technip
P eel N
7273F
KHARG ETHYLENE PLANT KHARG Olefin Complex
CONTRACTOR DOCUMENT Ndeg
Malellal Code Selia N Rev Pa p
1300 000 0 513
PETItOCHllMrCAL IN ST1UES DEVELOPMENT MANG MENT CO
OW NER DOCUMENT Ndeg
Material Code Serial Ndeg Rev Pa
513
12 For Lines Carrying Gas Steam or Vapor
bull
Examplelr~~~~~+-_ex~po_S_ed~0 ~nd_ ~Wi __~_h~yd_~__I~a~____tic es1-_s~pn_n~g~s~u~ppo~rts__~ Line criteria No shy Yes Yes
a - Example File 2_003_A_O_A File A RevD)
CASE I WNC+DI+TI+PI+H
CASE 2 WNC+PI+H
CASE3UI
CASE 4 U2
CASES U3
(Unit 20 Calculation Number 003 Operating Loa Cases
(OPE) Operating
(SUS) Deadweight (No contents) + Pressure PI
(OCC) Seismic Load X
(OCC) Se ismic Load Y
(ccq Seismic Load Z
CASE 6 LImiddotL2 (EXP) Expansion range Code Case
CASE 7 L3+L4+LS (CCe) R~sultant seismic load SRSS combination
CASE 8 L2+L7 (OCC) Sustalfled plus SeIsmic Combined absolutely C e Case
b Example File 2_003_B_O_A (Unot 20 Calculation Number 003 Hydrotest LcJCase Fi le B RevD) lftested in place
CASE I WW+PI (SUS) Deadweight Full of water + Hydrotest Pressure PI
bull 4 -gt fv
L1 --1- r
Igt 0
bull Technip
P ec(Ndeg
n73F
KHARG ETHYLENE PLANT KHARG Olefin Complex
CONTRACTOR DOCUMENT N
P N
613
PETROCHEMICAL IN USTRJpoundS DEVElOPMENT MANA EMENT CO
OWNER DOCUMENT Ndeg
Material Code Sertal Ndeg Rev Pa
613
Example 2 r-~~~~~~~XP~osed~to~w~i~nd~~h~~=r~ost~at=ic~t==st~~sp=n=n~g~su=ppo==rt=s~ line criteria Yes Yes Yes
a Example File S_OOS_A_Obullfi (Uuil50 Calculation Number 00) Operating Load Case Fi e ArevO) J7LLA A_A
CASE 1 WNC+QI+Tt+PI+H (OPE) Operating
CASE 2 WNC+PI+H
CASE 3 WIN I
CASE 4 WlN2
CASE 5 VI
CASE 6 U2
CASE 7V3
CASE 8 Ll -L2
CASE 9 L5+L6+L7
CASE 10 L2+L3-shyCASE II L2+L4
CASE 12 L2+L9
(SUS) Deadweight (No contents) + Pressure
(SUS) Wind along X (1nstcad oroce 10 avoid Snubber activatio if any)
(SUS) Wind along Z (Instead ofoce to avoid Snubberactivarion ifany)
(OCe) Seismic Load X
(OCC) Seismic Load Y
(OCC) Seismic Load Z
(EXP) Ex pansion range Code Case
(ocq Resultant seismic load SRSS combination gt
(OCe) Sustained plus Wind X combined absolutely C I Case
(OCC) Sustained plus Wind Z combined absolutely Codf Case
(aCe) Sustained plus Seismic Combined absolutely Cod Case
b Example File S_OOSJl_O bull A (Unit 5OCalculation Number 005Hydrostatic Load case fil B
revO) 4-OlL ~ _A_A
CASE 1 WW+PI (SUS) Deadweight full of water + Hydrotest Pressure PI
bull WI I bull AHa bull_ Amiddot KHARGJELOAOCASESOdDc
bull
bull
RevO)
CASE I W+PI +TI+DI+H
CASE 2 W+PI+T2+DI+H
CASE 3 W+PI+T3+DI+H
CASE 4 W+Pl+H
CASE 5 WNC+H
CASE6UI
CASE U2
CASE 8 U3
CASE 9 L6+L+L8
CASE 10 LimiddotL4
CASE I I L2middotL4
CASE 12 L3middotL4
CASE 13 L4+L9
Technip
KHARG ETHYLENE PLANT KHARG Olefin Complex
PET1IOCJiEMCAL INOUSTIUES DEVElOfMENT MANA EMENT co
7273F
Nmiddot UtIiI Doe T
1300 000 0 713
File A
1-1 For Lines Connected to Rotating Equipmenl
Example File 002_007 _A_O_A (Unit 002 Calculation Number 007 Load ea
(OPE)
(OPE)
(OPE)
(SUS)
(SUS)
(OCC)
(OCC)
(OCC)
Operating Pump A operating 380degC
Pump B Standby 21degC (Ambient)
Operating Pump B operating 380degC
Pump A Standby 21degC (Ambient)
Operating Pump A and B hot 380ltgtlt
Deadweight + Pressure
Weight (No contents)
Seismic X
Seismic Y
Seismic Z
(ocq Resultant seismic load SRSS combination
(EXP) Thermal T 1 Pump A operating 380degC
Pump B Standby 21degC (Ambient)
(EXP) ThennaJ 12 Pump B operating 380degC
Pump A Standby 21degC (Ambient)
(EXP) Therma1 13 Pump A and B hot 380degC
(OCC) Sustained plus Seismic Combined absolutely C e Case
Note Load Case 5 is used to calrulate shop calibration of spring support instaJled above pump nozzle
- - - -
bull Technip
KHARG ETHYLENE PLANT KHARG Olefin Complex
CONTRACTOR OOCUIoENT N OWNER DOCUMENT
P N IJnIt Doc T lMtecW eoo Serial N Rev P p unit Doe T Material Code Serial Rev P
7273F 000 WI 1300 000 0 813
131 Load Cases to be calculated to comply wjtb ASME 831 3 Code Cases
~xample
CASE I W+DI+TI+P I(OPE)Operaling CASE 2 W+Pl(SUS) Deadweight + Pressure
CASE 3 U I (OCC) Seismic Load X
CASE 4 U2(OCC) Seismic Load Y
CASE 5 U3(OCC) Seismic load Z
CASE 6 LI -L2(EXP) Expansion range Code Ca~
CASE 7 W+L4+L5(OCC) Resultanl seismic load SRSS combination
ASE 8 L2+L7(OCC) Sustained plus Seismic Combined absolutelyCode Case
CASE 9 LI+L7(OCC) Operating plus Seismic combined absolutely hOI restraint (Optional)
813
CASE 10 L9+~(OCC) Maximum restrai nt loads (Optional)~ 14 FOR LOW TEMPERATURE CARBON STEEL (LTCS)
141 Stress criteria
The point (3) of the figure 3232B imposes to take into account the following load cases
Permanent static loads
bull W Weight (signed load)
bull bull P Pressure (signed load)
bull T low Temperature (signed load)
bull F exlemal loads (signed load)
Occasional static and dynamic loads
bull U seismic accelerations Corresponding to the SASS combination of the Ul (X dyion) U2 (Y direction) and U3 (Z direction) components
bull WIN Wind (unsigned load)
Remarks
I) In Caesar load case it is necessary to have by load case line only one of load cases d~=ibed her-under
2) In Caesar input all stress intensification factors shal l be equal to 1
TIle criteria is
W + P +T + F + U or WIN lt O3Sh - 413 Mpa combined in ABS( ~ shy
bull
9113
Technip
bull KHARG ETHYLENE PLANT
KHARG Olefin Complex
QVoINEA OClCUME NT N
P bull p N Unit Doc T Malerial Code Serial Ndeg Rw
913
142 Examples
Examplelr-~__~~-+~e~x~po=s~ed~to~W~ind=-~~h~~~r~o~st=a=t~~te=s~t~=s~ ~ po~rt~s-+pr=ing~s~u~p~line criteria Yes Yes Yes
bull Example File 002_01O-A_O_A (Unit 002 Calculation Number OlD Load Case File A evD)
CASE 1 W+Tl+PI+H (OPE) Operating cold condition
CASE 2 W+T2+P2+H (OPE) Operating hot conditions
CASE 3 W+PI +H (SUS) Deadweight + Pressure
CASE 4 WINl (SUS) Wind along X (Instead of OCC to avoid Snubber activation if I y)
CASES WIN2 (SUS) Wind along Z (Instead of OCC to avoid Snubber activation if y)
CASE 6 Ul (OCC) Seismic Lcentad X
CASE 7 U2 (OCe) Seismic Load Y
CASES U3 (OCC) Seismic Load Z
CASE9W+H (SUS) Deadweight + Spring hanger
CASE 10 PI (SUS) Pressure
CASE J 1 Tl (EXP) Temperarure
CASE 12 LI -L2 (EXP) thermal stress range Code Case
CASE 13 Ll -L3 (EXP) thermal suess range Code Case
CASE 14 LlI+Ll2 (EXP) full thermal stress range checking ABS combination
CASE 15 L6+L7+LS (OCC) Resultant seismic load SRSS combination CASE 16 ~9+L10+L1I+L3 (OCC) Sustained plus Wind X combined absolutely Code Ease CASE 17 L9+LI0+L11+L4 (OCC) Sustained plus Wind Z combined absolutely Code tase CASE 18 L9+L10+Lll+L15 (OCC) Sustained plus Seismic Combined absolutely Code ase
bull
bull
bull
bull
bull
Technip
KHARG ETHYLENE PLANT KHARG Olefin Complex
COHTAACTOR DOCUMENT N
-~
PEJROCHEMICAI IES DBVELOPMENT MANAG co
OWNER DOCUMENT Ndeg Unit Doe T P N
7273F 000 WI 1300 006 813 1 813 1
8 SNOW WAD (Ws)
I Emiddot~middotv O
Snow loads shall 00 applied only for cold outside lines for which design T is below 0 C and which are not protected by floor equ ipment or others
The hereafter calculated vaJue (Ws) will be classed as unifonn load foUowing Y axis (U ) in a separate Caesar input file See 7273F_OOO_CN3_CN2_1370_SAMPLlC AXLS
Design snow load 25 kgll1l2
The distribution of snow remaining on the horizontal pipe will take the shape hereu dec a reducljon factor of 072 may be applied
Ws = ( lx 051gt In x h 022D ) 25
Ws = (Ix 072 x D ) 25
Ws = 18 x D Kflrsi= 180 x D NIP Where 0 = outside diameter of pipe o r outside diameter of pipe + insulation if exist( m)
70middot
9120
o
bull Technip -D KHARG ETHYLENE PLANT ~
KHARG Olefin Complex
middot INmiddot I A~ I P~ UNo I 7273F 000 WI 1300 I 006 I A I 115 I 115
APPENDIX IV
L bull WIND PRESSURE I ELEVATION
11 Wind Basic nata I Wind pressure calcuJation
As per Project Basic Engineering 7273F-30-PP-206 Bask Design Data
Basic wind speed 160km h (44 5 m s)
Exposure Category 0
According to UBC 97 the design wind loading shall be
p= CxCxqX
where
P =Design wind pressure allevel 10 III
C~ =156 at leve1 10 m (EIIposure and gust factor-Table I6-G)
Cq I for DNlt= 50 nun
= 08 for DNgt 50 mm (Exposure and gust factor-Table I6-H)
qs= 1226 kNm2 ( Wind stagnation pressure at 10 m -Table J6-F)
lw = 1 15 (Importance factor - Table 16-K)
p = 220 xC (kNl m)
Height Above Wind pressure Ground Level
(m) PI eq (kNlm2 )
Oto 10 22
10 (0 20 247
20 to 30 264
30 10 40 276
40 to 50 286
50 to 60 289
60 to 70 293
70 1080 299
80 to 90 312
bull
bull
bull
bull
CONTRACTOR OOCUIENT bull N UniI Doc T Milttl CoOl srI N Rev Pa p
7273F 000 WI 1300 000 0 ()J 13
2 CONFIGURATION FILES USING CAESAR II
21 Unit System (7273FFIL)
CAE S A R liVERS 430
INPUT UNITS USED
UNITS 7273F NOMISCH INPUT ON
LENGTH inches
FORCE pounds
MASS(dynamics) pounds
MOMENTS(INPUn inch-pounds
MOMENTS(OUTPUT) inch-pounds
STRESS Ibssqin
TEMP SCALE degrees F
PRESSURE psig
ELASTIC MODULUS Ibslsqin
PI PE DENSITY Ibslcuin
INSULATION DENS Ibslcuin
FLUID DENSITY Ibslcuin
TRANSL STI F Ibslin
ROTATIONAL STiF inlbldeg
UNIFORM LOAD Jblin
GLOAD gs
WIND LOAD IbsJsqin
ELEVATION inches
COMPOUND LENGTH inches
DIAMETER inches
WALL THICKNESS inches
OWNER DOCUMENT Ndeg
~ Doc T Malerial CoOa Serial Ndeg Rev
1013
x 25400 mm
x 4448 N
x 0454 kg
x 0113 Nm
x 0113 Nm
x 0007 MPa
x 0556 C
x 0069 bars
x 0007 MPa
x 27680000 kgCrmiddotm
x 27680000 kgJcum
x 27680000 kgci m
x 0175 Nm
x 0113
l x 175127 NJm
x 1000 gs
x 6894757 NJ m
x 0025 m
x 25400 mm
x 1000 inch
x 25400 mm
bull bull
Technip
KHARG ETHYLENE PLANT KHARG Olefin Complex
PETROCHlMlCAL IND JES DIiVElOPMENT MANGEMENT CO
11113
Technip bull
KHARG ETHYLENE PLANT ~ KHARG Olefin Complex
iETltOCHEMICtl OEVEIOPMENT MANArCO
CONTRACTOR DOCUMENT N OWNER DOCUMENT Nmiddot ProIecl N p U Doe TwalMrolerial Code ISen N ReI P_ Proiect N I UNt Doo T~ I ~eriIII Code
7273F 000 WI I 1300 I 000 I 0 I 11113 I I I
22 Setup File ( CAESARCFG )
C A E SAR II VERS450
SETUP FILE PARAMETERS
CONNECT GEOMETRY THRU CNODES YES I MIN ALLOWED BEND ANGLE 500000 I MAXjLLOWED BEND ANGLE bull 135000 I BEND LENGTH ATIACHMENT PERCENT 100000 I MINjNGLE TO ADJACENT BEND PT 500000
LOOP CLOSURE TOLERANCE 254000mm
THERMAL BOWING HORZ TOLERANCE 100000E-04
AUTO NODE NUMBER INCREMENT 100000
ZJXIS UP NO
USE PRESSURE STIFFENING DEFAULT
ALPHA TOLERANCE 500000E-02
RESLDmiddotFORCE NO
HGR_DEF RESWGT STIF
bull 01751200E+12 Nlmm
DECOMP SNG TOL 01 OOOOOOE+ 11
BEND_AXIAL SHAPE NO
FRICT STIF 875600 Ni mm I FRICT NORM FORCE VAR 025000 I FRICT ANGLE VAR 300000 I FRICT SLIDE MULT 100000
ROD TOLERANCE 100000
ROD INC 200000
INCORE NUMERICAL CHECK NO
OUTCORE NUMERICAL CHECK NO
DEFAULT TRANS RESTRAINT STIFF 0175120E+12 Nlmm
DEFAULT ROT RESTRAINT STIFF 0112980E+12 Nmi deaJ
IGNORE SPRING HANGER STIFFNESS bull NO I
WI I middot AiHG bull _ KtVRCUE LOoO CAS ES_Odoc
rmiddot
bull
bull
Technip
KHARG ETHYLENE PLANT KHARG Olefin Complex
Setup File (
CONNECT_GEOMETRY _ THRU_CNODES
WRC-07 VERSION
WRC- 07
DEFAULT
831
WI I middot AIlaquo) Amiddot KHARGJUOAD CASFsOdoc
T
F
YES
NO
181 281
NO
DEFAULT
02206272E+OSbull
bullbull
bull
bull
Thchnip bull
KHARG ETHYLENE PLANT ~ KHARG Olefin Complex
PFffiOCHEMICAL INO bull DEVELOPMENT MANAG ~ENTCO_
CONTRACTOR DOCUMENT Ndeg OWNER DOCUMENT N
Proioct Ndeg Unit Doc TIIDEII Material Code Serial Ndeg Rev I Paae Proiect N Unit Doc Type Material Code Serial N A~ 7273F I 000 I WI I 1300 I 000 I a I 13 13 I 1313
FRP Ratio GmodlEmo(Uaxial) O2500000E+OO
FRP EalEhVhla O1527272E+OO
SetuD File (CAESARCFG Continuation)
FRP Lamina1e Type THREE
FRP Alpha O2159827E+02 C
FRP Density O1660800E+04 kocum bullEXCLUDE 12 FROM UKOOA BENDI NG NO
OUTPUT REPORTS BY LOAD CASE YES
DISPLACEMENT NODAL SORTING YES
DYNAMIC INPUT EXAMPLE TEXT MAX
TIME HIST ANIMATE YES
ENABLE AUTOSAVE YES
AUTOSAVE TIME INTERVAL O3000000E+02
PROMPTED AUTOSAVE YES
DISABLE UNDOREDO NO
STRUCTURAL DATABASE AISC89BIN
VALVE amp FLANGE GENERIC VHD
EXPANSION JT DBASE FLEXPATHJHD
PI PING SIZE SPECIFICATION ANSI
DEFAULT SPRING HANGER TABLE O5000000E+01
SYSTEM DIRECTORY NAME SYSTEM
UNITS FILE NAME 7273FFIL
ENABLE ODBC OUTPUT NO
DEFAULT SPRING HANGER TABLE LlSEGA
- bull -
WI 1 ANG bull IV IlHAAG_IELOAD CAS ES_OdOC
SRMPL6 LOf]) C(15euro5 S V REfK Ti O-l FOeC e- JlUE TO PSv oPttvlNG
bull Sldlle Aymmiddot [CIDO(UMpoundNTS AllD SETIINGSVhBACONI7173FmiddotMBACONICAESAR FILESICNj016_REV ~
bull
bull
bull
Edt
+ t
loadCose Edlcr LoadCoseOptiom Loads WlNeLoads
loads Oefned n IrtJIA loed Casu Stress Type
W -Woltllt L1 W+D1 +T1 +P1 +H Of 01 middot Displcmnt Case ~ L2 wO-iT2+P1 +H-- Of T1 middot Thermal Case tn l3 W~D1~T3~P1H ~(]S-oiit~~ Of LltgtOd e T2 Thermal Case 2 -- - _- ------- -__- T3 Thermal Case U3
l4 W+P1+H SUS __ _- -----PI middot Pr euUle Case 1 LS Wt-P1t-H-t-F1 OCC Hp middot Hydlo Prenae L6 Ul OCC --- ---- _----- H middot Hanger l oads 17 U2 OCC UI middot Unf Load eMe 11 La U3 OCC U2 -UriloodlAse 12 L9 F1 OCC U3 Uri l oad Case 13 L10 L1-l4 EXP F1 middot Cone FOIct Case 11 1 Ll1 L2-l4 J EXP Vlllet Fled W WNC middot W~ no corieris L12 L3-lS EXP
L13 LS+l7+l8 OCC L1 4 L-4+l13 ----l ~~ IL15 L1 lt-l1 3 L1 6 LJl9 (fD lO(ll ch 011 (f~tnlh OCC
STATIQUE LoR)) I- Ill
1
FW FRANCE NDG SHT16F I
CliENT
PROJECT
CPNo
EXXON
18KTA E5000 Expansion
CALCNo ISV 3310
CALC BY BEP
CHKD BY
DATE 13012006
RELIEF VALVE LOADINGS vapour
RV Nos ISV 3310
SIZE 4x3
RATING 150xlSO
ORIFICE L
bull DATA DESCRIPTION
RV SET PRESSURE
PERCENT OVERPRESSURE
Ps (l+PolOO) + 147
REliEF TEMPERATURE
1195492
RATIO OF SPECIFIC HEATS SIZING FLOW
SElECTED ORIFICE AREA
CALCULATED ORIFICE AREA
FACTORED SIZING flOW
MAX No OF WORKING VALVES
SIZING flOW PER VALVE
113600
MOLECULAR WEIGHT
GAS CONSTANT 1544M
SYMBOl UNITS
Ps BARG
Po
P PSIA T1 DegC
T Oeg R
k WI Kg h A sqin Ac sqin W2 Kgh N
W Ib h w Ibsec M
R ftlblb Oeg
bull GRAVITY IQ ftS2
FI=
2 W RI
gPA
VALUE
7 10 F2
12635 256
9528 105
- shyFl
t~ --+
~ middotFI FI
t5489 rTABIJSmn Ow COiiOmON
2853 NOn IIQRIZOllTAL IOItCIS Kt MtA CEil
2853 15489 F2
1 341532 +shy948701 F3
885 174463 ltV AT POICONllIll0N
322 AampUMING IMPACT CTOII OYl
260496 Ib 1159 N
128894 Ib 573 N
520993 Ib 2318 N -
bullbull
SARASIN-lltJ l7Technical amp Calculation Data Sheet ZI 8olto R~62IKI _____ J40 11ap11M GnlCMl
VAlVH e COlTllOlS Safety Valve
e Bomel lype Opened
Project KHARG OLEfiN COMPLEX ~A
Tag No PSV 6 453A C-Quote Ref 3A30880IOOO Sales Engineer Abdeljalill Baigar W de Commande
Operating ondl tlons Connect ons
19 InlelON shy1 fluid type Superheated Stetlm
20 Inlet Finish ANSt600 RF (125-250 AARH) 2 Capacity 78500 Kglh 21 Outlet DN J Set ptesSUe br eft 22 Outlet Finish ANSI 150 ftF 1125-250 AARH) Ol$charoe Tom p J7S C Accordinn 10 ASME 616-5
5 Variable bad pressure 0 bar eft
Cold (If lest lXess 47 bar eft 8111 of material 7 Overpressure 11 () 16 floltfv SA216 wee
SA2115WCC2 Ylt8 Operating Pressure 40 bar eft
SA216 wee Tight Closing pressUIe (MAOP) 423 bar eft 26 NoWe Stllited AlSl410 1~ 27 174 PH Stainless SteelMechanical Tomp J7S middotC ~ 28 Gaskets Stalnl St1
29 SPfinQ Chromium Allov Steel 30 AlSI431c31 Adusitina Rlna SA351 CF3M 32 Stud Al1lQrB7 JJ Alt4i1r2H Accessories
Regular Levr 35 51etUted nozzl
ReqUIred Area 31 927 om Test Gag 495 s q InIl Selected Area 41 2 om
I 839 sq in 15 Onfice p
Reaction loroe DN~ t Flow capacity 101299 Kglh 18 Noise at 30 m acc to APt521 120 dB
apprO)flTlate noise level at 30 m according to API521 (mouth noiso) )perl dlsctlarge
Customer Name TECHNIP FRANCE evlslon ~ lion ate
890 4 20-juin-2005
Cust Item Numb 7U3F RFQ 1545-01 a ely a ype pflllg a a ely alve ea1T
I I J7 Standard API 520 I )
Commercial code S46P3530AmiddotDmiddotVMM I shyI Dimensions
A- 2254 mm B- 2540 mm W - 11800 mrnIA 525PlKd~KnKb Kshl ~ Welghl() s 1523 Kg I A- 89 Inch I bullB- 100 Inch
Dati 01 calcul w - 4115 Inch Mass Capaatv W 18500 KgIh Weight( ) 3357 Pound
P1 5553 bar abs r~ C Gase Constant 143843
() Indicative Values 0 now ooeIficient Kd 0915 0
Ksn 0865 Remarks Napier equation correction Kn 1
~ 2 valves are necessary 10 reach the required capacity
Back pressure correcUon Kb 1a BUlHmiddotup back pressureO 1 berg Same calculallO1 heet lor the 1st va lve and the spare one bull
N
~
GENERAl
PEO
PROCESS
CONDITONS
bull DESIGN
DATA
bull MATERIALS
I
OPT IONS
1 T Nu~
2 Service 3 Line NUrMer 4 P amp to Numbef
5 6 Conform to 961231EC 7 Fluid T
8 NJ licable rED Table 9
0 11
12
13
14
15 16
17 19
20 21 22
PED Cal
Fluid Fluid Servlc Required Capaci
MoltcullWe hI
ratln PrtSi ur
tlll TIm tUri
Badlt Prl$IIure
AJlovtabie Ova sure
Ov esslI10 FactOI Com esslbU Latenl Heal 01 V lion
o Tl 1012812005 Pour Commenta ires
Equipment
Fluid Groo
Fluid S~I
5 cltle Gl1Ivl Set Pressure
Col
HC+H20
15489
5 02
ReHov Temperatlyene 212
Constant Varia1je Total
23 Specific Hnt RItIo lC 24 Relief Densi
25 Relief Viscosity
26 Barometric Pressure 27 28 Nozzle Flit Semi
29 Design Saely Reflef Sale -Relief 30 Type Conventional BelloIN Plot Opefatad 31 BonnetT 32 n Code
33 Sizing Basis 34 Calcula ted Area
35 Selected Area 36 Orifice De nation
37 Size Rating -Inlel 38 Size Rat - Outlet
39 40 41 42 43 Stt 44 Fla es
45 Resilient Seat Seal 46 Guide
471 Spfing 46 Wtted Material
49 50
Bonnt Disc
Ri s Bellows
51 Cap Screwed or Bolted 52 Lever Plain or Packed 53 TestGag
54 55
22-ISV 3310 0 331fD332 SHCOO20150A1A 1 l -Q2S)(l2
y Gaseous Group 1
0 1
0
09
105
4
Note 10
k
C
k p
Safety Corrventlonal
hI Solted
ASME Delaut eau de refroldissement
1812 em
L 3 150 RF 450 RF
A2 16 WCB
NOlet A216WCB
NOle 1
Note 1
NOIot
NOIel
(Note 1
No
No
INSTRUMENT SPECIFICATION
Valve Safety Pressure Relief
oxicFlammable
GasIVapo
7
2564 C
A21 6WCB SS 316 Mini
Note 1
EJflt0nMobil Chemic
Sheet 5middot11 of 46
f
No 8 Date Revision Code 2831 No C3 1052 Amiddot163 1middottVOl Rev 0
i (
II Technical amp Calculation Data Sheet SARASIN-Agt Zllloa-R~
Safety Valve Nt BiOPUIle Gt1wtI bull bull 2110 1-1_
IN I ICustomer Name TECHNIP FRANCE
891 I 4 I bull s~ I
Cuslllem Numb 7273F RFQ 1545-01
Project KHARG OLEFIN COMPLEX I Opened
I 1 I
Quote Ref Tag No PSV pound I Nde Sales Abdeljalill Baigar I
I I uperatIng onaltons
Fluid ~e Superheated Steam 19 tnle ON shy
capaci ty 78500 Kgn 20 Inlet Finish ANSI 600 RF (125-250 AARH)
3 Set presMKC 21 Outlet ON
4935 bar eM 22 OtItlet Finish ANSI 150 RF (125-250 AARH)
DiSCharge Temp 375 middotC ASME B16-5 5 Variable back presslJe bull bar eft
Cold dilf lesc press 4935 bar eft I Bill 01 I
OverptesslKe B() 10 Bod SAl16 wee a Operating ProsslKe bar elf 24 Yoke SA216 wee
25 cabull SA216 weebull bull Tlglt Closing presSlKe (MAOP) 44 415 bar eff 26 Nozzle Sellited AlSI410 bullMlaquohBnIcaI Temp J15 C 21 Disc 174 PH Stilinless Steel 28 Gaskets Stainless $t1 bullSDOM Chromium Alloy Steel 30 Golde AlSI431 31 AcluslthQRinP SAl51 CF3M 32 Stud A183flr81 33 Nul Al94gr2H
gt0 Revulr Lever
Reqllif~ Afea 32023 om 35 middot SlelUted noule
12 496 sq in TU I Gag
1 Sellcl(l(l AIel 41 2 om
I 839 sq in Orirooe p
I ReactIon loree 3016 D I Flow capacity 100996 KgIh
I Noise ill 30 m ace to AP152 1 126 dB approxmate noise level at 30 m aCCOfding to APl521 (mtluth noise) open discharge
II 37 j API52 I I I
Commercial code S46P3530A-D-VMM I
IA= 525 PlKd~Kn KbKsh I I~-middot 2254 mm 2540 mm
11800 mm
bull 1523 Kg
lA shy 89 InCh
Dab 01 COI lcul I ~ - 100 Inch
IH- 465 Inch -jshyMa55 Capaoty W 18500 KgIh 3351 Pound -IP I 553 barabs C C-ase Constant 341143 I () Indicative Values 0 now coeffiCIent Kd 09150
N Ksh 0866 w- Napier equation coffeclion Kn bull 2 valves afe necessary to reach the required capacity lt Back Pfessure correcllon Kb
BUIItmiddotup back pressurecO 1 barg 2nd Ialve set at 05 of set pranure with 10 olelpreSSure in accordill1Ce With API 520
bullbulliii
bull 11 Load cases Ioad case combinations
The following load cases f load case combinations shall be analyzed 1) always or 2) on a casemiddot to-case basis
Static load cases for operating design and pressure test conditions
L6 jillL7 I
I --shy
I --shyI I I I I
L L
I Ll 9 L20
bull ~--
Load types (iC a pplicable load types should be added) W Dead weight (pipe weight + fluid weight + insulation weight) D Displacement T Design temperature P Design internal pressure U Uniform loads (eg snow load seismic load) F External forces (forces andor moments) HP Hydro test pressure H Hanger loads WIN Wind loads (for the main wind directions) WNC Dead weight without contents (pipe weight + insulation weight) WW Water-filled weight for pressure test
bull bull bull
bull
bull ~-
Technip
P eel N
7273F
KHARG ETHYLENE PLANT KHARG Olefin Complex
CONTRACTOR DOCUMENT Ndeg
Malellal Code Selia N Rev Pa p
1300 000 0 513
PETItOCHllMrCAL IN ST1UES DEVELOPMENT MANG MENT CO
OW NER DOCUMENT Ndeg
Material Code Serial Ndeg Rev Pa
513
12 For Lines Carrying Gas Steam or Vapor
bull
Examplelr~~~~~+-_ex~po_S_ed~0 ~nd_ ~Wi __~_h~yd_~__I~a~____tic es1-_s~pn_n~g~s~u~ppo~rts__~ Line criteria No shy Yes Yes
a - Example File 2_003_A_O_A File A RevD)
CASE I WNC+DI+TI+PI+H
CASE 2 WNC+PI+H
CASE3UI
CASE 4 U2
CASES U3
(Unit 20 Calculation Number 003 Operating Loa Cases
(OPE) Operating
(SUS) Deadweight (No contents) + Pressure PI
(OCC) Seismic Load X
(OCC) Se ismic Load Y
(ccq Seismic Load Z
CASE 6 LImiddotL2 (EXP) Expansion range Code Case
CASE 7 L3+L4+LS (CCe) R~sultant seismic load SRSS combination
CASE 8 L2+L7 (OCC) Sustalfled plus SeIsmic Combined absolutely C e Case
b Example File 2_003_B_O_A (Unot 20 Calculation Number 003 Hydrotest LcJCase Fi le B RevD) lftested in place
CASE I WW+PI (SUS) Deadweight Full of water + Hydrotest Pressure PI
bull 4 -gt fv
L1 --1- r
Igt 0
bull Technip
P ec(Ndeg
n73F
KHARG ETHYLENE PLANT KHARG Olefin Complex
CONTRACTOR DOCUMENT N
P N
613
PETROCHEMICAL IN USTRJpoundS DEVElOPMENT MANA EMENT CO
OWNER DOCUMENT Ndeg
Material Code Sertal Ndeg Rev Pa
613
Example 2 r-~~~~~~~XP~osed~to~w~i~nd~~h~~=r~ost~at=ic~t==st~~sp=n=n~g~su=ppo==rt=s~ line criteria Yes Yes Yes
a Example File S_OOS_A_Obullfi (Uuil50 Calculation Number 00) Operating Load Case Fi e ArevO) J7LLA A_A
CASE 1 WNC+QI+Tt+PI+H (OPE) Operating
CASE 2 WNC+PI+H
CASE 3 WIN I
CASE 4 WlN2
CASE 5 VI
CASE 6 U2
CASE 7V3
CASE 8 Ll -L2
CASE 9 L5+L6+L7
CASE 10 L2+L3-shyCASE II L2+L4
CASE 12 L2+L9
(SUS) Deadweight (No contents) + Pressure
(SUS) Wind along X (1nstcad oroce 10 avoid Snubber activatio if any)
(SUS) Wind along Z (Instead ofoce to avoid Snubberactivarion ifany)
(OCe) Seismic Load X
(OCC) Seismic Load Y
(OCC) Seismic Load Z
(EXP) Ex pansion range Code Case
(ocq Resultant seismic load SRSS combination gt
(OCe) Sustained plus Wind X combined absolutely C I Case
(OCC) Sustained plus Wind Z combined absolutely Codf Case
(aCe) Sustained plus Seismic Combined absolutely Cod Case
b Example File S_OOSJl_O bull A (Unit 5OCalculation Number 005Hydrostatic Load case fil B
revO) 4-OlL ~ _A_A
CASE 1 WW+PI (SUS) Deadweight full of water + Hydrotest Pressure PI
bull WI I bull AHa bull_ Amiddot KHARGJELOAOCASESOdDc
bull
bull
RevO)
CASE I W+PI +TI+DI+H
CASE 2 W+PI+T2+DI+H
CASE 3 W+PI+T3+DI+H
CASE 4 W+Pl+H
CASE 5 WNC+H
CASE6UI
CASE U2
CASE 8 U3
CASE 9 L6+L+L8
CASE 10 LimiddotL4
CASE I I L2middotL4
CASE 12 L3middotL4
CASE 13 L4+L9
Technip
KHARG ETHYLENE PLANT KHARG Olefin Complex
PET1IOCJiEMCAL INOUSTIUES DEVElOfMENT MANA EMENT co
7273F
Nmiddot UtIiI Doe T
1300 000 0 713
File A
1-1 For Lines Connected to Rotating Equipmenl
Example File 002_007 _A_O_A (Unit 002 Calculation Number 007 Load ea
(OPE)
(OPE)
(OPE)
(SUS)
(SUS)
(OCC)
(OCC)
(OCC)
Operating Pump A operating 380degC
Pump B Standby 21degC (Ambient)
Operating Pump B operating 380degC
Pump A Standby 21degC (Ambient)
Operating Pump A and B hot 380ltgtlt
Deadweight + Pressure
Weight (No contents)
Seismic X
Seismic Y
Seismic Z
(ocq Resultant seismic load SRSS combination
(EXP) Thermal T 1 Pump A operating 380degC
Pump B Standby 21degC (Ambient)
(EXP) ThennaJ 12 Pump B operating 380degC
Pump A Standby 21degC (Ambient)
(EXP) Therma1 13 Pump A and B hot 380degC
(OCC) Sustained plus Seismic Combined absolutely C e Case
Note Load Case 5 is used to calrulate shop calibration of spring support instaJled above pump nozzle
- - - -
bull Technip
KHARG ETHYLENE PLANT KHARG Olefin Complex
CONTRACTOR OOCUIoENT N OWNER DOCUMENT
P N IJnIt Doc T lMtecW eoo Serial N Rev P p unit Doe T Material Code Serial Rev P
7273F 000 WI 1300 000 0 813
131 Load Cases to be calculated to comply wjtb ASME 831 3 Code Cases
~xample
CASE I W+DI+TI+P I(OPE)Operaling CASE 2 W+Pl(SUS) Deadweight + Pressure
CASE 3 U I (OCC) Seismic Load X
CASE 4 U2(OCC) Seismic Load Y
CASE 5 U3(OCC) Seismic load Z
CASE 6 LI -L2(EXP) Expansion range Code Ca~
CASE 7 W+L4+L5(OCC) Resultanl seismic load SRSS combination
ASE 8 L2+L7(OCC) Sustained plus Seismic Combined absolutelyCode Case
CASE 9 LI+L7(OCC) Operating plus Seismic combined absolutely hOI restraint (Optional)
813
CASE 10 L9+~(OCC) Maximum restrai nt loads (Optional)~ 14 FOR LOW TEMPERATURE CARBON STEEL (LTCS)
141 Stress criteria
The point (3) of the figure 3232B imposes to take into account the following load cases
Permanent static loads
bull W Weight (signed load)
bull bull P Pressure (signed load)
bull T low Temperature (signed load)
bull F exlemal loads (signed load)
Occasional static and dynamic loads
bull U seismic accelerations Corresponding to the SASS combination of the Ul (X dyion) U2 (Y direction) and U3 (Z direction) components
bull WIN Wind (unsigned load)
Remarks
I) In Caesar load case it is necessary to have by load case line only one of load cases d~=ibed her-under
2) In Caesar input all stress intensification factors shal l be equal to 1
TIle criteria is
W + P +T + F + U or WIN lt O3Sh - 413 Mpa combined in ABS( ~ shy
bull
9113
Technip
bull KHARG ETHYLENE PLANT
KHARG Olefin Complex
QVoINEA OClCUME NT N
P bull p N Unit Doc T Malerial Code Serial Ndeg Rw
913
142 Examples
Examplelr-~__~~-+~e~x~po=s~ed~to~W~ind=-~~h~~~r~o~st=a=t~~te=s~t~=s~ ~ po~rt~s-+pr=ing~s~u~p~line criteria Yes Yes Yes
bull Example File 002_01O-A_O_A (Unit 002 Calculation Number OlD Load Case File A evD)
CASE 1 W+Tl+PI+H (OPE) Operating cold condition
CASE 2 W+T2+P2+H (OPE) Operating hot conditions
CASE 3 W+PI +H (SUS) Deadweight + Pressure
CASE 4 WINl (SUS) Wind along X (Instead of OCC to avoid Snubber activation if I y)
CASES WIN2 (SUS) Wind along Z (Instead of OCC to avoid Snubber activation if y)
CASE 6 Ul (OCC) Seismic Lcentad X
CASE 7 U2 (OCe) Seismic Load Y
CASES U3 (OCC) Seismic Load Z
CASE9W+H (SUS) Deadweight + Spring hanger
CASE 10 PI (SUS) Pressure
CASE J 1 Tl (EXP) Temperarure
CASE 12 LI -L2 (EXP) thermal stress range Code Case
CASE 13 Ll -L3 (EXP) thermal suess range Code Case
CASE 14 LlI+Ll2 (EXP) full thermal stress range checking ABS combination
CASE 15 L6+L7+LS (OCC) Resultant seismic load SRSS combination CASE 16 ~9+L10+L1I+L3 (OCC) Sustained plus Wind X combined absolutely Code Ease CASE 17 L9+LI0+L11+L4 (OCC) Sustained plus Wind Z combined absolutely Code tase CASE 18 L9+L10+Lll+L15 (OCC) Sustained plus Seismic Combined absolutely Code ase
bull
bull
bull
bull
bull
Technip
KHARG ETHYLENE PLANT KHARG Olefin Complex
COHTAACTOR DOCUMENT N
-~
PEJROCHEMICAI IES DBVELOPMENT MANAG co
OWNER DOCUMENT Ndeg Unit Doe T P N
7273F 000 WI 1300 006 813 1 813 1
8 SNOW WAD (Ws)
I Emiddot~middotv O
Snow loads shall 00 applied only for cold outside lines for which design T is below 0 C and which are not protected by floor equ ipment or others
The hereafter calculated vaJue (Ws) will be classed as unifonn load foUowing Y axis (U ) in a separate Caesar input file See 7273F_OOO_CN3_CN2_1370_SAMPLlC AXLS
Design snow load 25 kgll1l2
The distribution of snow remaining on the horizontal pipe will take the shape hereu dec a reducljon factor of 072 may be applied
Ws = ( lx 051gt In x h 022D ) 25
Ws = (Ix 072 x D ) 25
Ws = 18 x D Kflrsi= 180 x D NIP Where 0 = outside diameter of pipe o r outside diameter of pipe + insulation if exist( m)
70middot
9120
o
bull Technip -D KHARG ETHYLENE PLANT ~
KHARG Olefin Complex
middot INmiddot I A~ I P~ UNo I 7273F 000 WI 1300 I 006 I A I 115 I 115
APPENDIX IV
L bull WIND PRESSURE I ELEVATION
11 Wind Basic nata I Wind pressure calcuJation
As per Project Basic Engineering 7273F-30-PP-206 Bask Design Data
Basic wind speed 160km h (44 5 m s)
Exposure Category 0
According to UBC 97 the design wind loading shall be
p= CxCxqX
where
P =Design wind pressure allevel 10 III
C~ =156 at leve1 10 m (EIIposure and gust factor-Table I6-G)
Cq I for DNlt= 50 nun
= 08 for DNgt 50 mm (Exposure and gust factor-Table I6-H)
qs= 1226 kNm2 ( Wind stagnation pressure at 10 m -Table J6-F)
lw = 1 15 (Importance factor - Table 16-K)
p = 220 xC (kNl m)
Height Above Wind pressure Ground Level
(m) PI eq (kNlm2 )
Oto 10 22
10 (0 20 247
20 to 30 264
30 10 40 276
40 to 50 286
50 to 60 289
60 to 70 293
70 1080 299
80 to 90 312
bull
bull
bull
bull
CONTRACTOR OOCUIENT bull N UniI Doc T Milttl CoOl srI N Rev Pa p
7273F 000 WI 1300 000 0 ()J 13
2 CONFIGURATION FILES USING CAESAR II
21 Unit System (7273FFIL)
CAE S A R liVERS 430
INPUT UNITS USED
UNITS 7273F NOMISCH INPUT ON
LENGTH inches
FORCE pounds
MASS(dynamics) pounds
MOMENTS(INPUn inch-pounds
MOMENTS(OUTPUT) inch-pounds
STRESS Ibssqin
TEMP SCALE degrees F
PRESSURE psig
ELASTIC MODULUS Ibslsqin
PI PE DENSITY Ibslcuin
INSULATION DENS Ibslcuin
FLUID DENSITY Ibslcuin
TRANSL STI F Ibslin
ROTATIONAL STiF inlbldeg
UNIFORM LOAD Jblin
GLOAD gs
WIND LOAD IbsJsqin
ELEVATION inches
COMPOUND LENGTH inches
DIAMETER inches
WALL THICKNESS inches
OWNER DOCUMENT Ndeg
~ Doc T Malerial CoOa Serial Ndeg Rev
1013
x 25400 mm
x 4448 N
x 0454 kg
x 0113 Nm
x 0113 Nm
x 0007 MPa
x 0556 C
x 0069 bars
x 0007 MPa
x 27680000 kgCrmiddotm
x 27680000 kgJcum
x 27680000 kgci m
x 0175 Nm
x 0113
l x 175127 NJm
x 1000 gs
x 6894757 NJ m
x 0025 m
x 25400 mm
x 1000 inch
x 25400 mm
bull bull
Technip
KHARG ETHYLENE PLANT KHARG Olefin Complex
PETROCHlMlCAL IND JES DIiVElOPMENT MANGEMENT CO
11113
Technip bull
KHARG ETHYLENE PLANT ~ KHARG Olefin Complex
iETltOCHEMICtl OEVEIOPMENT MANArCO
CONTRACTOR DOCUMENT N OWNER DOCUMENT Nmiddot ProIecl N p U Doe TwalMrolerial Code ISen N ReI P_ Proiect N I UNt Doo T~ I ~eriIII Code
7273F 000 WI I 1300 I 000 I 0 I 11113 I I I
22 Setup File ( CAESARCFG )
C A E SAR II VERS450
SETUP FILE PARAMETERS
CONNECT GEOMETRY THRU CNODES YES I MIN ALLOWED BEND ANGLE 500000 I MAXjLLOWED BEND ANGLE bull 135000 I BEND LENGTH ATIACHMENT PERCENT 100000 I MINjNGLE TO ADJACENT BEND PT 500000
LOOP CLOSURE TOLERANCE 254000mm
THERMAL BOWING HORZ TOLERANCE 100000E-04
AUTO NODE NUMBER INCREMENT 100000
ZJXIS UP NO
USE PRESSURE STIFFENING DEFAULT
ALPHA TOLERANCE 500000E-02
RESLDmiddotFORCE NO
HGR_DEF RESWGT STIF
bull 01751200E+12 Nlmm
DECOMP SNG TOL 01 OOOOOOE+ 11
BEND_AXIAL SHAPE NO
FRICT STIF 875600 Ni mm I FRICT NORM FORCE VAR 025000 I FRICT ANGLE VAR 300000 I FRICT SLIDE MULT 100000
ROD TOLERANCE 100000
ROD INC 200000
INCORE NUMERICAL CHECK NO
OUTCORE NUMERICAL CHECK NO
DEFAULT TRANS RESTRAINT STIFF 0175120E+12 Nlmm
DEFAULT ROT RESTRAINT STIFF 0112980E+12 Nmi deaJ
IGNORE SPRING HANGER STIFFNESS bull NO I
WI I middot AiHG bull _ KtVRCUE LOoO CAS ES_Odoc
rmiddot
bull
bull
Technip
KHARG ETHYLENE PLANT KHARG Olefin Complex
Setup File (
CONNECT_GEOMETRY _ THRU_CNODES
WRC-07 VERSION
WRC- 07
DEFAULT
831
WI I middot AIlaquo) Amiddot KHARGJUOAD CASFsOdoc
T
F
YES
NO
181 281
NO
DEFAULT
02206272E+OSbull
bullbull
bull
bull
Thchnip bull
KHARG ETHYLENE PLANT ~ KHARG Olefin Complex
PFffiOCHEMICAL INO bull DEVELOPMENT MANAG ~ENTCO_
CONTRACTOR DOCUMENT Ndeg OWNER DOCUMENT N
Proioct Ndeg Unit Doc TIIDEII Material Code Serial Ndeg Rev I Paae Proiect N Unit Doc Type Material Code Serial N A~ 7273F I 000 I WI I 1300 I 000 I a I 13 13 I 1313
FRP Ratio GmodlEmo(Uaxial) O2500000E+OO
FRP EalEhVhla O1527272E+OO
SetuD File (CAESARCFG Continuation)
FRP Lamina1e Type THREE
FRP Alpha O2159827E+02 C
FRP Density O1660800E+04 kocum bullEXCLUDE 12 FROM UKOOA BENDI NG NO
OUTPUT REPORTS BY LOAD CASE YES
DISPLACEMENT NODAL SORTING YES
DYNAMIC INPUT EXAMPLE TEXT MAX
TIME HIST ANIMATE YES
ENABLE AUTOSAVE YES
AUTOSAVE TIME INTERVAL O3000000E+02
PROMPTED AUTOSAVE YES
DISABLE UNDOREDO NO
STRUCTURAL DATABASE AISC89BIN
VALVE amp FLANGE GENERIC VHD
EXPANSION JT DBASE FLEXPATHJHD
PI PING SIZE SPECIFICATION ANSI
DEFAULT SPRING HANGER TABLE O5000000E+01
SYSTEM DIRECTORY NAME SYSTEM
UNITS FILE NAME 7273FFIL
ENABLE ODBC OUTPUT NO
DEFAULT SPRING HANGER TABLE LlSEGA
- bull -
WI 1 ANG bull IV IlHAAG_IELOAD CAS ES_OdOC
SRMPL6 LOf]) C(15euro5 S V REfK Ti O-l FOeC e- JlUE TO PSv oPttvlNG
bull Sldlle Aymmiddot [CIDO(UMpoundNTS AllD SETIINGSVhBACONI7173FmiddotMBACONICAESAR FILESICNj016_REV ~
bull
bull
bull
Edt
+ t
loadCose Edlcr LoadCoseOptiom Loads WlNeLoads
loads Oefned n IrtJIA loed Casu Stress Type
W -Woltllt L1 W+D1 +T1 +P1 +H Of 01 middot Displcmnt Case ~ L2 wO-iT2+P1 +H-- Of T1 middot Thermal Case tn l3 W~D1~T3~P1H ~(]S-oiit~~ Of LltgtOd e T2 Thermal Case 2 -- - _- ------- -__- T3 Thermal Case U3
l4 W+P1+H SUS __ _- -----PI middot Pr euUle Case 1 LS Wt-P1t-H-t-F1 OCC Hp middot Hydlo Prenae L6 Ul OCC --- ---- _----- H middot Hanger l oads 17 U2 OCC UI middot Unf Load eMe 11 La U3 OCC U2 -UriloodlAse 12 L9 F1 OCC U3 Uri l oad Case 13 L10 L1-l4 EXP F1 middot Cone FOIct Case 11 1 Ll1 L2-l4 J EXP Vlllet Fled W WNC middot W~ no corieris L12 L3-lS EXP
L13 LS+l7+l8 OCC L1 4 L-4+l13 ----l ~~ IL15 L1 lt-l1 3 L1 6 LJl9 (fD lO(ll ch 011 (f~tnlh OCC
STATIQUE LoR)) I- Ill
1
FW FRANCE NDG SHT16F I
CliENT
PROJECT
CPNo
EXXON
18KTA E5000 Expansion
CALCNo ISV 3310
CALC BY BEP
CHKD BY
DATE 13012006
RELIEF VALVE LOADINGS vapour
RV Nos ISV 3310
SIZE 4x3
RATING 150xlSO
ORIFICE L
bull DATA DESCRIPTION
RV SET PRESSURE
PERCENT OVERPRESSURE
Ps (l+PolOO) + 147
REliEF TEMPERATURE
1195492
RATIO OF SPECIFIC HEATS SIZING FLOW
SElECTED ORIFICE AREA
CALCULATED ORIFICE AREA
FACTORED SIZING flOW
MAX No OF WORKING VALVES
SIZING flOW PER VALVE
113600
MOLECULAR WEIGHT
GAS CONSTANT 1544M
SYMBOl UNITS
Ps BARG
Po
P PSIA T1 DegC
T Oeg R
k WI Kg h A sqin Ac sqin W2 Kgh N
W Ib h w Ibsec M
R ftlblb Oeg
bull GRAVITY IQ ftS2
FI=
2 W RI
gPA
VALUE
7 10 F2
12635 256
9528 105
- shyFl
t~ --+
~ middotFI FI
t5489 rTABIJSmn Ow COiiOmON
2853 NOn IIQRIZOllTAL IOItCIS Kt MtA CEil
2853 15489 F2
1 341532 +shy948701 F3
885 174463 ltV AT POICONllIll0N
322 AampUMING IMPACT CTOII OYl
260496 Ib 1159 N
128894 Ib 573 N
520993 Ib 2318 N -
bullbull
SARASIN-lltJ l7Technical amp Calculation Data Sheet ZI 8olto R~62IKI _____ J40 11ap11M GnlCMl
VAlVH e COlTllOlS Safety Valve
e Bomel lype Opened
Project KHARG OLEfiN COMPLEX ~A
Tag No PSV 6 453A C-Quote Ref 3A30880IOOO Sales Engineer Abdeljalill Baigar W de Commande
Operating ondl tlons Connect ons
19 InlelON shy1 fluid type Superheated Stetlm
20 Inlet Finish ANSt600 RF (125-250 AARH) 2 Capacity 78500 Kglh 21 Outlet DN J Set ptesSUe br eft 22 Outlet Finish ANSI 150 ftF 1125-250 AARH) Ol$charoe Tom p J7S C Accordinn 10 ASME 616-5
5 Variable bad pressure 0 bar eft
Cold (If lest lXess 47 bar eft 8111 of material 7 Overpressure 11 () 16 floltfv SA216 wee
SA2115WCC2 Ylt8 Operating Pressure 40 bar eft
SA216 wee Tight Closing pressUIe (MAOP) 423 bar eft 26 NoWe Stllited AlSl410 1~ 27 174 PH Stainless SteelMechanical Tomp J7S middotC ~ 28 Gaskets Stalnl St1
29 SPfinQ Chromium Allov Steel 30 AlSI431c31 Adusitina Rlna SA351 CF3M 32 Stud Al1lQrB7 JJ Alt4i1r2H Accessories
Regular Levr 35 51etUted nozzl
ReqUIred Area 31 927 om Test Gag 495 s q InIl Selected Area 41 2 om
I 839 sq in 15 Onfice p
Reaction loroe DN~ t Flow capacity 101299 Kglh 18 Noise at 30 m acc to APt521 120 dB
apprO)flTlate noise level at 30 m according to API521 (mouth noiso) )perl dlsctlarge
Customer Name TECHNIP FRANCE evlslon ~ lion ate
890 4 20-juin-2005
Cust Item Numb 7U3F RFQ 1545-01 a ely a ype pflllg a a ely alve ea1T
I I J7 Standard API 520 I )
Commercial code S46P3530AmiddotDmiddotVMM I shyI Dimensions
A- 2254 mm B- 2540 mm W - 11800 mrnIA 525PlKd~KnKb Kshl ~ Welghl() s 1523 Kg I A- 89 Inch I bullB- 100 Inch
Dati 01 calcul w - 4115 Inch Mass Capaatv W 18500 KgIh Weight( ) 3357 Pound
P1 5553 bar abs r~ C Gase Constant 143843
() Indicative Values 0 now ooeIficient Kd 0915 0
Ksn 0865 Remarks Napier equation correction Kn 1
~ 2 valves are necessary 10 reach the required capacity
Back pressure correcUon Kb 1a BUlHmiddotup back pressureO 1 berg Same calculallO1 heet lor the 1st va lve and the spare one bull
N
~
GENERAl
PEO
PROCESS
CONDITONS
bull DESIGN
DATA
bull MATERIALS
I
OPT IONS
1 T Nu~
2 Service 3 Line NUrMer 4 P amp to Numbef
5 6 Conform to 961231EC 7 Fluid T
8 NJ licable rED Table 9
0 11
12
13
14
15 16
17 19
20 21 22
PED Cal
Fluid Fluid Servlc Required Capaci
MoltcullWe hI
ratln PrtSi ur
tlll TIm tUri
Badlt Prl$IIure
AJlovtabie Ova sure
Ov esslI10 FactOI Com esslbU Latenl Heal 01 V lion
o Tl 1012812005 Pour Commenta ires
Equipment
Fluid Groo
Fluid S~I
5 cltle Gl1Ivl Set Pressure
Col
HC+H20
15489
5 02
ReHov Temperatlyene 212
Constant Varia1je Total
23 Specific Hnt RItIo lC 24 Relief Densi
25 Relief Viscosity
26 Barometric Pressure 27 28 Nozzle Flit Semi
29 Design Saely Reflef Sale -Relief 30 Type Conventional BelloIN Plot Opefatad 31 BonnetT 32 n Code
33 Sizing Basis 34 Calcula ted Area
35 Selected Area 36 Orifice De nation
37 Size Rating -Inlel 38 Size Rat - Outlet
39 40 41 42 43 Stt 44 Fla es
45 Resilient Seat Seal 46 Guide
471 Spfing 46 Wtted Material
49 50
Bonnt Disc
Ri s Bellows
51 Cap Screwed or Bolted 52 Lever Plain or Packed 53 TestGag
54 55
22-ISV 3310 0 331fD332 SHCOO20150A1A 1 l -Q2S)(l2
y Gaseous Group 1
0 1
0
09
105
4
Note 10
k
C
k p
Safety Corrventlonal
hI Solted
ASME Delaut eau de refroldissement
1812 em
L 3 150 RF 450 RF
A2 16 WCB
NOlet A216WCB
NOle 1
Note 1
NOIot
NOIel
(Note 1
No
No
INSTRUMENT SPECIFICATION
Valve Safety Pressure Relief
oxicFlammable
GasIVapo
7
2564 C
A21 6WCB SS 316 Mini
Note 1
EJflt0nMobil Chemic
Sheet 5middot11 of 46
f
No 8 Date Revision Code 2831 No C3 1052 Amiddot163 1middottVOl Rev 0
i (
II Technical amp Calculation Data Sheet SARASIN-Agt Zllloa-R~
Safety Valve Nt BiOPUIle Gt1wtI bull bull 2110 1-1_
IN I ICustomer Name TECHNIP FRANCE
891 I 4 I bull s~ I
Cuslllem Numb 7273F RFQ 1545-01
Project KHARG OLEFIN COMPLEX I Opened
I 1 I
Quote Ref Tag No PSV pound I Nde Sales Abdeljalill Baigar I
I I uperatIng onaltons
Fluid ~e Superheated Steam 19 tnle ON shy
capaci ty 78500 Kgn 20 Inlet Finish ANSI 600 RF (125-250 AARH)
3 Set presMKC 21 Outlet ON
4935 bar eM 22 OtItlet Finish ANSI 150 RF (125-250 AARH)
DiSCharge Temp 375 middotC ASME B16-5 5 Variable back presslJe bull bar eft
Cold dilf lesc press 4935 bar eft I Bill 01 I
OverptesslKe B() 10 Bod SAl16 wee a Operating ProsslKe bar elf 24 Yoke SA216 wee
25 cabull SA216 weebull bull Tlglt Closing presSlKe (MAOP) 44 415 bar eff 26 Nozzle Sellited AlSI410 bullMlaquohBnIcaI Temp J15 C 21 Disc 174 PH Stilinless Steel 28 Gaskets Stainless $t1 bullSDOM Chromium Alloy Steel 30 Golde AlSI431 31 AcluslthQRinP SAl51 CF3M 32 Stud A183flr81 33 Nul Al94gr2H
gt0 Revulr Lever
Reqllif~ Afea 32023 om 35 middot SlelUted noule
12 496 sq in TU I Gag
1 Sellcl(l(l AIel 41 2 om
I 839 sq in Orirooe p
I ReactIon loree 3016 D I Flow capacity 100996 KgIh
I Noise ill 30 m ace to AP152 1 126 dB approxmate noise level at 30 m aCCOfding to APl521 (mtluth noise) open discharge
II 37 j API52 I I I
Commercial code S46P3530A-D-VMM I
IA= 525 PlKd~Kn KbKsh I I~-middot 2254 mm 2540 mm
11800 mm
bull 1523 Kg
lA shy 89 InCh
Dab 01 COI lcul I ~ - 100 Inch
IH- 465 Inch -jshyMa55 Capaoty W 18500 KgIh 3351 Pound -IP I 553 barabs C C-ase Constant 341143 I () Indicative Values 0 now coeffiCIent Kd 09150
N Ksh 0866 w- Napier equation coffeclion Kn bull 2 valves afe necessary to reach the required capacity lt Back Pfessure correcllon Kb
BUIItmiddotup back pressurecO 1 barg 2nd Ialve set at 05 of set pranure with 10 olelpreSSure in accordill1Ce With API 520
bullbulliii
bull 11 Load cases Ioad case combinations
The following load cases f load case combinations shall be analyzed 1) always or 2) on a casemiddot to-case basis
Static load cases for operating design and pressure test conditions
L6 jillL7 I
I --shy
I --shyI I I I I
L L
I Ll 9 L20
bull ~--
Load types (iC a pplicable load types should be added) W Dead weight (pipe weight + fluid weight + insulation weight) D Displacement T Design temperature P Design internal pressure U Uniform loads (eg snow load seismic load) F External forces (forces andor moments) HP Hydro test pressure H Hanger loads WIN Wind loads (for the main wind directions) WNC Dead weight without contents (pipe weight + insulation weight) WW Water-filled weight for pressure test
bull bull bull
bull
bull ~-
bull Technip
P ec(Ndeg
n73F
KHARG ETHYLENE PLANT KHARG Olefin Complex
CONTRACTOR DOCUMENT N
P N
613
PETROCHEMICAL IN USTRJpoundS DEVElOPMENT MANA EMENT CO
OWNER DOCUMENT Ndeg
Material Code Sertal Ndeg Rev Pa
613
Example 2 r-~~~~~~~XP~osed~to~w~i~nd~~h~~=r~ost~at=ic~t==st~~sp=n=n~g~su=ppo==rt=s~ line criteria Yes Yes Yes
a Example File S_OOS_A_Obullfi (Uuil50 Calculation Number 00) Operating Load Case Fi e ArevO) J7LLA A_A
CASE 1 WNC+QI+Tt+PI+H (OPE) Operating
CASE 2 WNC+PI+H
CASE 3 WIN I
CASE 4 WlN2
CASE 5 VI
CASE 6 U2
CASE 7V3
CASE 8 Ll -L2
CASE 9 L5+L6+L7
CASE 10 L2+L3-shyCASE II L2+L4
CASE 12 L2+L9
(SUS) Deadweight (No contents) + Pressure
(SUS) Wind along X (1nstcad oroce 10 avoid Snubber activatio if any)
(SUS) Wind along Z (Instead ofoce to avoid Snubberactivarion ifany)
(OCe) Seismic Load X
(OCC) Seismic Load Y
(OCC) Seismic Load Z
(EXP) Ex pansion range Code Case
(ocq Resultant seismic load SRSS combination gt
(OCe) Sustained plus Wind X combined absolutely C I Case
(OCC) Sustained plus Wind Z combined absolutely Codf Case
(aCe) Sustained plus Seismic Combined absolutely Cod Case
b Example File S_OOSJl_O bull A (Unit 5OCalculation Number 005Hydrostatic Load case fil B
revO) 4-OlL ~ _A_A
CASE 1 WW+PI (SUS) Deadweight full of water + Hydrotest Pressure PI
bull WI I bull AHa bull_ Amiddot KHARGJELOAOCASESOdDc
bull
bull
RevO)
CASE I W+PI +TI+DI+H
CASE 2 W+PI+T2+DI+H
CASE 3 W+PI+T3+DI+H
CASE 4 W+Pl+H
CASE 5 WNC+H
CASE6UI
CASE U2
CASE 8 U3
CASE 9 L6+L+L8
CASE 10 LimiddotL4
CASE I I L2middotL4
CASE 12 L3middotL4
CASE 13 L4+L9
Technip
KHARG ETHYLENE PLANT KHARG Olefin Complex
PET1IOCJiEMCAL INOUSTIUES DEVElOfMENT MANA EMENT co
7273F
Nmiddot UtIiI Doe T
1300 000 0 713
File A
1-1 For Lines Connected to Rotating Equipmenl
Example File 002_007 _A_O_A (Unit 002 Calculation Number 007 Load ea
(OPE)
(OPE)
(OPE)
(SUS)
(SUS)
(OCC)
(OCC)
(OCC)
Operating Pump A operating 380degC
Pump B Standby 21degC (Ambient)
Operating Pump B operating 380degC
Pump A Standby 21degC (Ambient)
Operating Pump A and B hot 380ltgtlt
Deadweight + Pressure
Weight (No contents)
Seismic X
Seismic Y
Seismic Z
(ocq Resultant seismic load SRSS combination
(EXP) Thermal T 1 Pump A operating 380degC
Pump B Standby 21degC (Ambient)
(EXP) ThennaJ 12 Pump B operating 380degC
Pump A Standby 21degC (Ambient)
(EXP) Therma1 13 Pump A and B hot 380degC
(OCC) Sustained plus Seismic Combined absolutely C e Case
Note Load Case 5 is used to calrulate shop calibration of spring support instaJled above pump nozzle
- - - -
bull Technip
KHARG ETHYLENE PLANT KHARG Olefin Complex
CONTRACTOR OOCUIoENT N OWNER DOCUMENT
P N IJnIt Doc T lMtecW eoo Serial N Rev P p unit Doe T Material Code Serial Rev P
7273F 000 WI 1300 000 0 813
131 Load Cases to be calculated to comply wjtb ASME 831 3 Code Cases
~xample
CASE I W+DI+TI+P I(OPE)Operaling CASE 2 W+Pl(SUS) Deadweight + Pressure
CASE 3 U I (OCC) Seismic Load X
CASE 4 U2(OCC) Seismic Load Y
CASE 5 U3(OCC) Seismic load Z
CASE 6 LI -L2(EXP) Expansion range Code Ca~
CASE 7 W+L4+L5(OCC) Resultanl seismic load SRSS combination
ASE 8 L2+L7(OCC) Sustained plus Seismic Combined absolutelyCode Case
CASE 9 LI+L7(OCC) Operating plus Seismic combined absolutely hOI restraint (Optional)
813
CASE 10 L9+~(OCC) Maximum restrai nt loads (Optional)~ 14 FOR LOW TEMPERATURE CARBON STEEL (LTCS)
141 Stress criteria
The point (3) of the figure 3232B imposes to take into account the following load cases
Permanent static loads
bull W Weight (signed load)
bull bull P Pressure (signed load)
bull T low Temperature (signed load)
bull F exlemal loads (signed load)
Occasional static and dynamic loads
bull U seismic accelerations Corresponding to the SASS combination of the Ul (X dyion) U2 (Y direction) and U3 (Z direction) components
bull WIN Wind (unsigned load)
Remarks
I) In Caesar load case it is necessary to have by load case line only one of load cases d~=ibed her-under
2) In Caesar input all stress intensification factors shal l be equal to 1
TIle criteria is
W + P +T + F + U or WIN lt O3Sh - 413 Mpa combined in ABS( ~ shy
bull
9113
Technip
bull KHARG ETHYLENE PLANT
KHARG Olefin Complex
QVoINEA OClCUME NT N
P bull p N Unit Doc T Malerial Code Serial Ndeg Rw
913
142 Examples
Examplelr-~__~~-+~e~x~po=s~ed~to~W~ind=-~~h~~~r~o~st=a=t~~te=s~t~=s~ ~ po~rt~s-+pr=ing~s~u~p~line criteria Yes Yes Yes
bull Example File 002_01O-A_O_A (Unit 002 Calculation Number OlD Load Case File A evD)
CASE 1 W+Tl+PI+H (OPE) Operating cold condition
CASE 2 W+T2+P2+H (OPE) Operating hot conditions
CASE 3 W+PI +H (SUS) Deadweight + Pressure
CASE 4 WINl (SUS) Wind along X (Instead of OCC to avoid Snubber activation if I y)
CASES WIN2 (SUS) Wind along Z (Instead of OCC to avoid Snubber activation if y)
CASE 6 Ul (OCC) Seismic Lcentad X
CASE 7 U2 (OCe) Seismic Load Y
CASES U3 (OCC) Seismic Load Z
CASE9W+H (SUS) Deadweight + Spring hanger
CASE 10 PI (SUS) Pressure
CASE J 1 Tl (EXP) Temperarure
CASE 12 LI -L2 (EXP) thermal stress range Code Case
CASE 13 Ll -L3 (EXP) thermal suess range Code Case
CASE 14 LlI+Ll2 (EXP) full thermal stress range checking ABS combination
CASE 15 L6+L7+LS (OCC) Resultant seismic load SRSS combination CASE 16 ~9+L10+L1I+L3 (OCC) Sustained plus Wind X combined absolutely Code Ease CASE 17 L9+LI0+L11+L4 (OCC) Sustained plus Wind Z combined absolutely Code tase CASE 18 L9+L10+Lll+L15 (OCC) Sustained plus Seismic Combined absolutely Code ase
bull
bull
bull
bull
bull
Technip
KHARG ETHYLENE PLANT KHARG Olefin Complex
COHTAACTOR DOCUMENT N
-~
PEJROCHEMICAI IES DBVELOPMENT MANAG co
OWNER DOCUMENT Ndeg Unit Doe T P N
7273F 000 WI 1300 006 813 1 813 1
8 SNOW WAD (Ws)
I Emiddot~middotv O
Snow loads shall 00 applied only for cold outside lines for which design T is below 0 C and which are not protected by floor equ ipment or others
The hereafter calculated vaJue (Ws) will be classed as unifonn load foUowing Y axis (U ) in a separate Caesar input file See 7273F_OOO_CN3_CN2_1370_SAMPLlC AXLS
Design snow load 25 kgll1l2
The distribution of snow remaining on the horizontal pipe will take the shape hereu dec a reducljon factor of 072 may be applied
Ws = ( lx 051gt In x h 022D ) 25
Ws = (Ix 072 x D ) 25
Ws = 18 x D Kflrsi= 180 x D NIP Where 0 = outside diameter of pipe o r outside diameter of pipe + insulation if exist( m)
70middot
9120
o
bull Technip -D KHARG ETHYLENE PLANT ~
KHARG Olefin Complex
middot INmiddot I A~ I P~ UNo I 7273F 000 WI 1300 I 006 I A I 115 I 115
APPENDIX IV
L bull WIND PRESSURE I ELEVATION
11 Wind Basic nata I Wind pressure calcuJation
As per Project Basic Engineering 7273F-30-PP-206 Bask Design Data
Basic wind speed 160km h (44 5 m s)
Exposure Category 0
According to UBC 97 the design wind loading shall be
p= CxCxqX
where
P =Design wind pressure allevel 10 III
C~ =156 at leve1 10 m (EIIposure and gust factor-Table I6-G)
Cq I for DNlt= 50 nun
= 08 for DNgt 50 mm (Exposure and gust factor-Table I6-H)
qs= 1226 kNm2 ( Wind stagnation pressure at 10 m -Table J6-F)
lw = 1 15 (Importance factor - Table 16-K)
p = 220 xC (kNl m)
Height Above Wind pressure Ground Level
(m) PI eq (kNlm2 )
Oto 10 22
10 (0 20 247
20 to 30 264
30 10 40 276
40 to 50 286
50 to 60 289
60 to 70 293
70 1080 299
80 to 90 312
bull
bull
bull
bull
CONTRACTOR OOCUIENT bull N UniI Doc T Milttl CoOl srI N Rev Pa p
7273F 000 WI 1300 000 0 ()J 13
2 CONFIGURATION FILES USING CAESAR II
21 Unit System (7273FFIL)
CAE S A R liVERS 430
INPUT UNITS USED
UNITS 7273F NOMISCH INPUT ON
LENGTH inches
FORCE pounds
MASS(dynamics) pounds
MOMENTS(INPUn inch-pounds
MOMENTS(OUTPUT) inch-pounds
STRESS Ibssqin
TEMP SCALE degrees F
PRESSURE psig
ELASTIC MODULUS Ibslsqin
PI PE DENSITY Ibslcuin
INSULATION DENS Ibslcuin
FLUID DENSITY Ibslcuin
TRANSL STI F Ibslin
ROTATIONAL STiF inlbldeg
UNIFORM LOAD Jblin
GLOAD gs
WIND LOAD IbsJsqin
ELEVATION inches
COMPOUND LENGTH inches
DIAMETER inches
WALL THICKNESS inches
OWNER DOCUMENT Ndeg
~ Doc T Malerial CoOa Serial Ndeg Rev
1013
x 25400 mm
x 4448 N
x 0454 kg
x 0113 Nm
x 0113 Nm
x 0007 MPa
x 0556 C
x 0069 bars
x 0007 MPa
x 27680000 kgCrmiddotm
x 27680000 kgJcum
x 27680000 kgci m
x 0175 Nm
x 0113
l x 175127 NJm
x 1000 gs
x 6894757 NJ m
x 0025 m
x 25400 mm
x 1000 inch
x 25400 mm
bull bull
Technip
KHARG ETHYLENE PLANT KHARG Olefin Complex
PETROCHlMlCAL IND JES DIiVElOPMENT MANGEMENT CO
11113
Technip bull
KHARG ETHYLENE PLANT ~ KHARG Olefin Complex
iETltOCHEMICtl OEVEIOPMENT MANArCO
CONTRACTOR DOCUMENT N OWNER DOCUMENT Nmiddot ProIecl N p U Doe TwalMrolerial Code ISen N ReI P_ Proiect N I UNt Doo T~ I ~eriIII Code
7273F 000 WI I 1300 I 000 I 0 I 11113 I I I
22 Setup File ( CAESARCFG )
C A E SAR II VERS450
SETUP FILE PARAMETERS
CONNECT GEOMETRY THRU CNODES YES I MIN ALLOWED BEND ANGLE 500000 I MAXjLLOWED BEND ANGLE bull 135000 I BEND LENGTH ATIACHMENT PERCENT 100000 I MINjNGLE TO ADJACENT BEND PT 500000
LOOP CLOSURE TOLERANCE 254000mm
THERMAL BOWING HORZ TOLERANCE 100000E-04
AUTO NODE NUMBER INCREMENT 100000
ZJXIS UP NO
USE PRESSURE STIFFENING DEFAULT
ALPHA TOLERANCE 500000E-02
RESLDmiddotFORCE NO
HGR_DEF RESWGT STIF
bull 01751200E+12 Nlmm
DECOMP SNG TOL 01 OOOOOOE+ 11
BEND_AXIAL SHAPE NO
FRICT STIF 875600 Ni mm I FRICT NORM FORCE VAR 025000 I FRICT ANGLE VAR 300000 I FRICT SLIDE MULT 100000
ROD TOLERANCE 100000
ROD INC 200000
INCORE NUMERICAL CHECK NO
OUTCORE NUMERICAL CHECK NO
DEFAULT TRANS RESTRAINT STIFF 0175120E+12 Nlmm
DEFAULT ROT RESTRAINT STIFF 0112980E+12 Nmi deaJ
IGNORE SPRING HANGER STIFFNESS bull NO I
WI I middot AiHG bull _ KtVRCUE LOoO CAS ES_Odoc
rmiddot
bull
bull
Technip
KHARG ETHYLENE PLANT KHARG Olefin Complex
Setup File (
CONNECT_GEOMETRY _ THRU_CNODES
WRC-07 VERSION
WRC- 07
DEFAULT
831
WI I middot AIlaquo) Amiddot KHARGJUOAD CASFsOdoc
T
F
YES
NO
181 281
NO
DEFAULT
02206272E+OSbull
bullbull
bull
bull
Thchnip bull
KHARG ETHYLENE PLANT ~ KHARG Olefin Complex
PFffiOCHEMICAL INO bull DEVELOPMENT MANAG ~ENTCO_
CONTRACTOR DOCUMENT Ndeg OWNER DOCUMENT N
Proioct Ndeg Unit Doc TIIDEII Material Code Serial Ndeg Rev I Paae Proiect N Unit Doc Type Material Code Serial N A~ 7273F I 000 I WI I 1300 I 000 I a I 13 13 I 1313
FRP Ratio GmodlEmo(Uaxial) O2500000E+OO
FRP EalEhVhla O1527272E+OO
SetuD File (CAESARCFG Continuation)
FRP Lamina1e Type THREE
FRP Alpha O2159827E+02 C
FRP Density O1660800E+04 kocum bullEXCLUDE 12 FROM UKOOA BENDI NG NO
OUTPUT REPORTS BY LOAD CASE YES
DISPLACEMENT NODAL SORTING YES
DYNAMIC INPUT EXAMPLE TEXT MAX
TIME HIST ANIMATE YES
ENABLE AUTOSAVE YES
AUTOSAVE TIME INTERVAL O3000000E+02
PROMPTED AUTOSAVE YES
DISABLE UNDOREDO NO
STRUCTURAL DATABASE AISC89BIN
VALVE amp FLANGE GENERIC VHD
EXPANSION JT DBASE FLEXPATHJHD
PI PING SIZE SPECIFICATION ANSI
DEFAULT SPRING HANGER TABLE O5000000E+01
SYSTEM DIRECTORY NAME SYSTEM
UNITS FILE NAME 7273FFIL
ENABLE ODBC OUTPUT NO
DEFAULT SPRING HANGER TABLE LlSEGA
- bull -
WI 1 ANG bull IV IlHAAG_IELOAD CAS ES_OdOC
SRMPL6 LOf]) C(15euro5 S V REfK Ti O-l FOeC e- JlUE TO PSv oPttvlNG
bull Sldlle Aymmiddot [CIDO(UMpoundNTS AllD SETIINGSVhBACONI7173FmiddotMBACONICAESAR FILESICNj016_REV ~
bull
bull
bull
Edt
+ t
loadCose Edlcr LoadCoseOptiom Loads WlNeLoads
loads Oefned n IrtJIA loed Casu Stress Type
W -Woltllt L1 W+D1 +T1 +P1 +H Of 01 middot Displcmnt Case ~ L2 wO-iT2+P1 +H-- Of T1 middot Thermal Case tn l3 W~D1~T3~P1H ~(]S-oiit~~ Of LltgtOd e T2 Thermal Case 2 -- - _- ------- -__- T3 Thermal Case U3
l4 W+P1+H SUS __ _- -----PI middot Pr euUle Case 1 LS Wt-P1t-H-t-F1 OCC Hp middot Hydlo Prenae L6 Ul OCC --- ---- _----- H middot Hanger l oads 17 U2 OCC UI middot Unf Load eMe 11 La U3 OCC U2 -UriloodlAse 12 L9 F1 OCC U3 Uri l oad Case 13 L10 L1-l4 EXP F1 middot Cone FOIct Case 11 1 Ll1 L2-l4 J EXP Vlllet Fled W WNC middot W~ no corieris L12 L3-lS EXP
L13 LS+l7+l8 OCC L1 4 L-4+l13 ----l ~~ IL15 L1 lt-l1 3 L1 6 LJl9 (fD lO(ll ch 011 (f~tnlh OCC
STATIQUE LoR)) I- Ill
1
FW FRANCE NDG SHT16F I
CliENT
PROJECT
CPNo
EXXON
18KTA E5000 Expansion
CALCNo ISV 3310
CALC BY BEP
CHKD BY
DATE 13012006
RELIEF VALVE LOADINGS vapour
RV Nos ISV 3310
SIZE 4x3
RATING 150xlSO
ORIFICE L
bull DATA DESCRIPTION
RV SET PRESSURE
PERCENT OVERPRESSURE
Ps (l+PolOO) + 147
REliEF TEMPERATURE
1195492
RATIO OF SPECIFIC HEATS SIZING FLOW
SElECTED ORIFICE AREA
CALCULATED ORIFICE AREA
FACTORED SIZING flOW
MAX No OF WORKING VALVES
SIZING flOW PER VALVE
113600
MOLECULAR WEIGHT
GAS CONSTANT 1544M
SYMBOl UNITS
Ps BARG
Po
P PSIA T1 DegC
T Oeg R
k WI Kg h A sqin Ac sqin W2 Kgh N
W Ib h w Ibsec M
R ftlblb Oeg
bull GRAVITY IQ ftS2
FI=
2 W RI
gPA
VALUE
7 10 F2
12635 256
9528 105
- shyFl
t~ --+
~ middotFI FI
t5489 rTABIJSmn Ow COiiOmON
2853 NOn IIQRIZOllTAL IOItCIS Kt MtA CEil
2853 15489 F2
1 341532 +shy948701 F3
885 174463 ltV AT POICONllIll0N
322 AampUMING IMPACT CTOII OYl
260496 Ib 1159 N
128894 Ib 573 N
520993 Ib 2318 N -
bullbull
SARASIN-lltJ l7Technical amp Calculation Data Sheet ZI 8olto R~62IKI _____ J40 11ap11M GnlCMl
VAlVH e COlTllOlS Safety Valve
e Bomel lype Opened
Project KHARG OLEfiN COMPLEX ~A
Tag No PSV 6 453A C-Quote Ref 3A30880IOOO Sales Engineer Abdeljalill Baigar W de Commande
Operating ondl tlons Connect ons
19 InlelON shy1 fluid type Superheated Stetlm
20 Inlet Finish ANSt600 RF (125-250 AARH) 2 Capacity 78500 Kglh 21 Outlet DN J Set ptesSUe br eft 22 Outlet Finish ANSI 150 ftF 1125-250 AARH) Ol$charoe Tom p J7S C Accordinn 10 ASME 616-5
5 Variable bad pressure 0 bar eft
Cold (If lest lXess 47 bar eft 8111 of material 7 Overpressure 11 () 16 floltfv SA216 wee
SA2115WCC2 Ylt8 Operating Pressure 40 bar eft
SA216 wee Tight Closing pressUIe (MAOP) 423 bar eft 26 NoWe Stllited AlSl410 1~ 27 174 PH Stainless SteelMechanical Tomp J7S middotC ~ 28 Gaskets Stalnl St1
29 SPfinQ Chromium Allov Steel 30 AlSI431c31 Adusitina Rlna SA351 CF3M 32 Stud Al1lQrB7 JJ Alt4i1r2H Accessories
Regular Levr 35 51etUted nozzl
ReqUIred Area 31 927 om Test Gag 495 s q InIl Selected Area 41 2 om
I 839 sq in 15 Onfice p
Reaction loroe DN~ t Flow capacity 101299 Kglh 18 Noise at 30 m acc to APt521 120 dB
apprO)flTlate noise level at 30 m according to API521 (mouth noiso) )perl dlsctlarge
Customer Name TECHNIP FRANCE evlslon ~ lion ate
890 4 20-juin-2005
Cust Item Numb 7U3F RFQ 1545-01 a ely a ype pflllg a a ely alve ea1T
I I J7 Standard API 520 I )
Commercial code S46P3530AmiddotDmiddotVMM I shyI Dimensions
A- 2254 mm B- 2540 mm W - 11800 mrnIA 525PlKd~KnKb Kshl ~ Welghl() s 1523 Kg I A- 89 Inch I bullB- 100 Inch
Dati 01 calcul w - 4115 Inch Mass Capaatv W 18500 KgIh Weight( ) 3357 Pound
P1 5553 bar abs r~ C Gase Constant 143843
() Indicative Values 0 now ooeIficient Kd 0915 0
Ksn 0865 Remarks Napier equation correction Kn 1
~ 2 valves are necessary 10 reach the required capacity
Back pressure correcUon Kb 1a BUlHmiddotup back pressureO 1 berg Same calculallO1 heet lor the 1st va lve and the spare one bull
N
~
GENERAl
PEO
PROCESS
CONDITONS
bull DESIGN
DATA
bull MATERIALS
I
OPT IONS
1 T Nu~
2 Service 3 Line NUrMer 4 P amp to Numbef
5 6 Conform to 961231EC 7 Fluid T
8 NJ licable rED Table 9
0 11
12
13
14
15 16
17 19
20 21 22
PED Cal
Fluid Fluid Servlc Required Capaci
MoltcullWe hI
ratln PrtSi ur
tlll TIm tUri
Badlt Prl$IIure
AJlovtabie Ova sure
Ov esslI10 FactOI Com esslbU Latenl Heal 01 V lion
o Tl 1012812005 Pour Commenta ires
Equipment
Fluid Groo
Fluid S~I
5 cltle Gl1Ivl Set Pressure
Col
HC+H20
15489
5 02
ReHov Temperatlyene 212
Constant Varia1je Total
23 Specific Hnt RItIo lC 24 Relief Densi
25 Relief Viscosity
26 Barometric Pressure 27 28 Nozzle Flit Semi
29 Design Saely Reflef Sale -Relief 30 Type Conventional BelloIN Plot Opefatad 31 BonnetT 32 n Code
33 Sizing Basis 34 Calcula ted Area
35 Selected Area 36 Orifice De nation
37 Size Rating -Inlel 38 Size Rat - Outlet
39 40 41 42 43 Stt 44 Fla es
45 Resilient Seat Seal 46 Guide
471 Spfing 46 Wtted Material
49 50
Bonnt Disc
Ri s Bellows
51 Cap Screwed or Bolted 52 Lever Plain or Packed 53 TestGag
54 55
22-ISV 3310 0 331fD332 SHCOO20150A1A 1 l -Q2S)(l2
y Gaseous Group 1
0 1
0
09
105
4
Note 10
k
C
k p
Safety Corrventlonal
hI Solted
ASME Delaut eau de refroldissement
1812 em
L 3 150 RF 450 RF
A2 16 WCB
NOlet A216WCB
NOle 1
Note 1
NOIot
NOIel
(Note 1
No
No
INSTRUMENT SPECIFICATION
Valve Safety Pressure Relief
oxicFlammable
GasIVapo
7
2564 C
A21 6WCB SS 316 Mini
Note 1
EJflt0nMobil Chemic
Sheet 5middot11 of 46
f
No 8 Date Revision Code 2831 No C3 1052 Amiddot163 1middottVOl Rev 0
i (
II Technical amp Calculation Data Sheet SARASIN-Agt Zllloa-R~
Safety Valve Nt BiOPUIle Gt1wtI bull bull 2110 1-1_
IN I ICustomer Name TECHNIP FRANCE
891 I 4 I bull s~ I
Cuslllem Numb 7273F RFQ 1545-01
Project KHARG OLEFIN COMPLEX I Opened
I 1 I
Quote Ref Tag No PSV pound I Nde Sales Abdeljalill Baigar I
I I uperatIng onaltons
Fluid ~e Superheated Steam 19 tnle ON shy
capaci ty 78500 Kgn 20 Inlet Finish ANSI 600 RF (125-250 AARH)
3 Set presMKC 21 Outlet ON
4935 bar eM 22 OtItlet Finish ANSI 150 RF (125-250 AARH)
DiSCharge Temp 375 middotC ASME B16-5 5 Variable back presslJe bull bar eft
Cold dilf lesc press 4935 bar eft I Bill 01 I
OverptesslKe B() 10 Bod SAl16 wee a Operating ProsslKe bar elf 24 Yoke SA216 wee
25 cabull SA216 weebull bull Tlglt Closing presSlKe (MAOP) 44 415 bar eff 26 Nozzle Sellited AlSI410 bullMlaquohBnIcaI Temp J15 C 21 Disc 174 PH Stilinless Steel 28 Gaskets Stainless $t1 bullSDOM Chromium Alloy Steel 30 Golde AlSI431 31 AcluslthQRinP SAl51 CF3M 32 Stud A183flr81 33 Nul Al94gr2H
gt0 Revulr Lever
Reqllif~ Afea 32023 om 35 middot SlelUted noule
12 496 sq in TU I Gag
1 Sellcl(l(l AIel 41 2 om
I 839 sq in Orirooe p
I ReactIon loree 3016 D I Flow capacity 100996 KgIh
I Noise ill 30 m ace to AP152 1 126 dB approxmate noise level at 30 m aCCOfding to APl521 (mtluth noise) open discharge
II 37 j API52 I I I
Commercial code S46P3530A-D-VMM I
IA= 525 PlKd~Kn KbKsh I I~-middot 2254 mm 2540 mm
11800 mm
bull 1523 Kg
lA shy 89 InCh
Dab 01 COI lcul I ~ - 100 Inch
IH- 465 Inch -jshyMa55 Capaoty W 18500 KgIh 3351 Pound -IP I 553 barabs C C-ase Constant 341143 I () Indicative Values 0 now coeffiCIent Kd 09150
N Ksh 0866 w- Napier equation coffeclion Kn bull 2 valves afe necessary to reach the required capacity lt Back Pfessure correcllon Kb
BUIItmiddotup back pressurecO 1 barg 2nd Ialve set at 05 of set pranure with 10 olelpreSSure in accordill1Ce With API 520
bullbulliii
bull 11 Load cases Ioad case combinations
The following load cases f load case combinations shall be analyzed 1) always or 2) on a casemiddot to-case basis
Static load cases for operating design and pressure test conditions
L6 jillL7 I
I --shy
I --shyI I I I I
L L
I Ll 9 L20
bull ~--
Load types (iC a pplicable load types should be added) W Dead weight (pipe weight + fluid weight + insulation weight) D Displacement T Design temperature P Design internal pressure U Uniform loads (eg snow load seismic load) F External forces (forces andor moments) HP Hydro test pressure H Hanger loads WIN Wind loads (for the main wind directions) WNC Dead weight without contents (pipe weight + insulation weight) WW Water-filled weight for pressure test
bull bull bull
bull
bull ~-
bull
bull
RevO)
CASE I W+PI +TI+DI+H
CASE 2 W+PI+T2+DI+H
CASE 3 W+PI+T3+DI+H
CASE 4 W+Pl+H
CASE 5 WNC+H
CASE6UI
CASE U2
CASE 8 U3
CASE 9 L6+L+L8
CASE 10 LimiddotL4
CASE I I L2middotL4
CASE 12 L3middotL4
CASE 13 L4+L9
Technip
KHARG ETHYLENE PLANT KHARG Olefin Complex
PET1IOCJiEMCAL INOUSTIUES DEVElOfMENT MANA EMENT co
7273F
Nmiddot UtIiI Doe T
1300 000 0 713
File A
1-1 For Lines Connected to Rotating Equipmenl
Example File 002_007 _A_O_A (Unit 002 Calculation Number 007 Load ea
(OPE)
(OPE)
(OPE)
(SUS)
(SUS)
(OCC)
(OCC)
(OCC)
Operating Pump A operating 380degC
Pump B Standby 21degC (Ambient)
Operating Pump B operating 380degC
Pump A Standby 21degC (Ambient)
Operating Pump A and B hot 380ltgtlt
Deadweight + Pressure
Weight (No contents)
Seismic X
Seismic Y
Seismic Z
(ocq Resultant seismic load SRSS combination
(EXP) Thermal T 1 Pump A operating 380degC
Pump B Standby 21degC (Ambient)
(EXP) ThennaJ 12 Pump B operating 380degC
Pump A Standby 21degC (Ambient)
(EXP) Therma1 13 Pump A and B hot 380degC
(OCC) Sustained plus Seismic Combined absolutely C e Case
Note Load Case 5 is used to calrulate shop calibration of spring support instaJled above pump nozzle
- - - -
bull Technip
KHARG ETHYLENE PLANT KHARG Olefin Complex
CONTRACTOR OOCUIoENT N OWNER DOCUMENT
P N IJnIt Doc T lMtecW eoo Serial N Rev P p unit Doe T Material Code Serial Rev P
7273F 000 WI 1300 000 0 813
131 Load Cases to be calculated to comply wjtb ASME 831 3 Code Cases
~xample
CASE I W+DI+TI+P I(OPE)Operaling CASE 2 W+Pl(SUS) Deadweight + Pressure
CASE 3 U I (OCC) Seismic Load X
CASE 4 U2(OCC) Seismic Load Y
CASE 5 U3(OCC) Seismic load Z
CASE 6 LI -L2(EXP) Expansion range Code Ca~
CASE 7 W+L4+L5(OCC) Resultanl seismic load SRSS combination
ASE 8 L2+L7(OCC) Sustained plus Seismic Combined absolutelyCode Case
CASE 9 LI+L7(OCC) Operating plus Seismic combined absolutely hOI restraint (Optional)
813
CASE 10 L9+~(OCC) Maximum restrai nt loads (Optional)~ 14 FOR LOW TEMPERATURE CARBON STEEL (LTCS)
141 Stress criteria
The point (3) of the figure 3232B imposes to take into account the following load cases
Permanent static loads
bull W Weight (signed load)
bull bull P Pressure (signed load)
bull T low Temperature (signed load)
bull F exlemal loads (signed load)
Occasional static and dynamic loads
bull U seismic accelerations Corresponding to the SASS combination of the Ul (X dyion) U2 (Y direction) and U3 (Z direction) components
bull WIN Wind (unsigned load)
Remarks
I) In Caesar load case it is necessary to have by load case line only one of load cases d~=ibed her-under
2) In Caesar input all stress intensification factors shal l be equal to 1
TIle criteria is
W + P +T + F + U or WIN lt O3Sh - 413 Mpa combined in ABS( ~ shy
bull
9113
Technip
bull KHARG ETHYLENE PLANT
KHARG Olefin Complex
QVoINEA OClCUME NT N
P bull p N Unit Doc T Malerial Code Serial Ndeg Rw
913
142 Examples
Examplelr-~__~~-+~e~x~po=s~ed~to~W~ind=-~~h~~~r~o~st=a=t~~te=s~t~=s~ ~ po~rt~s-+pr=ing~s~u~p~line criteria Yes Yes Yes
bull Example File 002_01O-A_O_A (Unit 002 Calculation Number OlD Load Case File A evD)
CASE 1 W+Tl+PI+H (OPE) Operating cold condition
CASE 2 W+T2+P2+H (OPE) Operating hot conditions
CASE 3 W+PI +H (SUS) Deadweight + Pressure
CASE 4 WINl (SUS) Wind along X (Instead of OCC to avoid Snubber activation if I y)
CASES WIN2 (SUS) Wind along Z (Instead of OCC to avoid Snubber activation if y)
CASE 6 Ul (OCC) Seismic Lcentad X
CASE 7 U2 (OCe) Seismic Load Y
CASES U3 (OCC) Seismic Load Z
CASE9W+H (SUS) Deadweight + Spring hanger
CASE 10 PI (SUS) Pressure
CASE J 1 Tl (EXP) Temperarure
CASE 12 LI -L2 (EXP) thermal stress range Code Case
CASE 13 Ll -L3 (EXP) thermal suess range Code Case
CASE 14 LlI+Ll2 (EXP) full thermal stress range checking ABS combination
CASE 15 L6+L7+LS (OCC) Resultant seismic load SRSS combination CASE 16 ~9+L10+L1I+L3 (OCC) Sustained plus Wind X combined absolutely Code Ease CASE 17 L9+LI0+L11+L4 (OCC) Sustained plus Wind Z combined absolutely Code tase CASE 18 L9+L10+Lll+L15 (OCC) Sustained plus Seismic Combined absolutely Code ase
bull
bull
bull
bull
bull
Technip
KHARG ETHYLENE PLANT KHARG Olefin Complex
COHTAACTOR DOCUMENT N
-~
PEJROCHEMICAI IES DBVELOPMENT MANAG co
OWNER DOCUMENT Ndeg Unit Doe T P N
7273F 000 WI 1300 006 813 1 813 1
8 SNOW WAD (Ws)
I Emiddot~middotv O
Snow loads shall 00 applied only for cold outside lines for which design T is below 0 C and which are not protected by floor equ ipment or others
The hereafter calculated vaJue (Ws) will be classed as unifonn load foUowing Y axis (U ) in a separate Caesar input file See 7273F_OOO_CN3_CN2_1370_SAMPLlC AXLS
Design snow load 25 kgll1l2
The distribution of snow remaining on the horizontal pipe will take the shape hereu dec a reducljon factor of 072 may be applied
Ws = ( lx 051gt In x h 022D ) 25
Ws = (Ix 072 x D ) 25
Ws = 18 x D Kflrsi= 180 x D NIP Where 0 = outside diameter of pipe o r outside diameter of pipe + insulation if exist( m)
70middot
9120
o
bull Technip -D KHARG ETHYLENE PLANT ~
KHARG Olefin Complex
middot INmiddot I A~ I P~ UNo I 7273F 000 WI 1300 I 006 I A I 115 I 115
APPENDIX IV
L bull WIND PRESSURE I ELEVATION
11 Wind Basic nata I Wind pressure calcuJation
As per Project Basic Engineering 7273F-30-PP-206 Bask Design Data
Basic wind speed 160km h (44 5 m s)
Exposure Category 0
According to UBC 97 the design wind loading shall be
p= CxCxqX
where
P =Design wind pressure allevel 10 III
C~ =156 at leve1 10 m (EIIposure and gust factor-Table I6-G)
Cq I for DNlt= 50 nun
= 08 for DNgt 50 mm (Exposure and gust factor-Table I6-H)
qs= 1226 kNm2 ( Wind stagnation pressure at 10 m -Table J6-F)
lw = 1 15 (Importance factor - Table 16-K)
p = 220 xC (kNl m)
Height Above Wind pressure Ground Level
(m) PI eq (kNlm2 )
Oto 10 22
10 (0 20 247
20 to 30 264
30 10 40 276
40 to 50 286
50 to 60 289
60 to 70 293
70 1080 299
80 to 90 312
bull
bull
bull
bull
CONTRACTOR OOCUIENT bull N UniI Doc T Milttl CoOl srI N Rev Pa p
7273F 000 WI 1300 000 0 ()J 13
2 CONFIGURATION FILES USING CAESAR II
21 Unit System (7273FFIL)
CAE S A R liVERS 430
INPUT UNITS USED
UNITS 7273F NOMISCH INPUT ON
LENGTH inches
FORCE pounds
MASS(dynamics) pounds
MOMENTS(INPUn inch-pounds
MOMENTS(OUTPUT) inch-pounds
STRESS Ibssqin
TEMP SCALE degrees F
PRESSURE psig
ELASTIC MODULUS Ibslsqin
PI PE DENSITY Ibslcuin
INSULATION DENS Ibslcuin
FLUID DENSITY Ibslcuin
TRANSL STI F Ibslin
ROTATIONAL STiF inlbldeg
UNIFORM LOAD Jblin
GLOAD gs
WIND LOAD IbsJsqin
ELEVATION inches
COMPOUND LENGTH inches
DIAMETER inches
WALL THICKNESS inches
OWNER DOCUMENT Ndeg
~ Doc T Malerial CoOa Serial Ndeg Rev
1013
x 25400 mm
x 4448 N
x 0454 kg
x 0113 Nm
x 0113 Nm
x 0007 MPa
x 0556 C
x 0069 bars
x 0007 MPa
x 27680000 kgCrmiddotm
x 27680000 kgJcum
x 27680000 kgci m
x 0175 Nm
x 0113
l x 175127 NJm
x 1000 gs
x 6894757 NJ m
x 0025 m
x 25400 mm
x 1000 inch
x 25400 mm
bull bull
Technip
KHARG ETHYLENE PLANT KHARG Olefin Complex
PETROCHlMlCAL IND JES DIiVElOPMENT MANGEMENT CO
11113
Technip bull
KHARG ETHYLENE PLANT ~ KHARG Olefin Complex
iETltOCHEMICtl OEVEIOPMENT MANArCO
CONTRACTOR DOCUMENT N OWNER DOCUMENT Nmiddot ProIecl N p U Doe TwalMrolerial Code ISen N ReI P_ Proiect N I UNt Doo T~ I ~eriIII Code
7273F 000 WI I 1300 I 000 I 0 I 11113 I I I
22 Setup File ( CAESARCFG )
C A E SAR II VERS450
SETUP FILE PARAMETERS
CONNECT GEOMETRY THRU CNODES YES I MIN ALLOWED BEND ANGLE 500000 I MAXjLLOWED BEND ANGLE bull 135000 I BEND LENGTH ATIACHMENT PERCENT 100000 I MINjNGLE TO ADJACENT BEND PT 500000
LOOP CLOSURE TOLERANCE 254000mm
THERMAL BOWING HORZ TOLERANCE 100000E-04
AUTO NODE NUMBER INCREMENT 100000
ZJXIS UP NO
USE PRESSURE STIFFENING DEFAULT
ALPHA TOLERANCE 500000E-02
RESLDmiddotFORCE NO
HGR_DEF RESWGT STIF
bull 01751200E+12 Nlmm
DECOMP SNG TOL 01 OOOOOOE+ 11
BEND_AXIAL SHAPE NO
FRICT STIF 875600 Ni mm I FRICT NORM FORCE VAR 025000 I FRICT ANGLE VAR 300000 I FRICT SLIDE MULT 100000
ROD TOLERANCE 100000
ROD INC 200000
INCORE NUMERICAL CHECK NO
OUTCORE NUMERICAL CHECK NO
DEFAULT TRANS RESTRAINT STIFF 0175120E+12 Nlmm
DEFAULT ROT RESTRAINT STIFF 0112980E+12 Nmi deaJ
IGNORE SPRING HANGER STIFFNESS bull NO I
WI I middot AiHG bull _ KtVRCUE LOoO CAS ES_Odoc
rmiddot
bull
bull
Technip
KHARG ETHYLENE PLANT KHARG Olefin Complex
Setup File (
CONNECT_GEOMETRY _ THRU_CNODES
WRC-07 VERSION
WRC- 07
DEFAULT
831
WI I middot AIlaquo) Amiddot KHARGJUOAD CASFsOdoc
T
F
YES
NO
181 281
NO
DEFAULT
02206272E+OSbull
bullbull
bull
bull
Thchnip bull
KHARG ETHYLENE PLANT ~ KHARG Olefin Complex
PFffiOCHEMICAL INO bull DEVELOPMENT MANAG ~ENTCO_
CONTRACTOR DOCUMENT Ndeg OWNER DOCUMENT N
Proioct Ndeg Unit Doc TIIDEII Material Code Serial Ndeg Rev I Paae Proiect N Unit Doc Type Material Code Serial N A~ 7273F I 000 I WI I 1300 I 000 I a I 13 13 I 1313
FRP Ratio GmodlEmo(Uaxial) O2500000E+OO
FRP EalEhVhla O1527272E+OO
SetuD File (CAESARCFG Continuation)
FRP Lamina1e Type THREE
FRP Alpha O2159827E+02 C
FRP Density O1660800E+04 kocum bullEXCLUDE 12 FROM UKOOA BENDI NG NO
OUTPUT REPORTS BY LOAD CASE YES
DISPLACEMENT NODAL SORTING YES
DYNAMIC INPUT EXAMPLE TEXT MAX
TIME HIST ANIMATE YES
ENABLE AUTOSAVE YES
AUTOSAVE TIME INTERVAL O3000000E+02
PROMPTED AUTOSAVE YES
DISABLE UNDOREDO NO
STRUCTURAL DATABASE AISC89BIN
VALVE amp FLANGE GENERIC VHD
EXPANSION JT DBASE FLEXPATHJHD
PI PING SIZE SPECIFICATION ANSI
DEFAULT SPRING HANGER TABLE O5000000E+01
SYSTEM DIRECTORY NAME SYSTEM
UNITS FILE NAME 7273FFIL
ENABLE ODBC OUTPUT NO
DEFAULT SPRING HANGER TABLE LlSEGA
- bull -
WI 1 ANG bull IV IlHAAG_IELOAD CAS ES_OdOC
SRMPL6 LOf]) C(15euro5 S V REfK Ti O-l FOeC e- JlUE TO PSv oPttvlNG
bull Sldlle Aymmiddot [CIDO(UMpoundNTS AllD SETIINGSVhBACONI7173FmiddotMBACONICAESAR FILESICNj016_REV ~
bull
bull
bull
Edt
+ t
loadCose Edlcr LoadCoseOptiom Loads WlNeLoads
loads Oefned n IrtJIA loed Casu Stress Type
W -Woltllt L1 W+D1 +T1 +P1 +H Of 01 middot Displcmnt Case ~ L2 wO-iT2+P1 +H-- Of T1 middot Thermal Case tn l3 W~D1~T3~P1H ~(]S-oiit~~ Of LltgtOd e T2 Thermal Case 2 -- - _- ------- -__- T3 Thermal Case U3
l4 W+P1+H SUS __ _- -----PI middot Pr euUle Case 1 LS Wt-P1t-H-t-F1 OCC Hp middot Hydlo Prenae L6 Ul OCC --- ---- _----- H middot Hanger l oads 17 U2 OCC UI middot Unf Load eMe 11 La U3 OCC U2 -UriloodlAse 12 L9 F1 OCC U3 Uri l oad Case 13 L10 L1-l4 EXP F1 middot Cone FOIct Case 11 1 Ll1 L2-l4 J EXP Vlllet Fled W WNC middot W~ no corieris L12 L3-lS EXP
L13 LS+l7+l8 OCC L1 4 L-4+l13 ----l ~~ IL15 L1 lt-l1 3 L1 6 LJl9 (fD lO(ll ch 011 (f~tnlh OCC
STATIQUE LoR)) I- Ill
1
FW FRANCE NDG SHT16F I
CliENT
PROJECT
CPNo
EXXON
18KTA E5000 Expansion
CALCNo ISV 3310
CALC BY BEP
CHKD BY
DATE 13012006
RELIEF VALVE LOADINGS vapour
RV Nos ISV 3310
SIZE 4x3
RATING 150xlSO
ORIFICE L
bull DATA DESCRIPTION
RV SET PRESSURE
PERCENT OVERPRESSURE
Ps (l+PolOO) + 147
REliEF TEMPERATURE
1195492
RATIO OF SPECIFIC HEATS SIZING FLOW
SElECTED ORIFICE AREA
CALCULATED ORIFICE AREA
FACTORED SIZING flOW
MAX No OF WORKING VALVES
SIZING flOW PER VALVE
113600
MOLECULAR WEIGHT
GAS CONSTANT 1544M
SYMBOl UNITS
Ps BARG
Po
P PSIA T1 DegC
T Oeg R
k WI Kg h A sqin Ac sqin W2 Kgh N
W Ib h w Ibsec M
R ftlblb Oeg
bull GRAVITY IQ ftS2
FI=
2 W RI
gPA
VALUE
7 10 F2
12635 256
9528 105
- shyFl
t~ --+
~ middotFI FI
t5489 rTABIJSmn Ow COiiOmON
2853 NOn IIQRIZOllTAL IOItCIS Kt MtA CEil
2853 15489 F2
1 341532 +shy948701 F3
885 174463 ltV AT POICONllIll0N
322 AampUMING IMPACT CTOII OYl
260496 Ib 1159 N
128894 Ib 573 N
520993 Ib 2318 N -
bullbull
SARASIN-lltJ l7Technical amp Calculation Data Sheet ZI 8olto R~62IKI _____ J40 11ap11M GnlCMl
VAlVH e COlTllOlS Safety Valve
e Bomel lype Opened
Project KHARG OLEfiN COMPLEX ~A
Tag No PSV 6 453A C-Quote Ref 3A30880IOOO Sales Engineer Abdeljalill Baigar W de Commande
Operating ondl tlons Connect ons
19 InlelON shy1 fluid type Superheated Stetlm
20 Inlet Finish ANSt600 RF (125-250 AARH) 2 Capacity 78500 Kglh 21 Outlet DN J Set ptesSUe br eft 22 Outlet Finish ANSI 150 ftF 1125-250 AARH) Ol$charoe Tom p J7S C Accordinn 10 ASME 616-5
5 Variable bad pressure 0 bar eft
Cold (If lest lXess 47 bar eft 8111 of material 7 Overpressure 11 () 16 floltfv SA216 wee
SA2115WCC2 Ylt8 Operating Pressure 40 bar eft
SA216 wee Tight Closing pressUIe (MAOP) 423 bar eft 26 NoWe Stllited AlSl410 1~ 27 174 PH Stainless SteelMechanical Tomp J7S middotC ~ 28 Gaskets Stalnl St1
29 SPfinQ Chromium Allov Steel 30 AlSI431c31 Adusitina Rlna SA351 CF3M 32 Stud Al1lQrB7 JJ Alt4i1r2H Accessories
Regular Levr 35 51etUted nozzl
ReqUIred Area 31 927 om Test Gag 495 s q InIl Selected Area 41 2 om
I 839 sq in 15 Onfice p
Reaction loroe DN~ t Flow capacity 101299 Kglh 18 Noise at 30 m acc to APt521 120 dB
apprO)flTlate noise level at 30 m according to API521 (mouth noiso) )perl dlsctlarge
Customer Name TECHNIP FRANCE evlslon ~ lion ate
890 4 20-juin-2005
Cust Item Numb 7U3F RFQ 1545-01 a ely a ype pflllg a a ely alve ea1T
I I J7 Standard API 520 I )
Commercial code S46P3530AmiddotDmiddotVMM I shyI Dimensions
A- 2254 mm B- 2540 mm W - 11800 mrnIA 525PlKd~KnKb Kshl ~ Welghl() s 1523 Kg I A- 89 Inch I bullB- 100 Inch
Dati 01 calcul w - 4115 Inch Mass Capaatv W 18500 KgIh Weight( ) 3357 Pound
P1 5553 bar abs r~ C Gase Constant 143843
() Indicative Values 0 now ooeIficient Kd 0915 0
Ksn 0865 Remarks Napier equation correction Kn 1
~ 2 valves are necessary 10 reach the required capacity
Back pressure correcUon Kb 1a BUlHmiddotup back pressureO 1 berg Same calculallO1 heet lor the 1st va lve and the spare one bull
N
~
GENERAl
PEO
PROCESS
CONDITONS
bull DESIGN
DATA
bull MATERIALS
I
OPT IONS
1 T Nu~
2 Service 3 Line NUrMer 4 P amp to Numbef
5 6 Conform to 961231EC 7 Fluid T
8 NJ licable rED Table 9
0 11
12
13
14
15 16
17 19
20 21 22
PED Cal
Fluid Fluid Servlc Required Capaci
MoltcullWe hI
ratln PrtSi ur
tlll TIm tUri
Badlt Prl$IIure
AJlovtabie Ova sure
Ov esslI10 FactOI Com esslbU Latenl Heal 01 V lion
o Tl 1012812005 Pour Commenta ires
Equipment
Fluid Groo
Fluid S~I
5 cltle Gl1Ivl Set Pressure
Col
HC+H20
15489
5 02
ReHov Temperatlyene 212
Constant Varia1je Total
23 Specific Hnt RItIo lC 24 Relief Densi
25 Relief Viscosity
26 Barometric Pressure 27 28 Nozzle Flit Semi
29 Design Saely Reflef Sale -Relief 30 Type Conventional BelloIN Plot Opefatad 31 BonnetT 32 n Code
33 Sizing Basis 34 Calcula ted Area
35 Selected Area 36 Orifice De nation
37 Size Rating -Inlel 38 Size Rat - Outlet
39 40 41 42 43 Stt 44 Fla es
45 Resilient Seat Seal 46 Guide
471 Spfing 46 Wtted Material
49 50
Bonnt Disc
Ri s Bellows
51 Cap Screwed or Bolted 52 Lever Plain or Packed 53 TestGag
54 55
22-ISV 3310 0 331fD332 SHCOO20150A1A 1 l -Q2S)(l2
y Gaseous Group 1
0 1
0
09
105
4
Note 10
k
C
k p
Safety Corrventlonal
hI Solted
ASME Delaut eau de refroldissement
1812 em
L 3 150 RF 450 RF
A2 16 WCB
NOlet A216WCB
NOle 1
Note 1
NOIot
NOIel
(Note 1
No
No
INSTRUMENT SPECIFICATION
Valve Safety Pressure Relief
oxicFlammable
GasIVapo
7
2564 C
A21 6WCB SS 316 Mini
Note 1
EJflt0nMobil Chemic
Sheet 5middot11 of 46
f
No 8 Date Revision Code 2831 No C3 1052 Amiddot163 1middottVOl Rev 0
i (
II Technical amp Calculation Data Sheet SARASIN-Agt Zllloa-R~
Safety Valve Nt BiOPUIle Gt1wtI bull bull 2110 1-1_
IN I ICustomer Name TECHNIP FRANCE
891 I 4 I bull s~ I
Cuslllem Numb 7273F RFQ 1545-01
Project KHARG OLEFIN COMPLEX I Opened
I 1 I
Quote Ref Tag No PSV pound I Nde Sales Abdeljalill Baigar I
I I uperatIng onaltons
Fluid ~e Superheated Steam 19 tnle ON shy
capaci ty 78500 Kgn 20 Inlet Finish ANSI 600 RF (125-250 AARH)
3 Set presMKC 21 Outlet ON
4935 bar eM 22 OtItlet Finish ANSI 150 RF (125-250 AARH)
DiSCharge Temp 375 middotC ASME B16-5 5 Variable back presslJe bull bar eft
Cold dilf lesc press 4935 bar eft I Bill 01 I
OverptesslKe B() 10 Bod SAl16 wee a Operating ProsslKe bar elf 24 Yoke SA216 wee
25 cabull SA216 weebull bull Tlglt Closing presSlKe (MAOP) 44 415 bar eff 26 Nozzle Sellited AlSI410 bullMlaquohBnIcaI Temp J15 C 21 Disc 174 PH Stilinless Steel 28 Gaskets Stainless $t1 bullSDOM Chromium Alloy Steel 30 Golde AlSI431 31 AcluslthQRinP SAl51 CF3M 32 Stud A183flr81 33 Nul Al94gr2H
gt0 Revulr Lever
Reqllif~ Afea 32023 om 35 middot SlelUted noule
12 496 sq in TU I Gag
1 Sellcl(l(l AIel 41 2 om
I 839 sq in Orirooe p
I ReactIon loree 3016 D I Flow capacity 100996 KgIh
I Noise ill 30 m ace to AP152 1 126 dB approxmate noise level at 30 m aCCOfding to APl521 (mtluth noise) open discharge
II 37 j API52 I I I
Commercial code S46P3530A-D-VMM I
IA= 525 PlKd~Kn KbKsh I I~-middot 2254 mm 2540 mm
11800 mm
bull 1523 Kg
lA shy 89 InCh
Dab 01 COI lcul I ~ - 100 Inch
IH- 465 Inch -jshyMa55 Capaoty W 18500 KgIh 3351 Pound -IP I 553 barabs C C-ase Constant 341143 I () Indicative Values 0 now coeffiCIent Kd 09150
N Ksh 0866 w- Napier equation coffeclion Kn bull 2 valves afe necessary to reach the required capacity lt Back Pfessure correcllon Kb
BUIItmiddotup back pressurecO 1 barg 2nd Ialve set at 05 of set pranure with 10 olelpreSSure in accordill1Ce With API 520
bullbulliii
bull 11 Load cases Ioad case combinations
The following load cases f load case combinations shall be analyzed 1) always or 2) on a casemiddot to-case basis
Static load cases for operating design and pressure test conditions
L6 jillL7 I
I --shy
I --shyI I I I I
L L
I Ll 9 L20
bull ~--
Load types (iC a pplicable load types should be added) W Dead weight (pipe weight + fluid weight + insulation weight) D Displacement T Design temperature P Design internal pressure U Uniform loads (eg snow load seismic load) F External forces (forces andor moments) HP Hydro test pressure H Hanger loads WIN Wind loads (for the main wind directions) WNC Dead weight without contents (pipe weight + insulation weight) WW Water-filled weight for pressure test
bull bull bull
bull
bull ~-
- - - -
bull Technip
KHARG ETHYLENE PLANT KHARG Olefin Complex
CONTRACTOR OOCUIoENT N OWNER DOCUMENT
P N IJnIt Doc T lMtecW eoo Serial N Rev P p unit Doe T Material Code Serial Rev P
7273F 000 WI 1300 000 0 813
131 Load Cases to be calculated to comply wjtb ASME 831 3 Code Cases
~xample
CASE I W+DI+TI+P I(OPE)Operaling CASE 2 W+Pl(SUS) Deadweight + Pressure
CASE 3 U I (OCC) Seismic Load X
CASE 4 U2(OCC) Seismic Load Y
CASE 5 U3(OCC) Seismic load Z
CASE 6 LI -L2(EXP) Expansion range Code Ca~
CASE 7 W+L4+L5(OCC) Resultanl seismic load SRSS combination
ASE 8 L2+L7(OCC) Sustained plus Seismic Combined absolutelyCode Case
CASE 9 LI+L7(OCC) Operating plus Seismic combined absolutely hOI restraint (Optional)
813
CASE 10 L9+~(OCC) Maximum restrai nt loads (Optional)~ 14 FOR LOW TEMPERATURE CARBON STEEL (LTCS)
141 Stress criteria
The point (3) of the figure 3232B imposes to take into account the following load cases
Permanent static loads
bull W Weight (signed load)
bull bull P Pressure (signed load)
bull T low Temperature (signed load)
bull F exlemal loads (signed load)
Occasional static and dynamic loads
bull U seismic accelerations Corresponding to the SASS combination of the Ul (X dyion) U2 (Y direction) and U3 (Z direction) components
bull WIN Wind (unsigned load)
Remarks
I) In Caesar load case it is necessary to have by load case line only one of load cases d~=ibed her-under
2) In Caesar input all stress intensification factors shal l be equal to 1
TIle criteria is
W + P +T + F + U or WIN lt O3Sh - 413 Mpa combined in ABS( ~ shy
bull
9113
Technip
bull KHARG ETHYLENE PLANT
KHARG Olefin Complex
QVoINEA OClCUME NT N
P bull p N Unit Doc T Malerial Code Serial Ndeg Rw
913
142 Examples
Examplelr-~__~~-+~e~x~po=s~ed~to~W~ind=-~~h~~~r~o~st=a=t~~te=s~t~=s~ ~ po~rt~s-+pr=ing~s~u~p~line criteria Yes Yes Yes
bull Example File 002_01O-A_O_A (Unit 002 Calculation Number OlD Load Case File A evD)
CASE 1 W+Tl+PI+H (OPE) Operating cold condition
CASE 2 W+T2+P2+H (OPE) Operating hot conditions
CASE 3 W+PI +H (SUS) Deadweight + Pressure
CASE 4 WINl (SUS) Wind along X (Instead of OCC to avoid Snubber activation if I y)
CASES WIN2 (SUS) Wind along Z (Instead of OCC to avoid Snubber activation if y)
CASE 6 Ul (OCC) Seismic Lcentad X
CASE 7 U2 (OCe) Seismic Load Y
CASES U3 (OCC) Seismic Load Z
CASE9W+H (SUS) Deadweight + Spring hanger
CASE 10 PI (SUS) Pressure
CASE J 1 Tl (EXP) Temperarure
CASE 12 LI -L2 (EXP) thermal stress range Code Case
CASE 13 Ll -L3 (EXP) thermal suess range Code Case
CASE 14 LlI+Ll2 (EXP) full thermal stress range checking ABS combination
CASE 15 L6+L7+LS (OCC) Resultant seismic load SRSS combination CASE 16 ~9+L10+L1I+L3 (OCC) Sustained plus Wind X combined absolutely Code Ease CASE 17 L9+LI0+L11+L4 (OCC) Sustained plus Wind Z combined absolutely Code tase CASE 18 L9+L10+Lll+L15 (OCC) Sustained plus Seismic Combined absolutely Code ase
bull
bull
bull
bull
bull
Technip
KHARG ETHYLENE PLANT KHARG Olefin Complex
COHTAACTOR DOCUMENT N
-~
PEJROCHEMICAI IES DBVELOPMENT MANAG co
OWNER DOCUMENT Ndeg Unit Doe T P N
7273F 000 WI 1300 006 813 1 813 1
8 SNOW WAD (Ws)
I Emiddot~middotv O
Snow loads shall 00 applied only for cold outside lines for which design T is below 0 C and which are not protected by floor equ ipment or others
The hereafter calculated vaJue (Ws) will be classed as unifonn load foUowing Y axis (U ) in a separate Caesar input file See 7273F_OOO_CN3_CN2_1370_SAMPLlC AXLS
Design snow load 25 kgll1l2
The distribution of snow remaining on the horizontal pipe will take the shape hereu dec a reducljon factor of 072 may be applied
Ws = ( lx 051gt In x h 022D ) 25
Ws = (Ix 072 x D ) 25
Ws = 18 x D Kflrsi= 180 x D NIP Where 0 = outside diameter of pipe o r outside diameter of pipe + insulation if exist( m)
70middot
9120
o
bull Technip -D KHARG ETHYLENE PLANT ~
KHARG Olefin Complex
middot INmiddot I A~ I P~ UNo I 7273F 000 WI 1300 I 006 I A I 115 I 115
APPENDIX IV
L bull WIND PRESSURE I ELEVATION
11 Wind Basic nata I Wind pressure calcuJation
As per Project Basic Engineering 7273F-30-PP-206 Bask Design Data
Basic wind speed 160km h (44 5 m s)
Exposure Category 0
According to UBC 97 the design wind loading shall be
p= CxCxqX
where
P =Design wind pressure allevel 10 III
C~ =156 at leve1 10 m (EIIposure and gust factor-Table I6-G)
Cq I for DNlt= 50 nun
= 08 for DNgt 50 mm (Exposure and gust factor-Table I6-H)
qs= 1226 kNm2 ( Wind stagnation pressure at 10 m -Table J6-F)
lw = 1 15 (Importance factor - Table 16-K)
p = 220 xC (kNl m)
Height Above Wind pressure Ground Level
(m) PI eq (kNlm2 )
Oto 10 22
10 (0 20 247
20 to 30 264
30 10 40 276
40 to 50 286
50 to 60 289
60 to 70 293
70 1080 299
80 to 90 312
bull
bull
bull
bull
CONTRACTOR OOCUIENT bull N UniI Doc T Milttl CoOl srI N Rev Pa p
7273F 000 WI 1300 000 0 ()J 13
2 CONFIGURATION FILES USING CAESAR II
21 Unit System (7273FFIL)
CAE S A R liVERS 430
INPUT UNITS USED
UNITS 7273F NOMISCH INPUT ON
LENGTH inches
FORCE pounds
MASS(dynamics) pounds
MOMENTS(INPUn inch-pounds
MOMENTS(OUTPUT) inch-pounds
STRESS Ibssqin
TEMP SCALE degrees F
PRESSURE psig
ELASTIC MODULUS Ibslsqin
PI PE DENSITY Ibslcuin
INSULATION DENS Ibslcuin
FLUID DENSITY Ibslcuin
TRANSL STI F Ibslin
ROTATIONAL STiF inlbldeg
UNIFORM LOAD Jblin
GLOAD gs
WIND LOAD IbsJsqin
ELEVATION inches
COMPOUND LENGTH inches
DIAMETER inches
WALL THICKNESS inches
OWNER DOCUMENT Ndeg
~ Doc T Malerial CoOa Serial Ndeg Rev
1013
x 25400 mm
x 4448 N
x 0454 kg
x 0113 Nm
x 0113 Nm
x 0007 MPa
x 0556 C
x 0069 bars
x 0007 MPa
x 27680000 kgCrmiddotm
x 27680000 kgJcum
x 27680000 kgci m
x 0175 Nm
x 0113
l x 175127 NJm
x 1000 gs
x 6894757 NJ m
x 0025 m
x 25400 mm
x 1000 inch
x 25400 mm
bull bull
Technip
KHARG ETHYLENE PLANT KHARG Olefin Complex
PETROCHlMlCAL IND JES DIiVElOPMENT MANGEMENT CO
11113
Technip bull
KHARG ETHYLENE PLANT ~ KHARG Olefin Complex
iETltOCHEMICtl OEVEIOPMENT MANArCO
CONTRACTOR DOCUMENT N OWNER DOCUMENT Nmiddot ProIecl N p U Doe TwalMrolerial Code ISen N ReI P_ Proiect N I UNt Doo T~ I ~eriIII Code
7273F 000 WI I 1300 I 000 I 0 I 11113 I I I
22 Setup File ( CAESARCFG )
C A E SAR II VERS450
SETUP FILE PARAMETERS
CONNECT GEOMETRY THRU CNODES YES I MIN ALLOWED BEND ANGLE 500000 I MAXjLLOWED BEND ANGLE bull 135000 I BEND LENGTH ATIACHMENT PERCENT 100000 I MINjNGLE TO ADJACENT BEND PT 500000
LOOP CLOSURE TOLERANCE 254000mm
THERMAL BOWING HORZ TOLERANCE 100000E-04
AUTO NODE NUMBER INCREMENT 100000
ZJXIS UP NO
USE PRESSURE STIFFENING DEFAULT
ALPHA TOLERANCE 500000E-02
RESLDmiddotFORCE NO
HGR_DEF RESWGT STIF
bull 01751200E+12 Nlmm
DECOMP SNG TOL 01 OOOOOOE+ 11
BEND_AXIAL SHAPE NO
FRICT STIF 875600 Ni mm I FRICT NORM FORCE VAR 025000 I FRICT ANGLE VAR 300000 I FRICT SLIDE MULT 100000
ROD TOLERANCE 100000
ROD INC 200000
INCORE NUMERICAL CHECK NO
OUTCORE NUMERICAL CHECK NO
DEFAULT TRANS RESTRAINT STIFF 0175120E+12 Nlmm
DEFAULT ROT RESTRAINT STIFF 0112980E+12 Nmi deaJ
IGNORE SPRING HANGER STIFFNESS bull NO I
WI I middot AiHG bull _ KtVRCUE LOoO CAS ES_Odoc
rmiddot
bull
bull
Technip
KHARG ETHYLENE PLANT KHARG Olefin Complex
Setup File (
CONNECT_GEOMETRY _ THRU_CNODES
WRC-07 VERSION
WRC- 07
DEFAULT
831
WI I middot AIlaquo) Amiddot KHARGJUOAD CASFsOdoc
T
F
YES
NO
181 281
NO
DEFAULT
02206272E+OSbull
bullbull
bull
bull
Thchnip bull
KHARG ETHYLENE PLANT ~ KHARG Olefin Complex
PFffiOCHEMICAL INO bull DEVELOPMENT MANAG ~ENTCO_
CONTRACTOR DOCUMENT Ndeg OWNER DOCUMENT N
Proioct Ndeg Unit Doc TIIDEII Material Code Serial Ndeg Rev I Paae Proiect N Unit Doc Type Material Code Serial N A~ 7273F I 000 I WI I 1300 I 000 I a I 13 13 I 1313
FRP Ratio GmodlEmo(Uaxial) O2500000E+OO
FRP EalEhVhla O1527272E+OO
SetuD File (CAESARCFG Continuation)
FRP Lamina1e Type THREE
FRP Alpha O2159827E+02 C
FRP Density O1660800E+04 kocum bullEXCLUDE 12 FROM UKOOA BENDI NG NO
OUTPUT REPORTS BY LOAD CASE YES
DISPLACEMENT NODAL SORTING YES
DYNAMIC INPUT EXAMPLE TEXT MAX
TIME HIST ANIMATE YES
ENABLE AUTOSAVE YES
AUTOSAVE TIME INTERVAL O3000000E+02
PROMPTED AUTOSAVE YES
DISABLE UNDOREDO NO
STRUCTURAL DATABASE AISC89BIN
VALVE amp FLANGE GENERIC VHD
EXPANSION JT DBASE FLEXPATHJHD
PI PING SIZE SPECIFICATION ANSI
DEFAULT SPRING HANGER TABLE O5000000E+01
SYSTEM DIRECTORY NAME SYSTEM
UNITS FILE NAME 7273FFIL
ENABLE ODBC OUTPUT NO
DEFAULT SPRING HANGER TABLE LlSEGA
- bull -
WI 1 ANG bull IV IlHAAG_IELOAD CAS ES_OdOC
SRMPL6 LOf]) C(15euro5 S V REfK Ti O-l FOeC e- JlUE TO PSv oPttvlNG
bull Sldlle Aymmiddot [CIDO(UMpoundNTS AllD SETIINGSVhBACONI7173FmiddotMBACONICAESAR FILESICNj016_REV ~
bull
bull
bull
Edt
+ t
loadCose Edlcr LoadCoseOptiom Loads WlNeLoads
loads Oefned n IrtJIA loed Casu Stress Type
W -Woltllt L1 W+D1 +T1 +P1 +H Of 01 middot Displcmnt Case ~ L2 wO-iT2+P1 +H-- Of T1 middot Thermal Case tn l3 W~D1~T3~P1H ~(]S-oiit~~ Of LltgtOd e T2 Thermal Case 2 -- - _- ------- -__- T3 Thermal Case U3
l4 W+P1+H SUS __ _- -----PI middot Pr euUle Case 1 LS Wt-P1t-H-t-F1 OCC Hp middot Hydlo Prenae L6 Ul OCC --- ---- _----- H middot Hanger l oads 17 U2 OCC UI middot Unf Load eMe 11 La U3 OCC U2 -UriloodlAse 12 L9 F1 OCC U3 Uri l oad Case 13 L10 L1-l4 EXP F1 middot Cone FOIct Case 11 1 Ll1 L2-l4 J EXP Vlllet Fled W WNC middot W~ no corieris L12 L3-lS EXP
L13 LS+l7+l8 OCC L1 4 L-4+l13 ----l ~~ IL15 L1 lt-l1 3 L1 6 LJl9 (fD lO(ll ch 011 (f~tnlh OCC
STATIQUE LoR)) I- Ill
1
FW FRANCE NDG SHT16F I
CliENT
PROJECT
CPNo
EXXON
18KTA E5000 Expansion
CALCNo ISV 3310
CALC BY BEP
CHKD BY
DATE 13012006
RELIEF VALVE LOADINGS vapour
RV Nos ISV 3310
SIZE 4x3
RATING 150xlSO
ORIFICE L
bull DATA DESCRIPTION
RV SET PRESSURE
PERCENT OVERPRESSURE
Ps (l+PolOO) + 147
REliEF TEMPERATURE
1195492
RATIO OF SPECIFIC HEATS SIZING FLOW
SElECTED ORIFICE AREA
CALCULATED ORIFICE AREA
FACTORED SIZING flOW
MAX No OF WORKING VALVES
SIZING flOW PER VALVE
113600
MOLECULAR WEIGHT
GAS CONSTANT 1544M
SYMBOl UNITS
Ps BARG
Po
P PSIA T1 DegC
T Oeg R
k WI Kg h A sqin Ac sqin W2 Kgh N
W Ib h w Ibsec M
R ftlblb Oeg
bull GRAVITY IQ ftS2
FI=
2 W RI
gPA
VALUE
7 10 F2
12635 256
9528 105
- shyFl
t~ --+
~ middotFI FI
t5489 rTABIJSmn Ow COiiOmON
2853 NOn IIQRIZOllTAL IOItCIS Kt MtA CEil
2853 15489 F2
1 341532 +shy948701 F3
885 174463 ltV AT POICONllIll0N
322 AampUMING IMPACT CTOII OYl
260496 Ib 1159 N
128894 Ib 573 N
520993 Ib 2318 N -
bullbull
SARASIN-lltJ l7Technical amp Calculation Data Sheet ZI 8olto R~62IKI _____ J40 11ap11M GnlCMl
VAlVH e COlTllOlS Safety Valve
e Bomel lype Opened
Project KHARG OLEfiN COMPLEX ~A
Tag No PSV 6 453A C-Quote Ref 3A30880IOOO Sales Engineer Abdeljalill Baigar W de Commande
Operating ondl tlons Connect ons
19 InlelON shy1 fluid type Superheated Stetlm
20 Inlet Finish ANSt600 RF (125-250 AARH) 2 Capacity 78500 Kglh 21 Outlet DN J Set ptesSUe br eft 22 Outlet Finish ANSI 150 ftF 1125-250 AARH) Ol$charoe Tom p J7S C Accordinn 10 ASME 616-5
5 Variable bad pressure 0 bar eft
Cold (If lest lXess 47 bar eft 8111 of material 7 Overpressure 11 () 16 floltfv SA216 wee
SA2115WCC2 Ylt8 Operating Pressure 40 bar eft
SA216 wee Tight Closing pressUIe (MAOP) 423 bar eft 26 NoWe Stllited AlSl410 1~ 27 174 PH Stainless SteelMechanical Tomp J7S middotC ~ 28 Gaskets Stalnl St1
29 SPfinQ Chromium Allov Steel 30 AlSI431c31 Adusitina Rlna SA351 CF3M 32 Stud Al1lQrB7 JJ Alt4i1r2H Accessories
Regular Levr 35 51etUted nozzl
ReqUIred Area 31 927 om Test Gag 495 s q InIl Selected Area 41 2 om
I 839 sq in 15 Onfice p
Reaction loroe DN~ t Flow capacity 101299 Kglh 18 Noise at 30 m acc to APt521 120 dB
apprO)flTlate noise level at 30 m according to API521 (mouth noiso) )perl dlsctlarge
Customer Name TECHNIP FRANCE evlslon ~ lion ate
890 4 20-juin-2005
Cust Item Numb 7U3F RFQ 1545-01 a ely a ype pflllg a a ely alve ea1T
I I J7 Standard API 520 I )
Commercial code S46P3530AmiddotDmiddotVMM I shyI Dimensions
A- 2254 mm B- 2540 mm W - 11800 mrnIA 525PlKd~KnKb Kshl ~ Welghl() s 1523 Kg I A- 89 Inch I bullB- 100 Inch
Dati 01 calcul w - 4115 Inch Mass Capaatv W 18500 KgIh Weight( ) 3357 Pound
P1 5553 bar abs r~ C Gase Constant 143843
() Indicative Values 0 now ooeIficient Kd 0915 0
Ksn 0865 Remarks Napier equation correction Kn 1
~ 2 valves are necessary 10 reach the required capacity
Back pressure correcUon Kb 1a BUlHmiddotup back pressureO 1 berg Same calculallO1 heet lor the 1st va lve and the spare one bull
N
~
GENERAl
PEO
PROCESS
CONDITONS
bull DESIGN
DATA
bull MATERIALS
I
OPT IONS
1 T Nu~
2 Service 3 Line NUrMer 4 P amp to Numbef
5 6 Conform to 961231EC 7 Fluid T
8 NJ licable rED Table 9
0 11
12
13
14
15 16
17 19
20 21 22
PED Cal
Fluid Fluid Servlc Required Capaci
MoltcullWe hI
ratln PrtSi ur
tlll TIm tUri
Badlt Prl$IIure
AJlovtabie Ova sure
Ov esslI10 FactOI Com esslbU Latenl Heal 01 V lion
o Tl 1012812005 Pour Commenta ires
Equipment
Fluid Groo
Fluid S~I
5 cltle Gl1Ivl Set Pressure
Col
HC+H20
15489
5 02
ReHov Temperatlyene 212
Constant Varia1je Total
23 Specific Hnt RItIo lC 24 Relief Densi
25 Relief Viscosity
26 Barometric Pressure 27 28 Nozzle Flit Semi
29 Design Saely Reflef Sale -Relief 30 Type Conventional BelloIN Plot Opefatad 31 BonnetT 32 n Code
33 Sizing Basis 34 Calcula ted Area
35 Selected Area 36 Orifice De nation
37 Size Rating -Inlel 38 Size Rat - Outlet
39 40 41 42 43 Stt 44 Fla es
45 Resilient Seat Seal 46 Guide
471 Spfing 46 Wtted Material
49 50
Bonnt Disc
Ri s Bellows
51 Cap Screwed or Bolted 52 Lever Plain or Packed 53 TestGag
54 55
22-ISV 3310 0 331fD332 SHCOO20150A1A 1 l -Q2S)(l2
y Gaseous Group 1
0 1
0
09
105
4
Note 10
k
C
k p
Safety Corrventlonal
hI Solted
ASME Delaut eau de refroldissement
1812 em
L 3 150 RF 450 RF
A2 16 WCB
NOlet A216WCB
NOle 1
Note 1
NOIot
NOIel
(Note 1
No
No
INSTRUMENT SPECIFICATION
Valve Safety Pressure Relief
oxicFlammable
GasIVapo
7
2564 C
A21 6WCB SS 316 Mini
Note 1
EJflt0nMobil Chemic
Sheet 5middot11 of 46
f
No 8 Date Revision Code 2831 No C3 1052 Amiddot163 1middottVOl Rev 0
i (
II Technical amp Calculation Data Sheet SARASIN-Agt Zllloa-R~
Safety Valve Nt BiOPUIle Gt1wtI bull bull 2110 1-1_
IN I ICustomer Name TECHNIP FRANCE
891 I 4 I bull s~ I
Cuslllem Numb 7273F RFQ 1545-01
Project KHARG OLEFIN COMPLEX I Opened
I 1 I
Quote Ref Tag No PSV pound I Nde Sales Abdeljalill Baigar I
I I uperatIng onaltons
Fluid ~e Superheated Steam 19 tnle ON shy
capaci ty 78500 Kgn 20 Inlet Finish ANSI 600 RF (125-250 AARH)
3 Set presMKC 21 Outlet ON
4935 bar eM 22 OtItlet Finish ANSI 150 RF (125-250 AARH)
DiSCharge Temp 375 middotC ASME B16-5 5 Variable back presslJe bull bar eft
Cold dilf lesc press 4935 bar eft I Bill 01 I
OverptesslKe B() 10 Bod SAl16 wee a Operating ProsslKe bar elf 24 Yoke SA216 wee
25 cabull SA216 weebull bull Tlglt Closing presSlKe (MAOP) 44 415 bar eff 26 Nozzle Sellited AlSI410 bullMlaquohBnIcaI Temp J15 C 21 Disc 174 PH Stilinless Steel 28 Gaskets Stainless $t1 bullSDOM Chromium Alloy Steel 30 Golde AlSI431 31 AcluslthQRinP SAl51 CF3M 32 Stud A183flr81 33 Nul Al94gr2H
gt0 Revulr Lever
Reqllif~ Afea 32023 om 35 middot SlelUted noule
12 496 sq in TU I Gag
1 Sellcl(l(l AIel 41 2 om
I 839 sq in Orirooe p
I ReactIon loree 3016 D I Flow capacity 100996 KgIh
I Noise ill 30 m ace to AP152 1 126 dB approxmate noise level at 30 m aCCOfding to APl521 (mtluth noise) open discharge
II 37 j API52 I I I
Commercial code S46P3530A-D-VMM I
IA= 525 PlKd~Kn KbKsh I I~-middot 2254 mm 2540 mm
11800 mm
bull 1523 Kg
lA shy 89 InCh
Dab 01 COI lcul I ~ - 100 Inch
IH- 465 Inch -jshyMa55 Capaoty W 18500 KgIh 3351 Pound -IP I 553 barabs C C-ase Constant 341143 I () Indicative Values 0 now coeffiCIent Kd 09150
N Ksh 0866 w- Napier equation coffeclion Kn bull 2 valves afe necessary to reach the required capacity lt Back Pfessure correcllon Kb
BUIItmiddotup back pressurecO 1 barg 2nd Ialve set at 05 of set pranure with 10 olelpreSSure in accordill1Ce With API 520
bullbulliii
bull 11 Load cases Ioad case combinations
The following load cases f load case combinations shall be analyzed 1) always or 2) on a casemiddot to-case basis
Static load cases for operating design and pressure test conditions
L6 jillL7 I
I --shy
I --shyI I I I I
L L
I Ll 9 L20
bull ~--
Load types (iC a pplicable load types should be added) W Dead weight (pipe weight + fluid weight + insulation weight) D Displacement T Design temperature P Design internal pressure U Uniform loads (eg snow load seismic load) F External forces (forces andor moments) HP Hydro test pressure H Hanger loads WIN Wind loads (for the main wind directions) WNC Dead weight without contents (pipe weight + insulation weight) WW Water-filled weight for pressure test
bull bull bull
bull
bull ~-
9113
Technip
bull KHARG ETHYLENE PLANT
KHARG Olefin Complex
QVoINEA OClCUME NT N
P bull p N Unit Doc T Malerial Code Serial Ndeg Rw
913
142 Examples
Examplelr-~__~~-+~e~x~po=s~ed~to~W~ind=-~~h~~~r~o~st=a=t~~te=s~t~=s~ ~ po~rt~s-+pr=ing~s~u~p~line criteria Yes Yes Yes
bull Example File 002_01O-A_O_A (Unit 002 Calculation Number OlD Load Case File A evD)
CASE 1 W+Tl+PI+H (OPE) Operating cold condition
CASE 2 W+T2+P2+H (OPE) Operating hot conditions
CASE 3 W+PI +H (SUS) Deadweight + Pressure
CASE 4 WINl (SUS) Wind along X (Instead of OCC to avoid Snubber activation if I y)
CASES WIN2 (SUS) Wind along Z (Instead of OCC to avoid Snubber activation if y)
CASE 6 Ul (OCC) Seismic Lcentad X
CASE 7 U2 (OCe) Seismic Load Y
CASES U3 (OCC) Seismic Load Z
CASE9W+H (SUS) Deadweight + Spring hanger
CASE 10 PI (SUS) Pressure
CASE J 1 Tl (EXP) Temperarure
CASE 12 LI -L2 (EXP) thermal stress range Code Case
CASE 13 Ll -L3 (EXP) thermal suess range Code Case
CASE 14 LlI+Ll2 (EXP) full thermal stress range checking ABS combination
CASE 15 L6+L7+LS (OCC) Resultant seismic load SRSS combination CASE 16 ~9+L10+L1I+L3 (OCC) Sustained plus Wind X combined absolutely Code Ease CASE 17 L9+LI0+L11+L4 (OCC) Sustained plus Wind Z combined absolutely Code tase CASE 18 L9+L10+Lll+L15 (OCC) Sustained plus Seismic Combined absolutely Code ase
bull
bull
bull
bull
bull
Technip
KHARG ETHYLENE PLANT KHARG Olefin Complex
COHTAACTOR DOCUMENT N
-~
PEJROCHEMICAI IES DBVELOPMENT MANAG co
OWNER DOCUMENT Ndeg Unit Doe T P N
7273F 000 WI 1300 006 813 1 813 1
8 SNOW WAD (Ws)
I Emiddot~middotv O
Snow loads shall 00 applied only for cold outside lines for which design T is below 0 C and which are not protected by floor equ ipment or others
The hereafter calculated vaJue (Ws) will be classed as unifonn load foUowing Y axis (U ) in a separate Caesar input file See 7273F_OOO_CN3_CN2_1370_SAMPLlC AXLS
Design snow load 25 kgll1l2
The distribution of snow remaining on the horizontal pipe will take the shape hereu dec a reducljon factor of 072 may be applied
Ws = ( lx 051gt In x h 022D ) 25
Ws = (Ix 072 x D ) 25
Ws = 18 x D Kflrsi= 180 x D NIP Where 0 = outside diameter of pipe o r outside diameter of pipe + insulation if exist( m)
70middot
9120
o
bull Technip -D KHARG ETHYLENE PLANT ~
KHARG Olefin Complex
middot INmiddot I A~ I P~ UNo I 7273F 000 WI 1300 I 006 I A I 115 I 115
APPENDIX IV
L bull WIND PRESSURE I ELEVATION
11 Wind Basic nata I Wind pressure calcuJation
As per Project Basic Engineering 7273F-30-PP-206 Bask Design Data
Basic wind speed 160km h (44 5 m s)
Exposure Category 0
According to UBC 97 the design wind loading shall be
p= CxCxqX
where
P =Design wind pressure allevel 10 III
C~ =156 at leve1 10 m (EIIposure and gust factor-Table I6-G)
Cq I for DNlt= 50 nun
= 08 for DNgt 50 mm (Exposure and gust factor-Table I6-H)
qs= 1226 kNm2 ( Wind stagnation pressure at 10 m -Table J6-F)
lw = 1 15 (Importance factor - Table 16-K)
p = 220 xC (kNl m)
Height Above Wind pressure Ground Level
(m) PI eq (kNlm2 )
Oto 10 22
10 (0 20 247
20 to 30 264
30 10 40 276
40 to 50 286
50 to 60 289
60 to 70 293
70 1080 299
80 to 90 312
bull
bull
bull
bull
CONTRACTOR OOCUIENT bull N UniI Doc T Milttl CoOl srI N Rev Pa p
7273F 000 WI 1300 000 0 ()J 13
2 CONFIGURATION FILES USING CAESAR II
21 Unit System (7273FFIL)
CAE S A R liVERS 430
INPUT UNITS USED
UNITS 7273F NOMISCH INPUT ON
LENGTH inches
FORCE pounds
MASS(dynamics) pounds
MOMENTS(INPUn inch-pounds
MOMENTS(OUTPUT) inch-pounds
STRESS Ibssqin
TEMP SCALE degrees F
PRESSURE psig
ELASTIC MODULUS Ibslsqin
PI PE DENSITY Ibslcuin
INSULATION DENS Ibslcuin
FLUID DENSITY Ibslcuin
TRANSL STI F Ibslin
ROTATIONAL STiF inlbldeg
UNIFORM LOAD Jblin
GLOAD gs
WIND LOAD IbsJsqin
ELEVATION inches
COMPOUND LENGTH inches
DIAMETER inches
WALL THICKNESS inches
OWNER DOCUMENT Ndeg
~ Doc T Malerial CoOa Serial Ndeg Rev
1013
x 25400 mm
x 4448 N
x 0454 kg
x 0113 Nm
x 0113 Nm
x 0007 MPa
x 0556 C
x 0069 bars
x 0007 MPa
x 27680000 kgCrmiddotm
x 27680000 kgJcum
x 27680000 kgci m
x 0175 Nm
x 0113
l x 175127 NJm
x 1000 gs
x 6894757 NJ m
x 0025 m
x 25400 mm
x 1000 inch
x 25400 mm
bull bull
Technip
KHARG ETHYLENE PLANT KHARG Olefin Complex
PETROCHlMlCAL IND JES DIiVElOPMENT MANGEMENT CO
11113
Technip bull
KHARG ETHYLENE PLANT ~ KHARG Olefin Complex
iETltOCHEMICtl OEVEIOPMENT MANArCO
CONTRACTOR DOCUMENT N OWNER DOCUMENT Nmiddot ProIecl N p U Doe TwalMrolerial Code ISen N ReI P_ Proiect N I UNt Doo T~ I ~eriIII Code
7273F 000 WI I 1300 I 000 I 0 I 11113 I I I
22 Setup File ( CAESARCFG )
C A E SAR II VERS450
SETUP FILE PARAMETERS
CONNECT GEOMETRY THRU CNODES YES I MIN ALLOWED BEND ANGLE 500000 I MAXjLLOWED BEND ANGLE bull 135000 I BEND LENGTH ATIACHMENT PERCENT 100000 I MINjNGLE TO ADJACENT BEND PT 500000
LOOP CLOSURE TOLERANCE 254000mm
THERMAL BOWING HORZ TOLERANCE 100000E-04
AUTO NODE NUMBER INCREMENT 100000
ZJXIS UP NO
USE PRESSURE STIFFENING DEFAULT
ALPHA TOLERANCE 500000E-02
RESLDmiddotFORCE NO
HGR_DEF RESWGT STIF
bull 01751200E+12 Nlmm
DECOMP SNG TOL 01 OOOOOOE+ 11
BEND_AXIAL SHAPE NO
FRICT STIF 875600 Ni mm I FRICT NORM FORCE VAR 025000 I FRICT ANGLE VAR 300000 I FRICT SLIDE MULT 100000
ROD TOLERANCE 100000
ROD INC 200000
INCORE NUMERICAL CHECK NO
OUTCORE NUMERICAL CHECK NO
DEFAULT TRANS RESTRAINT STIFF 0175120E+12 Nlmm
DEFAULT ROT RESTRAINT STIFF 0112980E+12 Nmi deaJ
IGNORE SPRING HANGER STIFFNESS bull NO I
WI I middot AiHG bull _ KtVRCUE LOoO CAS ES_Odoc
rmiddot
bull
bull
Technip
KHARG ETHYLENE PLANT KHARG Olefin Complex
Setup File (
CONNECT_GEOMETRY _ THRU_CNODES
WRC-07 VERSION
WRC- 07
DEFAULT
831
WI I middot AIlaquo) Amiddot KHARGJUOAD CASFsOdoc
T
F
YES
NO
181 281
NO
DEFAULT
02206272E+OSbull
bullbull
bull
bull
Thchnip bull
KHARG ETHYLENE PLANT ~ KHARG Olefin Complex
PFffiOCHEMICAL INO bull DEVELOPMENT MANAG ~ENTCO_
CONTRACTOR DOCUMENT Ndeg OWNER DOCUMENT N
Proioct Ndeg Unit Doc TIIDEII Material Code Serial Ndeg Rev I Paae Proiect N Unit Doc Type Material Code Serial N A~ 7273F I 000 I WI I 1300 I 000 I a I 13 13 I 1313
FRP Ratio GmodlEmo(Uaxial) O2500000E+OO
FRP EalEhVhla O1527272E+OO
SetuD File (CAESARCFG Continuation)
FRP Lamina1e Type THREE
FRP Alpha O2159827E+02 C
FRP Density O1660800E+04 kocum bullEXCLUDE 12 FROM UKOOA BENDI NG NO
OUTPUT REPORTS BY LOAD CASE YES
DISPLACEMENT NODAL SORTING YES
DYNAMIC INPUT EXAMPLE TEXT MAX
TIME HIST ANIMATE YES
ENABLE AUTOSAVE YES
AUTOSAVE TIME INTERVAL O3000000E+02
PROMPTED AUTOSAVE YES
DISABLE UNDOREDO NO
STRUCTURAL DATABASE AISC89BIN
VALVE amp FLANGE GENERIC VHD
EXPANSION JT DBASE FLEXPATHJHD
PI PING SIZE SPECIFICATION ANSI
DEFAULT SPRING HANGER TABLE O5000000E+01
SYSTEM DIRECTORY NAME SYSTEM
UNITS FILE NAME 7273FFIL
ENABLE ODBC OUTPUT NO
DEFAULT SPRING HANGER TABLE LlSEGA
- bull -
WI 1 ANG bull IV IlHAAG_IELOAD CAS ES_OdOC
SRMPL6 LOf]) C(15euro5 S V REfK Ti O-l FOeC e- JlUE TO PSv oPttvlNG
bull Sldlle Aymmiddot [CIDO(UMpoundNTS AllD SETIINGSVhBACONI7173FmiddotMBACONICAESAR FILESICNj016_REV ~
bull
bull
bull
Edt
+ t
loadCose Edlcr LoadCoseOptiom Loads WlNeLoads
loads Oefned n IrtJIA loed Casu Stress Type
W -Woltllt L1 W+D1 +T1 +P1 +H Of 01 middot Displcmnt Case ~ L2 wO-iT2+P1 +H-- Of T1 middot Thermal Case tn l3 W~D1~T3~P1H ~(]S-oiit~~ Of LltgtOd e T2 Thermal Case 2 -- - _- ------- -__- T3 Thermal Case U3
l4 W+P1+H SUS __ _- -----PI middot Pr euUle Case 1 LS Wt-P1t-H-t-F1 OCC Hp middot Hydlo Prenae L6 Ul OCC --- ---- _----- H middot Hanger l oads 17 U2 OCC UI middot Unf Load eMe 11 La U3 OCC U2 -UriloodlAse 12 L9 F1 OCC U3 Uri l oad Case 13 L10 L1-l4 EXP F1 middot Cone FOIct Case 11 1 Ll1 L2-l4 J EXP Vlllet Fled W WNC middot W~ no corieris L12 L3-lS EXP
L13 LS+l7+l8 OCC L1 4 L-4+l13 ----l ~~ IL15 L1 lt-l1 3 L1 6 LJl9 (fD lO(ll ch 011 (f~tnlh OCC
STATIQUE LoR)) I- Ill
1
FW FRANCE NDG SHT16F I
CliENT
PROJECT
CPNo
EXXON
18KTA E5000 Expansion
CALCNo ISV 3310
CALC BY BEP
CHKD BY
DATE 13012006
RELIEF VALVE LOADINGS vapour
RV Nos ISV 3310
SIZE 4x3
RATING 150xlSO
ORIFICE L
bull DATA DESCRIPTION
RV SET PRESSURE
PERCENT OVERPRESSURE
Ps (l+PolOO) + 147
REliEF TEMPERATURE
1195492
RATIO OF SPECIFIC HEATS SIZING FLOW
SElECTED ORIFICE AREA
CALCULATED ORIFICE AREA
FACTORED SIZING flOW
MAX No OF WORKING VALVES
SIZING flOW PER VALVE
113600
MOLECULAR WEIGHT
GAS CONSTANT 1544M
SYMBOl UNITS
Ps BARG
Po
P PSIA T1 DegC
T Oeg R
k WI Kg h A sqin Ac sqin W2 Kgh N
W Ib h w Ibsec M
R ftlblb Oeg
bull GRAVITY IQ ftS2
FI=
2 W RI
gPA
VALUE
7 10 F2
12635 256
9528 105
- shyFl
t~ --+
~ middotFI FI
t5489 rTABIJSmn Ow COiiOmON
2853 NOn IIQRIZOllTAL IOItCIS Kt MtA CEil
2853 15489 F2
1 341532 +shy948701 F3
885 174463 ltV AT POICONllIll0N
322 AampUMING IMPACT CTOII OYl
260496 Ib 1159 N
128894 Ib 573 N
520993 Ib 2318 N -
bullbull
SARASIN-lltJ l7Technical amp Calculation Data Sheet ZI 8olto R~62IKI _____ J40 11ap11M GnlCMl
VAlVH e COlTllOlS Safety Valve
e Bomel lype Opened
Project KHARG OLEfiN COMPLEX ~A
Tag No PSV 6 453A C-Quote Ref 3A30880IOOO Sales Engineer Abdeljalill Baigar W de Commande
Operating ondl tlons Connect ons
19 InlelON shy1 fluid type Superheated Stetlm
20 Inlet Finish ANSt600 RF (125-250 AARH) 2 Capacity 78500 Kglh 21 Outlet DN J Set ptesSUe br eft 22 Outlet Finish ANSI 150 ftF 1125-250 AARH) Ol$charoe Tom p J7S C Accordinn 10 ASME 616-5
5 Variable bad pressure 0 bar eft
Cold (If lest lXess 47 bar eft 8111 of material 7 Overpressure 11 () 16 floltfv SA216 wee
SA2115WCC2 Ylt8 Operating Pressure 40 bar eft
SA216 wee Tight Closing pressUIe (MAOP) 423 bar eft 26 NoWe Stllited AlSl410 1~ 27 174 PH Stainless SteelMechanical Tomp J7S middotC ~ 28 Gaskets Stalnl St1
29 SPfinQ Chromium Allov Steel 30 AlSI431c31 Adusitina Rlna SA351 CF3M 32 Stud Al1lQrB7 JJ Alt4i1r2H Accessories
Regular Levr 35 51etUted nozzl
ReqUIred Area 31 927 om Test Gag 495 s q InIl Selected Area 41 2 om
I 839 sq in 15 Onfice p
Reaction loroe DN~ t Flow capacity 101299 Kglh 18 Noise at 30 m acc to APt521 120 dB
apprO)flTlate noise level at 30 m according to API521 (mouth noiso) )perl dlsctlarge
Customer Name TECHNIP FRANCE evlslon ~ lion ate
890 4 20-juin-2005
Cust Item Numb 7U3F RFQ 1545-01 a ely a ype pflllg a a ely alve ea1T
I I J7 Standard API 520 I )
Commercial code S46P3530AmiddotDmiddotVMM I shyI Dimensions
A- 2254 mm B- 2540 mm W - 11800 mrnIA 525PlKd~KnKb Kshl ~ Welghl() s 1523 Kg I A- 89 Inch I bullB- 100 Inch
Dati 01 calcul w - 4115 Inch Mass Capaatv W 18500 KgIh Weight( ) 3357 Pound
P1 5553 bar abs r~ C Gase Constant 143843
() Indicative Values 0 now ooeIficient Kd 0915 0
Ksn 0865 Remarks Napier equation correction Kn 1
~ 2 valves are necessary 10 reach the required capacity
Back pressure correcUon Kb 1a BUlHmiddotup back pressureO 1 berg Same calculallO1 heet lor the 1st va lve and the spare one bull
N
~
GENERAl
PEO
PROCESS
CONDITONS
bull DESIGN
DATA
bull MATERIALS
I
OPT IONS
1 T Nu~
2 Service 3 Line NUrMer 4 P amp to Numbef
5 6 Conform to 961231EC 7 Fluid T
8 NJ licable rED Table 9
0 11
12
13
14
15 16
17 19
20 21 22
PED Cal
Fluid Fluid Servlc Required Capaci
MoltcullWe hI
ratln PrtSi ur
tlll TIm tUri
Badlt Prl$IIure
AJlovtabie Ova sure
Ov esslI10 FactOI Com esslbU Latenl Heal 01 V lion
o Tl 1012812005 Pour Commenta ires
Equipment
Fluid Groo
Fluid S~I
5 cltle Gl1Ivl Set Pressure
Col
HC+H20
15489
5 02
ReHov Temperatlyene 212
Constant Varia1je Total
23 Specific Hnt RItIo lC 24 Relief Densi
25 Relief Viscosity
26 Barometric Pressure 27 28 Nozzle Flit Semi
29 Design Saely Reflef Sale -Relief 30 Type Conventional BelloIN Plot Opefatad 31 BonnetT 32 n Code
33 Sizing Basis 34 Calcula ted Area
35 Selected Area 36 Orifice De nation
37 Size Rating -Inlel 38 Size Rat - Outlet
39 40 41 42 43 Stt 44 Fla es
45 Resilient Seat Seal 46 Guide
471 Spfing 46 Wtted Material
49 50
Bonnt Disc
Ri s Bellows
51 Cap Screwed or Bolted 52 Lever Plain or Packed 53 TestGag
54 55
22-ISV 3310 0 331fD332 SHCOO20150A1A 1 l -Q2S)(l2
y Gaseous Group 1
0 1
0
09
105
4
Note 10
k
C
k p
Safety Corrventlonal
hI Solted
ASME Delaut eau de refroldissement
1812 em
L 3 150 RF 450 RF
A2 16 WCB
NOlet A216WCB
NOle 1
Note 1
NOIot
NOIel
(Note 1
No
No
INSTRUMENT SPECIFICATION
Valve Safety Pressure Relief
oxicFlammable
GasIVapo
7
2564 C
A21 6WCB SS 316 Mini
Note 1
EJflt0nMobil Chemic
Sheet 5middot11 of 46
f
No 8 Date Revision Code 2831 No C3 1052 Amiddot163 1middottVOl Rev 0
i (
II Technical amp Calculation Data Sheet SARASIN-Agt Zllloa-R~
Safety Valve Nt BiOPUIle Gt1wtI bull bull 2110 1-1_
IN I ICustomer Name TECHNIP FRANCE
891 I 4 I bull s~ I
Cuslllem Numb 7273F RFQ 1545-01
Project KHARG OLEFIN COMPLEX I Opened
I 1 I
Quote Ref Tag No PSV pound I Nde Sales Abdeljalill Baigar I
I I uperatIng onaltons
Fluid ~e Superheated Steam 19 tnle ON shy
capaci ty 78500 Kgn 20 Inlet Finish ANSI 600 RF (125-250 AARH)
3 Set presMKC 21 Outlet ON
4935 bar eM 22 OtItlet Finish ANSI 150 RF (125-250 AARH)
DiSCharge Temp 375 middotC ASME B16-5 5 Variable back presslJe bull bar eft
Cold dilf lesc press 4935 bar eft I Bill 01 I
OverptesslKe B() 10 Bod SAl16 wee a Operating ProsslKe bar elf 24 Yoke SA216 wee
25 cabull SA216 weebull bull Tlglt Closing presSlKe (MAOP) 44 415 bar eff 26 Nozzle Sellited AlSI410 bullMlaquohBnIcaI Temp J15 C 21 Disc 174 PH Stilinless Steel 28 Gaskets Stainless $t1 bullSDOM Chromium Alloy Steel 30 Golde AlSI431 31 AcluslthQRinP SAl51 CF3M 32 Stud A183flr81 33 Nul Al94gr2H
gt0 Revulr Lever
Reqllif~ Afea 32023 om 35 middot SlelUted noule
12 496 sq in TU I Gag
1 Sellcl(l(l AIel 41 2 om
I 839 sq in Orirooe p
I ReactIon loree 3016 D I Flow capacity 100996 KgIh
I Noise ill 30 m ace to AP152 1 126 dB approxmate noise level at 30 m aCCOfding to APl521 (mtluth noise) open discharge
II 37 j API52 I I I
Commercial code S46P3530A-D-VMM I
IA= 525 PlKd~Kn KbKsh I I~-middot 2254 mm 2540 mm
11800 mm
bull 1523 Kg
lA shy 89 InCh
Dab 01 COI lcul I ~ - 100 Inch
IH- 465 Inch -jshyMa55 Capaoty W 18500 KgIh 3351 Pound -IP I 553 barabs C C-ase Constant 341143 I () Indicative Values 0 now coeffiCIent Kd 09150
N Ksh 0866 w- Napier equation coffeclion Kn bull 2 valves afe necessary to reach the required capacity lt Back Pfessure correcllon Kb
BUIItmiddotup back pressurecO 1 barg 2nd Ialve set at 05 of set pranure with 10 olelpreSSure in accordill1Ce With API 520
bullbulliii
bull 11 Load cases Ioad case combinations
The following load cases f load case combinations shall be analyzed 1) always or 2) on a casemiddot to-case basis
Static load cases for operating design and pressure test conditions
L6 jillL7 I
I --shy
I --shyI I I I I
L L
I Ll 9 L20
bull ~--
Load types (iC a pplicable load types should be added) W Dead weight (pipe weight + fluid weight + insulation weight) D Displacement T Design temperature P Design internal pressure U Uniform loads (eg snow load seismic load) F External forces (forces andor moments) HP Hydro test pressure H Hanger loads WIN Wind loads (for the main wind directions) WNC Dead weight without contents (pipe weight + insulation weight) WW Water-filled weight for pressure test
bull bull bull
bull
bull ~-
bull
bull
bull
bull
Technip
KHARG ETHYLENE PLANT KHARG Olefin Complex
COHTAACTOR DOCUMENT N
-~
PEJROCHEMICAI IES DBVELOPMENT MANAG co
OWNER DOCUMENT Ndeg Unit Doe T P N
7273F 000 WI 1300 006 813 1 813 1
8 SNOW WAD (Ws)
I Emiddot~middotv O
Snow loads shall 00 applied only for cold outside lines for which design T is below 0 C and which are not protected by floor equ ipment or others
The hereafter calculated vaJue (Ws) will be classed as unifonn load foUowing Y axis (U ) in a separate Caesar input file See 7273F_OOO_CN3_CN2_1370_SAMPLlC AXLS
Design snow load 25 kgll1l2
The distribution of snow remaining on the horizontal pipe will take the shape hereu dec a reducljon factor of 072 may be applied
Ws = ( lx 051gt In x h 022D ) 25
Ws = (Ix 072 x D ) 25
Ws = 18 x D Kflrsi= 180 x D NIP Where 0 = outside diameter of pipe o r outside diameter of pipe + insulation if exist( m)
70middot
9120
o
bull Technip -D KHARG ETHYLENE PLANT ~
KHARG Olefin Complex
middot INmiddot I A~ I P~ UNo I 7273F 000 WI 1300 I 006 I A I 115 I 115
APPENDIX IV
L bull WIND PRESSURE I ELEVATION
11 Wind Basic nata I Wind pressure calcuJation
As per Project Basic Engineering 7273F-30-PP-206 Bask Design Data
Basic wind speed 160km h (44 5 m s)
Exposure Category 0
According to UBC 97 the design wind loading shall be
p= CxCxqX
where
P =Design wind pressure allevel 10 III
C~ =156 at leve1 10 m (EIIposure and gust factor-Table I6-G)
Cq I for DNlt= 50 nun
= 08 for DNgt 50 mm (Exposure and gust factor-Table I6-H)
qs= 1226 kNm2 ( Wind stagnation pressure at 10 m -Table J6-F)
lw = 1 15 (Importance factor - Table 16-K)
p = 220 xC (kNl m)
Height Above Wind pressure Ground Level
(m) PI eq (kNlm2 )
Oto 10 22
10 (0 20 247
20 to 30 264
30 10 40 276
40 to 50 286
50 to 60 289
60 to 70 293
70 1080 299
80 to 90 312
bull
bull
bull
bull
CONTRACTOR OOCUIENT bull N UniI Doc T Milttl CoOl srI N Rev Pa p
7273F 000 WI 1300 000 0 ()J 13
2 CONFIGURATION FILES USING CAESAR II
21 Unit System (7273FFIL)
CAE S A R liVERS 430
INPUT UNITS USED
UNITS 7273F NOMISCH INPUT ON
LENGTH inches
FORCE pounds
MASS(dynamics) pounds
MOMENTS(INPUn inch-pounds
MOMENTS(OUTPUT) inch-pounds
STRESS Ibssqin
TEMP SCALE degrees F
PRESSURE psig
ELASTIC MODULUS Ibslsqin
PI PE DENSITY Ibslcuin
INSULATION DENS Ibslcuin
FLUID DENSITY Ibslcuin
TRANSL STI F Ibslin
ROTATIONAL STiF inlbldeg
UNIFORM LOAD Jblin
GLOAD gs
WIND LOAD IbsJsqin
ELEVATION inches
COMPOUND LENGTH inches
DIAMETER inches
WALL THICKNESS inches
OWNER DOCUMENT Ndeg
~ Doc T Malerial CoOa Serial Ndeg Rev
1013
x 25400 mm
x 4448 N
x 0454 kg
x 0113 Nm
x 0113 Nm
x 0007 MPa
x 0556 C
x 0069 bars
x 0007 MPa
x 27680000 kgCrmiddotm
x 27680000 kgJcum
x 27680000 kgci m
x 0175 Nm
x 0113
l x 175127 NJm
x 1000 gs
x 6894757 NJ m
x 0025 m
x 25400 mm
x 1000 inch
x 25400 mm
bull bull
Technip
KHARG ETHYLENE PLANT KHARG Olefin Complex
PETROCHlMlCAL IND JES DIiVElOPMENT MANGEMENT CO
11113
Technip bull
KHARG ETHYLENE PLANT ~ KHARG Olefin Complex
iETltOCHEMICtl OEVEIOPMENT MANArCO
CONTRACTOR DOCUMENT N OWNER DOCUMENT Nmiddot ProIecl N p U Doe TwalMrolerial Code ISen N ReI P_ Proiect N I UNt Doo T~ I ~eriIII Code
7273F 000 WI I 1300 I 000 I 0 I 11113 I I I
22 Setup File ( CAESARCFG )
C A E SAR II VERS450
SETUP FILE PARAMETERS
CONNECT GEOMETRY THRU CNODES YES I MIN ALLOWED BEND ANGLE 500000 I MAXjLLOWED BEND ANGLE bull 135000 I BEND LENGTH ATIACHMENT PERCENT 100000 I MINjNGLE TO ADJACENT BEND PT 500000
LOOP CLOSURE TOLERANCE 254000mm
THERMAL BOWING HORZ TOLERANCE 100000E-04
AUTO NODE NUMBER INCREMENT 100000
ZJXIS UP NO
USE PRESSURE STIFFENING DEFAULT
ALPHA TOLERANCE 500000E-02
RESLDmiddotFORCE NO
HGR_DEF RESWGT STIF
bull 01751200E+12 Nlmm
DECOMP SNG TOL 01 OOOOOOE+ 11
BEND_AXIAL SHAPE NO
FRICT STIF 875600 Ni mm I FRICT NORM FORCE VAR 025000 I FRICT ANGLE VAR 300000 I FRICT SLIDE MULT 100000
ROD TOLERANCE 100000
ROD INC 200000
INCORE NUMERICAL CHECK NO
OUTCORE NUMERICAL CHECK NO
DEFAULT TRANS RESTRAINT STIFF 0175120E+12 Nlmm
DEFAULT ROT RESTRAINT STIFF 0112980E+12 Nmi deaJ
IGNORE SPRING HANGER STIFFNESS bull NO I
WI I middot AiHG bull _ KtVRCUE LOoO CAS ES_Odoc
rmiddot
bull
bull
Technip
KHARG ETHYLENE PLANT KHARG Olefin Complex
Setup File (
CONNECT_GEOMETRY _ THRU_CNODES
WRC-07 VERSION
WRC- 07
DEFAULT
831
WI I middot AIlaquo) Amiddot KHARGJUOAD CASFsOdoc
T
F
YES
NO
181 281
NO
DEFAULT
02206272E+OSbull
bullbull
bull
bull
Thchnip bull
KHARG ETHYLENE PLANT ~ KHARG Olefin Complex
PFffiOCHEMICAL INO bull DEVELOPMENT MANAG ~ENTCO_
CONTRACTOR DOCUMENT Ndeg OWNER DOCUMENT N
Proioct Ndeg Unit Doc TIIDEII Material Code Serial Ndeg Rev I Paae Proiect N Unit Doc Type Material Code Serial N A~ 7273F I 000 I WI I 1300 I 000 I a I 13 13 I 1313
FRP Ratio GmodlEmo(Uaxial) O2500000E+OO
FRP EalEhVhla O1527272E+OO
SetuD File (CAESARCFG Continuation)
FRP Lamina1e Type THREE
FRP Alpha O2159827E+02 C
FRP Density O1660800E+04 kocum bullEXCLUDE 12 FROM UKOOA BENDI NG NO
OUTPUT REPORTS BY LOAD CASE YES
DISPLACEMENT NODAL SORTING YES
DYNAMIC INPUT EXAMPLE TEXT MAX
TIME HIST ANIMATE YES
ENABLE AUTOSAVE YES
AUTOSAVE TIME INTERVAL O3000000E+02
PROMPTED AUTOSAVE YES
DISABLE UNDOREDO NO
STRUCTURAL DATABASE AISC89BIN
VALVE amp FLANGE GENERIC VHD
EXPANSION JT DBASE FLEXPATHJHD
PI PING SIZE SPECIFICATION ANSI
DEFAULT SPRING HANGER TABLE O5000000E+01
SYSTEM DIRECTORY NAME SYSTEM
UNITS FILE NAME 7273FFIL
ENABLE ODBC OUTPUT NO
DEFAULT SPRING HANGER TABLE LlSEGA
- bull -
WI 1 ANG bull IV IlHAAG_IELOAD CAS ES_OdOC
SRMPL6 LOf]) C(15euro5 S V REfK Ti O-l FOeC e- JlUE TO PSv oPttvlNG
bull Sldlle Aymmiddot [CIDO(UMpoundNTS AllD SETIINGSVhBACONI7173FmiddotMBACONICAESAR FILESICNj016_REV ~
bull
bull
bull
Edt
+ t
loadCose Edlcr LoadCoseOptiom Loads WlNeLoads
loads Oefned n IrtJIA loed Casu Stress Type
W -Woltllt L1 W+D1 +T1 +P1 +H Of 01 middot Displcmnt Case ~ L2 wO-iT2+P1 +H-- Of T1 middot Thermal Case tn l3 W~D1~T3~P1H ~(]S-oiit~~ Of LltgtOd e T2 Thermal Case 2 -- - _- ------- -__- T3 Thermal Case U3
l4 W+P1+H SUS __ _- -----PI middot Pr euUle Case 1 LS Wt-P1t-H-t-F1 OCC Hp middot Hydlo Prenae L6 Ul OCC --- ---- _----- H middot Hanger l oads 17 U2 OCC UI middot Unf Load eMe 11 La U3 OCC U2 -UriloodlAse 12 L9 F1 OCC U3 Uri l oad Case 13 L10 L1-l4 EXP F1 middot Cone FOIct Case 11 1 Ll1 L2-l4 J EXP Vlllet Fled W WNC middot W~ no corieris L12 L3-lS EXP
L13 LS+l7+l8 OCC L1 4 L-4+l13 ----l ~~ IL15 L1 lt-l1 3 L1 6 LJl9 (fD lO(ll ch 011 (f~tnlh OCC
STATIQUE LoR)) I- Ill
1
FW FRANCE NDG SHT16F I
CliENT
PROJECT
CPNo
EXXON
18KTA E5000 Expansion
CALCNo ISV 3310
CALC BY BEP
CHKD BY
DATE 13012006
RELIEF VALVE LOADINGS vapour
RV Nos ISV 3310
SIZE 4x3
RATING 150xlSO
ORIFICE L
bull DATA DESCRIPTION
RV SET PRESSURE
PERCENT OVERPRESSURE
Ps (l+PolOO) + 147
REliEF TEMPERATURE
1195492
RATIO OF SPECIFIC HEATS SIZING FLOW
SElECTED ORIFICE AREA
CALCULATED ORIFICE AREA
FACTORED SIZING flOW
MAX No OF WORKING VALVES
SIZING flOW PER VALVE
113600
MOLECULAR WEIGHT
GAS CONSTANT 1544M
SYMBOl UNITS
Ps BARG
Po
P PSIA T1 DegC
T Oeg R
k WI Kg h A sqin Ac sqin W2 Kgh N
W Ib h w Ibsec M
R ftlblb Oeg
bull GRAVITY IQ ftS2
FI=
2 W RI
gPA
VALUE
7 10 F2
12635 256
9528 105
- shyFl
t~ --+
~ middotFI FI
t5489 rTABIJSmn Ow COiiOmON
2853 NOn IIQRIZOllTAL IOItCIS Kt MtA CEil
2853 15489 F2
1 341532 +shy948701 F3
885 174463 ltV AT POICONllIll0N
322 AampUMING IMPACT CTOII OYl
260496 Ib 1159 N
128894 Ib 573 N
520993 Ib 2318 N -
bullbull
SARASIN-lltJ l7Technical amp Calculation Data Sheet ZI 8olto R~62IKI _____ J40 11ap11M GnlCMl
VAlVH e COlTllOlS Safety Valve
e Bomel lype Opened
Project KHARG OLEfiN COMPLEX ~A
Tag No PSV 6 453A C-Quote Ref 3A30880IOOO Sales Engineer Abdeljalill Baigar W de Commande
Operating ondl tlons Connect ons
19 InlelON shy1 fluid type Superheated Stetlm
20 Inlet Finish ANSt600 RF (125-250 AARH) 2 Capacity 78500 Kglh 21 Outlet DN J Set ptesSUe br eft 22 Outlet Finish ANSI 150 ftF 1125-250 AARH) Ol$charoe Tom p J7S C Accordinn 10 ASME 616-5
5 Variable bad pressure 0 bar eft
Cold (If lest lXess 47 bar eft 8111 of material 7 Overpressure 11 () 16 floltfv SA216 wee
SA2115WCC2 Ylt8 Operating Pressure 40 bar eft
SA216 wee Tight Closing pressUIe (MAOP) 423 bar eft 26 NoWe Stllited AlSl410 1~ 27 174 PH Stainless SteelMechanical Tomp J7S middotC ~ 28 Gaskets Stalnl St1
29 SPfinQ Chromium Allov Steel 30 AlSI431c31 Adusitina Rlna SA351 CF3M 32 Stud Al1lQrB7 JJ Alt4i1r2H Accessories
Regular Levr 35 51etUted nozzl
ReqUIred Area 31 927 om Test Gag 495 s q InIl Selected Area 41 2 om
I 839 sq in 15 Onfice p
Reaction loroe DN~ t Flow capacity 101299 Kglh 18 Noise at 30 m acc to APt521 120 dB
apprO)flTlate noise level at 30 m according to API521 (mouth noiso) )perl dlsctlarge
Customer Name TECHNIP FRANCE evlslon ~ lion ate
890 4 20-juin-2005
Cust Item Numb 7U3F RFQ 1545-01 a ely a ype pflllg a a ely alve ea1T
I I J7 Standard API 520 I )
Commercial code S46P3530AmiddotDmiddotVMM I shyI Dimensions
A- 2254 mm B- 2540 mm W - 11800 mrnIA 525PlKd~KnKb Kshl ~ Welghl() s 1523 Kg I A- 89 Inch I bullB- 100 Inch
Dati 01 calcul w - 4115 Inch Mass Capaatv W 18500 KgIh Weight( ) 3357 Pound
P1 5553 bar abs r~ C Gase Constant 143843
() Indicative Values 0 now ooeIficient Kd 0915 0
Ksn 0865 Remarks Napier equation correction Kn 1
~ 2 valves are necessary 10 reach the required capacity
Back pressure correcUon Kb 1a BUlHmiddotup back pressureO 1 berg Same calculallO1 heet lor the 1st va lve and the spare one bull
N
~
GENERAl
PEO
PROCESS
CONDITONS
bull DESIGN
DATA
bull MATERIALS
I
OPT IONS
1 T Nu~
2 Service 3 Line NUrMer 4 P amp to Numbef
5 6 Conform to 961231EC 7 Fluid T
8 NJ licable rED Table 9
0 11
12
13
14
15 16
17 19
20 21 22
PED Cal
Fluid Fluid Servlc Required Capaci
MoltcullWe hI
ratln PrtSi ur
tlll TIm tUri
Badlt Prl$IIure
AJlovtabie Ova sure
Ov esslI10 FactOI Com esslbU Latenl Heal 01 V lion
o Tl 1012812005 Pour Commenta ires
Equipment
Fluid Groo
Fluid S~I
5 cltle Gl1Ivl Set Pressure
Col
HC+H20
15489
5 02
ReHov Temperatlyene 212
Constant Varia1je Total
23 Specific Hnt RItIo lC 24 Relief Densi
25 Relief Viscosity
26 Barometric Pressure 27 28 Nozzle Flit Semi
29 Design Saely Reflef Sale -Relief 30 Type Conventional BelloIN Plot Opefatad 31 BonnetT 32 n Code
33 Sizing Basis 34 Calcula ted Area
35 Selected Area 36 Orifice De nation
37 Size Rating -Inlel 38 Size Rat - Outlet
39 40 41 42 43 Stt 44 Fla es
45 Resilient Seat Seal 46 Guide
471 Spfing 46 Wtted Material
49 50
Bonnt Disc
Ri s Bellows
51 Cap Screwed or Bolted 52 Lever Plain or Packed 53 TestGag
54 55
22-ISV 3310 0 331fD332 SHCOO20150A1A 1 l -Q2S)(l2
y Gaseous Group 1
0 1
0
09
105
4
Note 10
k
C
k p
Safety Corrventlonal
hI Solted
ASME Delaut eau de refroldissement
1812 em
L 3 150 RF 450 RF
A2 16 WCB
NOlet A216WCB
NOle 1
Note 1
NOIot
NOIel
(Note 1
No
No
INSTRUMENT SPECIFICATION
Valve Safety Pressure Relief
oxicFlammable
GasIVapo
7
2564 C
A21 6WCB SS 316 Mini
Note 1
EJflt0nMobil Chemic
Sheet 5middot11 of 46
f
No 8 Date Revision Code 2831 No C3 1052 Amiddot163 1middottVOl Rev 0
i (
II Technical amp Calculation Data Sheet SARASIN-Agt Zllloa-R~
Safety Valve Nt BiOPUIle Gt1wtI bull bull 2110 1-1_
IN I ICustomer Name TECHNIP FRANCE
891 I 4 I bull s~ I
Cuslllem Numb 7273F RFQ 1545-01
Project KHARG OLEFIN COMPLEX I Opened
I 1 I
Quote Ref Tag No PSV pound I Nde Sales Abdeljalill Baigar I
I I uperatIng onaltons
Fluid ~e Superheated Steam 19 tnle ON shy
capaci ty 78500 Kgn 20 Inlet Finish ANSI 600 RF (125-250 AARH)
3 Set presMKC 21 Outlet ON
4935 bar eM 22 OtItlet Finish ANSI 150 RF (125-250 AARH)
DiSCharge Temp 375 middotC ASME B16-5 5 Variable back presslJe bull bar eft
Cold dilf lesc press 4935 bar eft I Bill 01 I
OverptesslKe B() 10 Bod SAl16 wee a Operating ProsslKe bar elf 24 Yoke SA216 wee
25 cabull SA216 weebull bull Tlglt Closing presSlKe (MAOP) 44 415 bar eff 26 Nozzle Sellited AlSI410 bullMlaquohBnIcaI Temp J15 C 21 Disc 174 PH Stilinless Steel 28 Gaskets Stainless $t1 bullSDOM Chromium Alloy Steel 30 Golde AlSI431 31 AcluslthQRinP SAl51 CF3M 32 Stud A183flr81 33 Nul Al94gr2H
gt0 Revulr Lever
Reqllif~ Afea 32023 om 35 middot SlelUted noule
12 496 sq in TU I Gag
1 Sellcl(l(l AIel 41 2 om
I 839 sq in Orirooe p
I ReactIon loree 3016 D I Flow capacity 100996 KgIh
I Noise ill 30 m ace to AP152 1 126 dB approxmate noise level at 30 m aCCOfding to APl521 (mtluth noise) open discharge
II 37 j API52 I I I
Commercial code S46P3530A-D-VMM I
IA= 525 PlKd~Kn KbKsh I I~-middot 2254 mm 2540 mm
11800 mm
bull 1523 Kg
lA shy 89 InCh
Dab 01 COI lcul I ~ - 100 Inch
IH- 465 Inch -jshyMa55 Capaoty W 18500 KgIh 3351 Pound -IP I 553 barabs C C-ase Constant 341143 I () Indicative Values 0 now coeffiCIent Kd 09150
N Ksh 0866 w- Napier equation coffeclion Kn bull 2 valves afe necessary to reach the required capacity lt Back Pfessure correcllon Kb
BUIItmiddotup back pressurecO 1 barg 2nd Ialve set at 05 of set pranure with 10 olelpreSSure in accordill1Ce With API 520
bullbulliii
bull 11 Load cases Ioad case combinations
The following load cases f load case combinations shall be analyzed 1) always or 2) on a casemiddot to-case basis
Static load cases for operating design and pressure test conditions
L6 jillL7 I
I --shy
I --shyI I I I I
L L
I Ll 9 L20
bull ~--
Load types (iC a pplicable load types should be added) W Dead weight (pipe weight + fluid weight + insulation weight) D Displacement T Design temperature P Design internal pressure U Uniform loads (eg snow load seismic load) F External forces (forces andor moments) HP Hydro test pressure H Hanger loads WIN Wind loads (for the main wind directions) WNC Dead weight without contents (pipe weight + insulation weight) WW Water-filled weight for pressure test
bull bull bull
bull
bull ~-
bull Technip -D KHARG ETHYLENE PLANT ~
KHARG Olefin Complex
middot INmiddot I A~ I P~ UNo I 7273F 000 WI 1300 I 006 I A I 115 I 115
APPENDIX IV
L bull WIND PRESSURE I ELEVATION
11 Wind Basic nata I Wind pressure calcuJation
As per Project Basic Engineering 7273F-30-PP-206 Bask Design Data
Basic wind speed 160km h (44 5 m s)
Exposure Category 0
According to UBC 97 the design wind loading shall be
p= CxCxqX
where
P =Design wind pressure allevel 10 III
C~ =156 at leve1 10 m (EIIposure and gust factor-Table I6-G)
Cq I for DNlt= 50 nun
= 08 for DNgt 50 mm (Exposure and gust factor-Table I6-H)
qs= 1226 kNm2 ( Wind stagnation pressure at 10 m -Table J6-F)
lw = 1 15 (Importance factor - Table 16-K)
p = 220 xC (kNl m)
Height Above Wind pressure Ground Level
(m) PI eq (kNlm2 )
Oto 10 22
10 (0 20 247
20 to 30 264
30 10 40 276
40 to 50 286
50 to 60 289
60 to 70 293
70 1080 299
80 to 90 312
bull
bull
bull
bull
CONTRACTOR OOCUIENT bull N UniI Doc T Milttl CoOl srI N Rev Pa p
7273F 000 WI 1300 000 0 ()J 13
2 CONFIGURATION FILES USING CAESAR II
21 Unit System (7273FFIL)
CAE S A R liVERS 430
INPUT UNITS USED
UNITS 7273F NOMISCH INPUT ON
LENGTH inches
FORCE pounds
MASS(dynamics) pounds
MOMENTS(INPUn inch-pounds
MOMENTS(OUTPUT) inch-pounds
STRESS Ibssqin
TEMP SCALE degrees F
PRESSURE psig
ELASTIC MODULUS Ibslsqin
PI PE DENSITY Ibslcuin
INSULATION DENS Ibslcuin
FLUID DENSITY Ibslcuin
TRANSL STI F Ibslin
ROTATIONAL STiF inlbldeg
UNIFORM LOAD Jblin
GLOAD gs
WIND LOAD IbsJsqin
ELEVATION inches
COMPOUND LENGTH inches
DIAMETER inches
WALL THICKNESS inches
OWNER DOCUMENT Ndeg
~ Doc T Malerial CoOa Serial Ndeg Rev
1013
x 25400 mm
x 4448 N
x 0454 kg
x 0113 Nm
x 0113 Nm
x 0007 MPa
x 0556 C
x 0069 bars
x 0007 MPa
x 27680000 kgCrmiddotm
x 27680000 kgJcum
x 27680000 kgci m
x 0175 Nm
x 0113
l x 175127 NJm
x 1000 gs
x 6894757 NJ m
x 0025 m
x 25400 mm
x 1000 inch
x 25400 mm
bull bull
Technip
KHARG ETHYLENE PLANT KHARG Olefin Complex
PETROCHlMlCAL IND JES DIiVElOPMENT MANGEMENT CO
11113
Technip bull
KHARG ETHYLENE PLANT ~ KHARG Olefin Complex
iETltOCHEMICtl OEVEIOPMENT MANArCO
CONTRACTOR DOCUMENT N OWNER DOCUMENT Nmiddot ProIecl N p U Doe TwalMrolerial Code ISen N ReI P_ Proiect N I UNt Doo T~ I ~eriIII Code
7273F 000 WI I 1300 I 000 I 0 I 11113 I I I
22 Setup File ( CAESARCFG )
C A E SAR II VERS450
SETUP FILE PARAMETERS
CONNECT GEOMETRY THRU CNODES YES I MIN ALLOWED BEND ANGLE 500000 I MAXjLLOWED BEND ANGLE bull 135000 I BEND LENGTH ATIACHMENT PERCENT 100000 I MINjNGLE TO ADJACENT BEND PT 500000
LOOP CLOSURE TOLERANCE 254000mm
THERMAL BOWING HORZ TOLERANCE 100000E-04
AUTO NODE NUMBER INCREMENT 100000
ZJXIS UP NO
USE PRESSURE STIFFENING DEFAULT
ALPHA TOLERANCE 500000E-02
RESLDmiddotFORCE NO
HGR_DEF RESWGT STIF
bull 01751200E+12 Nlmm
DECOMP SNG TOL 01 OOOOOOE+ 11
BEND_AXIAL SHAPE NO
FRICT STIF 875600 Ni mm I FRICT NORM FORCE VAR 025000 I FRICT ANGLE VAR 300000 I FRICT SLIDE MULT 100000
ROD TOLERANCE 100000
ROD INC 200000
INCORE NUMERICAL CHECK NO
OUTCORE NUMERICAL CHECK NO
DEFAULT TRANS RESTRAINT STIFF 0175120E+12 Nlmm
DEFAULT ROT RESTRAINT STIFF 0112980E+12 Nmi deaJ
IGNORE SPRING HANGER STIFFNESS bull NO I
WI I middot AiHG bull _ KtVRCUE LOoO CAS ES_Odoc
rmiddot
bull
bull
Technip
KHARG ETHYLENE PLANT KHARG Olefin Complex
Setup File (
CONNECT_GEOMETRY _ THRU_CNODES
WRC-07 VERSION
WRC- 07
DEFAULT
831
WI I middot AIlaquo) Amiddot KHARGJUOAD CASFsOdoc
T
F
YES
NO
181 281
NO
DEFAULT
02206272E+OSbull
bullbull
bull
bull
Thchnip bull
KHARG ETHYLENE PLANT ~ KHARG Olefin Complex
PFffiOCHEMICAL INO bull DEVELOPMENT MANAG ~ENTCO_
CONTRACTOR DOCUMENT Ndeg OWNER DOCUMENT N
Proioct Ndeg Unit Doc TIIDEII Material Code Serial Ndeg Rev I Paae Proiect N Unit Doc Type Material Code Serial N A~ 7273F I 000 I WI I 1300 I 000 I a I 13 13 I 1313
FRP Ratio GmodlEmo(Uaxial) O2500000E+OO
FRP EalEhVhla O1527272E+OO
SetuD File (CAESARCFG Continuation)
FRP Lamina1e Type THREE
FRP Alpha O2159827E+02 C
FRP Density O1660800E+04 kocum bullEXCLUDE 12 FROM UKOOA BENDI NG NO
OUTPUT REPORTS BY LOAD CASE YES
DISPLACEMENT NODAL SORTING YES
DYNAMIC INPUT EXAMPLE TEXT MAX
TIME HIST ANIMATE YES
ENABLE AUTOSAVE YES
AUTOSAVE TIME INTERVAL O3000000E+02
PROMPTED AUTOSAVE YES
DISABLE UNDOREDO NO
STRUCTURAL DATABASE AISC89BIN
VALVE amp FLANGE GENERIC VHD
EXPANSION JT DBASE FLEXPATHJHD
PI PING SIZE SPECIFICATION ANSI
DEFAULT SPRING HANGER TABLE O5000000E+01
SYSTEM DIRECTORY NAME SYSTEM
UNITS FILE NAME 7273FFIL
ENABLE ODBC OUTPUT NO
DEFAULT SPRING HANGER TABLE LlSEGA
- bull -
WI 1 ANG bull IV IlHAAG_IELOAD CAS ES_OdOC
SRMPL6 LOf]) C(15euro5 S V REfK Ti O-l FOeC e- JlUE TO PSv oPttvlNG
bull Sldlle Aymmiddot [CIDO(UMpoundNTS AllD SETIINGSVhBACONI7173FmiddotMBACONICAESAR FILESICNj016_REV ~
bull
bull
bull
Edt
+ t
loadCose Edlcr LoadCoseOptiom Loads WlNeLoads
loads Oefned n IrtJIA loed Casu Stress Type
W -Woltllt L1 W+D1 +T1 +P1 +H Of 01 middot Displcmnt Case ~ L2 wO-iT2+P1 +H-- Of T1 middot Thermal Case tn l3 W~D1~T3~P1H ~(]S-oiit~~ Of LltgtOd e T2 Thermal Case 2 -- - _- ------- -__- T3 Thermal Case U3
l4 W+P1+H SUS __ _- -----PI middot Pr euUle Case 1 LS Wt-P1t-H-t-F1 OCC Hp middot Hydlo Prenae L6 Ul OCC --- ---- _----- H middot Hanger l oads 17 U2 OCC UI middot Unf Load eMe 11 La U3 OCC U2 -UriloodlAse 12 L9 F1 OCC U3 Uri l oad Case 13 L10 L1-l4 EXP F1 middot Cone FOIct Case 11 1 Ll1 L2-l4 J EXP Vlllet Fled W WNC middot W~ no corieris L12 L3-lS EXP
L13 LS+l7+l8 OCC L1 4 L-4+l13 ----l ~~ IL15 L1 lt-l1 3 L1 6 LJl9 (fD lO(ll ch 011 (f~tnlh OCC
STATIQUE LoR)) I- Ill
1
FW FRANCE NDG SHT16F I
CliENT
PROJECT
CPNo
EXXON
18KTA E5000 Expansion
CALCNo ISV 3310
CALC BY BEP
CHKD BY
DATE 13012006
RELIEF VALVE LOADINGS vapour
RV Nos ISV 3310
SIZE 4x3
RATING 150xlSO
ORIFICE L
bull DATA DESCRIPTION
RV SET PRESSURE
PERCENT OVERPRESSURE
Ps (l+PolOO) + 147
REliEF TEMPERATURE
1195492
RATIO OF SPECIFIC HEATS SIZING FLOW
SElECTED ORIFICE AREA
CALCULATED ORIFICE AREA
FACTORED SIZING flOW
MAX No OF WORKING VALVES
SIZING flOW PER VALVE
113600
MOLECULAR WEIGHT
GAS CONSTANT 1544M
SYMBOl UNITS
Ps BARG
Po
P PSIA T1 DegC
T Oeg R
k WI Kg h A sqin Ac sqin W2 Kgh N
W Ib h w Ibsec M
R ftlblb Oeg
bull GRAVITY IQ ftS2
FI=
2 W RI
gPA
VALUE
7 10 F2
12635 256
9528 105
- shyFl
t~ --+
~ middotFI FI
t5489 rTABIJSmn Ow COiiOmON
2853 NOn IIQRIZOllTAL IOItCIS Kt MtA CEil
2853 15489 F2
1 341532 +shy948701 F3
885 174463 ltV AT POICONllIll0N
322 AampUMING IMPACT CTOII OYl
260496 Ib 1159 N
128894 Ib 573 N
520993 Ib 2318 N -
bullbull
SARASIN-lltJ l7Technical amp Calculation Data Sheet ZI 8olto R~62IKI _____ J40 11ap11M GnlCMl
VAlVH e COlTllOlS Safety Valve
e Bomel lype Opened
Project KHARG OLEfiN COMPLEX ~A
Tag No PSV 6 453A C-Quote Ref 3A30880IOOO Sales Engineer Abdeljalill Baigar W de Commande
Operating ondl tlons Connect ons
19 InlelON shy1 fluid type Superheated Stetlm
20 Inlet Finish ANSt600 RF (125-250 AARH) 2 Capacity 78500 Kglh 21 Outlet DN J Set ptesSUe br eft 22 Outlet Finish ANSI 150 ftF 1125-250 AARH) Ol$charoe Tom p J7S C Accordinn 10 ASME 616-5
5 Variable bad pressure 0 bar eft
Cold (If lest lXess 47 bar eft 8111 of material 7 Overpressure 11 () 16 floltfv SA216 wee
SA2115WCC2 Ylt8 Operating Pressure 40 bar eft
SA216 wee Tight Closing pressUIe (MAOP) 423 bar eft 26 NoWe Stllited AlSl410 1~ 27 174 PH Stainless SteelMechanical Tomp J7S middotC ~ 28 Gaskets Stalnl St1
29 SPfinQ Chromium Allov Steel 30 AlSI431c31 Adusitina Rlna SA351 CF3M 32 Stud Al1lQrB7 JJ Alt4i1r2H Accessories
Regular Levr 35 51etUted nozzl
ReqUIred Area 31 927 om Test Gag 495 s q InIl Selected Area 41 2 om
I 839 sq in 15 Onfice p
Reaction loroe DN~ t Flow capacity 101299 Kglh 18 Noise at 30 m acc to APt521 120 dB
apprO)flTlate noise level at 30 m according to API521 (mouth noiso) )perl dlsctlarge
Customer Name TECHNIP FRANCE evlslon ~ lion ate
890 4 20-juin-2005
Cust Item Numb 7U3F RFQ 1545-01 a ely a ype pflllg a a ely alve ea1T
I I J7 Standard API 520 I )
Commercial code S46P3530AmiddotDmiddotVMM I shyI Dimensions
A- 2254 mm B- 2540 mm W - 11800 mrnIA 525PlKd~KnKb Kshl ~ Welghl() s 1523 Kg I A- 89 Inch I bullB- 100 Inch
Dati 01 calcul w - 4115 Inch Mass Capaatv W 18500 KgIh Weight( ) 3357 Pound
P1 5553 bar abs r~ C Gase Constant 143843
() Indicative Values 0 now ooeIficient Kd 0915 0
Ksn 0865 Remarks Napier equation correction Kn 1
~ 2 valves are necessary 10 reach the required capacity
Back pressure correcUon Kb 1a BUlHmiddotup back pressureO 1 berg Same calculallO1 heet lor the 1st va lve and the spare one bull
N
~
GENERAl
PEO
PROCESS
CONDITONS
bull DESIGN
DATA
bull MATERIALS
I
OPT IONS
1 T Nu~
2 Service 3 Line NUrMer 4 P amp to Numbef
5 6 Conform to 961231EC 7 Fluid T
8 NJ licable rED Table 9
0 11
12
13
14
15 16
17 19
20 21 22
PED Cal
Fluid Fluid Servlc Required Capaci
MoltcullWe hI
ratln PrtSi ur
tlll TIm tUri
Badlt Prl$IIure
AJlovtabie Ova sure
Ov esslI10 FactOI Com esslbU Latenl Heal 01 V lion
o Tl 1012812005 Pour Commenta ires
Equipment
Fluid Groo
Fluid S~I
5 cltle Gl1Ivl Set Pressure
Col
HC+H20
15489
5 02
ReHov Temperatlyene 212
Constant Varia1je Total
23 Specific Hnt RItIo lC 24 Relief Densi
25 Relief Viscosity
26 Barometric Pressure 27 28 Nozzle Flit Semi
29 Design Saely Reflef Sale -Relief 30 Type Conventional BelloIN Plot Opefatad 31 BonnetT 32 n Code
33 Sizing Basis 34 Calcula ted Area
35 Selected Area 36 Orifice De nation
37 Size Rating -Inlel 38 Size Rat - Outlet
39 40 41 42 43 Stt 44 Fla es
45 Resilient Seat Seal 46 Guide
471 Spfing 46 Wtted Material
49 50
Bonnt Disc
Ri s Bellows
51 Cap Screwed or Bolted 52 Lever Plain or Packed 53 TestGag
54 55
22-ISV 3310 0 331fD332 SHCOO20150A1A 1 l -Q2S)(l2
y Gaseous Group 1
0 1
0
09
105
4
Note 10
k
C
k p
Safety Corrventlonal
hI Solted
ASME Delaut eau de refroldissement
1812 em
L 3 150 RF 450 RF
A2 16 WCB
NOlet A216WCB
NOle 1
Note 1
NOIot
NOIel
(Note 1
No
No
INSTRUMENT SPECIFICATION
Valve Safety Pressure Relief
oxicFlammable
GasIVapo
7
2564 C
A21 6WCB SS 316 Mini
Note 1
EJflt0nMobil Chemic
Sheet 5middot11 of 46
f
No 8 Date Revision Code 2831 No C3 1052 Amiddot163 1middottVOl Rev 0
i (
II Technical amp Calculation Data Sheet SARASIN-Agt Zllloa-R~
Safety Valve Nt BiOPUIle Gt1wtI bull bull 2110 1-1_
IN I ICustomer Name TECHNIP FRANCE
891 I 4 I bull s~ I
Cuslllem Numb 7273F RFQ 1545-01
Project KHARG OLEFIN COMPLEX I Opened
I 1 I
Quote Ref Tag No PSV pound I Nde Sales Abdeljalill Baigar I
I I uperatIng onaltons
Fluid ~e Superheated Steam 19 tnle ON shy
capaci ty 78500 Kgn 20 Inlet Finish ANSI 600 RF (125-250 AARH)
3 Set presMKC 21 Outlet ON
4935 bar eM 22 OtItlet Finish ANSI 150 RF (125-250 AARH)
DiSCharge Temp 375 middotC ASME B16-5 5 Variable back presslJe bull bar eft
Cold dilf lesc press 4935 bar eft I Bill 01 I
OverptesslKe B() 10 Bod SAl16 wee a Operating ProsslKe bar elf 24 Yoke SA216 wee
25 cabull SA216 weebull bull Tlglt Closing presSlKe (MAOP) 44 415 bar eff 26 Nozzle Sellited AlSI410 bullMlaquohBnIcaI Temp J15 C 21 Disc 174 PH Stilinless Steel 28 Gaskets Stainless $t1 bullSDOM Chromium Alloy Steel 30 Golde AlSI431 31 AcluslthQRinP SAl51 CF3M 32 Stud A183flr81 33 Nul Al94gr2H
gt0 Revulr Lever
Reqllif~ Afea 32023 om 35 middot SlelUted noule
12 496 sq in TU I Gag
1 Sellcl(l(l AIel 41 2 om
I 839 sq in Orirooe p
I ReactIon loree 3016 D I Flow capacity 100996 KgIh
I Noise ill 30 m ace to AP152 1 126 dB approxmate noise level at 30 m aCCOfding to APl521 (mtluth noise) open discharge
II 37 j API52 I I I
Commercial code S46P3530A-D-VMM I
IA= 525 PlKd~Kn KbKsh I I~-middot 2254 mm 2540 mm
11800 mm
bull 1523 Kg
lA shy 89 InCh
Dab 01 COI lcul I ~ - 100 Inch
IH- 465 Inch -jshyMa55 Capaoty W 18500 KgIh 3351 Pound -IP I 553 barabs C C-ase Constant 341143 I () Indicative Values 0 now coeffiCIent Kd 09150
N Ksh 0866 w- Napier equation coffeclion Kn bull 2 valves afe necessary to reach the required capacity lt Back Pfessure correcllon Kb
BUIItmiddotup back pressurecO 1 barg 2nd Ialve set at 05 of set pranure with 10 olelpreSSure in accordill1Ce With API 520
bullbulliii
bull 11 Load cases Ioad case combinations
The following load cases f load case combinations shall be analyzed 1) always or 2) on a casemiddot to-case basis
Static load cases for operating design and pressure test conditions
L6 jillL7 I
I --shy
I --shyI I I I I
L L
I Ll 9 L20
bull ~--
Load types (iC a pplicable load types should be added) W Dead weight (pipe weight + fluid weight + insulation weight) D Displacement T Design temperature P Design internal pressure U Uniform loads (eg snow load seismic load) F External forces (forces andor moments) HP Hydro test pressure H Hanger loads WIN Wind loads (for the main wind directions) WNC Dead weight without contents (pipe weight + insulation weight) WW Water-filled weight for pressure test
bull bull bull
bull
bull ~-
bull
bull
bull
CONTRACTOR OOCUIENT bull N UniI Doc T Milttl CoOl srI N Rev Pa p
7273F 000 WI 1300 000 0 ()J 13
2 CONFIGURATION FILES USING CAESAR II
21 Unit System (7273FFIL)
CAE S A R liVERS 430
INPUT UNITS USED
UNITS 7273F NOMISCH INPUT ON
LENGTH inches
FORCE pounds
MASS(dynamics) pounds
MOMENTS(INPUn inch-pounds
MOMENTS(OUTPUT) inch-pounds
STRESS Ibssqin
TEMP SCALE degrees F
PRESSURE psig
ELASTIC MODULUS Ibslsqin
PI PE DENSITY Ibslcuin
INSULATION DENS Ibslcuin
FLUID DENSITY Ibslcuin
TRANSL STI F Ibslin
ROTATIONAL STiF inlbldeg
UNIFORM LOAD Jblin
GLOAD gs
WIND LOAD IbsJsqin
ELEVATION inches
COMPOUND LENGTH inches
DIAMETER inches
WALL THICKNESS inches
OWNER DOCUMENT Ndeg
~ Doc T Malerial CoOa Serial Ndeg Rev
1013
x 25400 mm
x 4448 N
x 0454 kg
x 0113 Nm
x 0113 Nm
x 0007 MPa
x 0556 C
x 0069 bars
x 0007 MPa
x 27680000 kgCrmiddotm
x 27680000 kgJcum
x 27680000 kgci m
x 0175 Nm
x 0113
l x 175127 NJm
x 1000 gs
x 6894757 NJ m
x 0025 m
x 25400 mm
x 1000 inch
x 25400 mm
bull bull
Technip
KHARG ETHYLENE PLANT KHARG Olefin Complex
PETROCHlMlCAL IND JES DIiVElOPMENT MANGEMENT CO
11113
Technip bull
KHARG ETHYLENE PLANT ~ KHARG Olefin Complex
iETltOCHEMICtl OEVEIOPMENT MANArCO
CONTRACTOR DOCUMENT N OWNER DOCUMENT Nmiddot ProIecl N p U Doe TwalMrolerial Code ISen N ReI P_ Proiect N I UNt Doo T~ I ~eriIII Code
7273F 000 WI I 1300 I 000 I 0 I 11113 I I I
22 Setup File ( CAESARCFG )
C A E SAR II VERS450
SETUP FILE PARAMETERS
CONNECT GEOMETRY THRU CNODES YES I MIN ALLOWED BEND ANGLE 500000 I MAXjLLOWED BEND ANGLE bull 135000 I BEND LENGTH ATIACHMENT PERCENT 100000 I MINjNGLE TO ADJACENT BEND PT 500000
LOOP CLOSURE TOLERANCE 254000mm
THERMAL BOWING HORZ TOLERANCE 100000E-04
AUTO NODE NUMBER INCREMENT 100000
ZJXIS UP NO
USE PRESSURE STIFFENING DEFAULT
ALPHA TOLERANCE 500000E-02
RESLDmiddotFORCE NO
HGR_DEF RESWGT STIF
bull 01751200E+12 Nlmm
DECOMP SNG TOL 01 OOOOOOE+ 11
BEND_AXIAL SHAPE NO
FRICT STIF 875600 Ni mm I FRICT NORM FORCE VAR 025000 I FRICT ANGLE VAR 300000 I FRICT SLIDE MULT 100000
ROD TOLERANCE 100000
ROD INC 200000
INCORE NUMERICAL CHECK NO
OUTCORE NUMERICAL CHECK NO
DEFAULT TRANS RESTRAINT STIFF 0175120E+12 Nlmm
DEFAULT ROT RESTRAINT STIFF 0112980E+12 Nmi deaJ
IGNORE SPRING HANGER STIFFNESS bull NO I
WI I middot AiHG bull _ KtVRCUE LOoO CAS ES_Odoc
rmiddot
bull
bull
Technip
KHARG ETHYLENE PLANT KHARG Olefin Complex
Setup File (
CONNECT_GEOMETRY _ THRU_CNODES
WRC-07 VERSION
WRC- 07
DEFAULT
831
WI I middot AIlaquo) Amiddot KHARGJUOAD CASFsOdoc
T
F
YES
NO
181 281
NO
DEFAULT
02206272E+OSbull
bullbull
bull
bull
Thchnip bull
KHARG ETHYLENE PLANT ~ KHARG Olefin Complex
PFffiOCHEMICAL INO bull DEVELOPMENT MANAG ~ENTCO_
CONTRACTOR DOCUMENT Ndeg OWNER DOCUMENT N
Proioct Ndeg Unit Doc TIIDEII Material Code Serial Ndeg Rev I Paae Proiect N Unit Doc Type Material Code Serial N A~ 7273F I 000 I WI I 1300 I 000 I a I 13 13 I 1313
FRP Ratio GmodlEmo(Uaxial) O2500000E+OO
FRP EalEhVhla O1527272E+OO
SetuD File (CAESARCFG Continuation)
FRP Lamina1e Type THREE
FRP Alpha O2159827E+02 C
FRP Density O1660800E+04 kocum bullEXCLUDE 12 FROM UKOOA BENDI NG NO
OUTPUT REPORTS BY LOAD CASE YES
DISPLACEMENT NODAL SORTING YES
DYNAMIC INPUT EXAMPLE TEXT MAX
TIME HIST ANIMATE YES
ENABLE AUTOSAVE YES
AUTOSAVE TIME INTERVAL O3000000E+02
PROMPTED AUTOSAVE YES
DISABLE UNDOREDO NO
STRUCTURAL DATABASE AISC89BIN
VALVE amp FLANGE GENERIC VHD
EXPANSION JT DBASE FLEXPATHJHD
PI PING SIZE SPECIFICATION ANSI
DEFAULT SPRING HANGER TABLE O5000000E+01
SYSTEM DIRECTORY NAME SYSTEM
UNITS FILE NAME 7273FFIL
ENABLE ODBC OUTPUT NO
DEFAULT SPRING HANGER TABLE LlSEGA
- bull -
WI 1 ANG bull IV IlHAAG_IELOAD CAS ES_OdOC
SRMPL6 LOf]) C(15euro5 S V REfK Ti O-l FOeC e- JlUE TO PSv oPttvlNG
bull Sldlle Aymmiddot [CIDO(UMpoundNTS AllD SETIINGSVhBACONI7173FmiddotMBACONICAESAR FILESICNj016_REV ~
bull
bull
bull
Edt
+ t
loadCose Edlcr LoadCoseOptiom Loads WlNeLoads
loads Oefned n IrtJIA loed Casu Stress Type
W -Woltllt L1 W+D1 +T1 +P1 +H Of 01 middot Displcmnt Case ~ L2 wO-iT2+P1 +H-- Of T1 middot Thermal Case tn l3 W~D1~T3~P1H ~(]S-oiit~~ Of LltgtOd e T2 Thermal Case 2 -- - _- ------- -__- T3 Thermal Case U3
l4 W+P1+H SUS __ _- -----PI middot Pr euUle Case 1 LS Wt-P1t-H-t-F1 OCC Hp middot Hydlo Prenae L6 Ul OCC --- ---- _----- H middot Hanger l oads 17 U2 OCC UI middot Unf Load eMe 11 La U3 OCC U2 -UriloodlAse 12 L9 F1 OCC U3 Uri l oad Case 13 L10 L1-l4 EXP F1 middot Cone FOIct Case 11 1 Ll1 L2-l4 J EXP Vlllet Fled W WNC middot W~ no corieris L12 L3-lS EXP
L13 LS+l7+l8 OCC L1 4 L-4+l13 ----l ~~ IL15 L1 lt-l1 3 L1 6 LJl9 (fD lO(ll ch 011 (f~tnlh OCC
STATIQUE LoR)) I- Ill
1
FW FRANCE NDG SHT16F I
CliENT
PROJECT
CPNo
EXXON
18KTA E5000 Expansion
CALCNo ISV 3310
CALC BY BEP
CHKD BY
DATE 13012006
RELIEF VALVE LOADINGS vapour
RV Nos ISV 3310
SIZE 4x3
RATING 150xlSO
ORIFICE L
bull DATA DESCRIPTION
RV SET PRESSURE
PERCENT OVERPRESSURE
Ps (l+PolOO) + 147
REliEF TEMPERATURE
1195492
RATIO OF SPECIFIC HEATS SIZING FLOW
SElECTED ORIFICE AREA
CALCULATED ORIFICE AREA
FACTORED SIZING flOW
MAX No OF WORKING VALVES
SIZING flOW PER VALVE
113600
MOLECULAR WEIGHT
GAS CONSTANT 1544M
SYMBOl UNITS
Ps BARG
Po
P PSIA T1 DegC
T Oeg R
k WI Kg h A sqin Ac sqin W2 Kgh N
W Ib h w Ibsec M
R ftlblb Oeg
bull GRAVITY IQ ftS2
FI=
2 W RI
gPA
VALUE
7 10 F2
12635 256
9528 105
- shyFl
t~ --+
~ middotFI FI
t5489 rTABIJSmn Ow COiiOmON
2853 NOn IIQRIZOllTAL IOItCIS Kt MtA CEil
2853 15489 F2
1 341532 +shy948701 F3
885 174463 ltV AT POICONllIll0N
322 AampUMING IMPACT CTOII OYl
260496 Ib 1159 N
128894 Ib 573 N
520993 Ib 2318 N -
bullbull
SARASIN-lltJ l7Technical amp Calculation Data Sheet ZI 8olto R~62IKI _____ J40 11ap11M GnlCMl
VAlVH e COlTllOlS Safety Valve
e Bomel lype Opened
Project KHARG OLEfiN COMPLEX ~A
Tag No PSV 6 453A C-Quote Ref 3A30880IOOO Sales Engineer Abdeljalill Baigar W de Commande
Operating ondl tlons Connect ons
19 InlelON shy1 fluid type Superheated Stetlm
20 Inlet Finish ANSt600 RF (125-250 AARH) 2 Capacity 78500 Kglh 21 Outlet DN J Set ptesSUe br eft 22 Outlet Finish ANSI 150 ftF 1125-250 AARH) Ol$charoe Tom p J7S C Accordinn 10 ASME 616-5
5 Variable bad pressure 0 bar eft
Cold (If lest lXess 47 bar eft 8111 of material 7 Overpressure 11 () 16 floltfv SA216 wee
SA2115WCC2 Ylt8 Operating Pressure 40 bar eft
SA216 wee Tight Closing pressUIe (MAOP) 423 bar eft 26 NoWe Stllited AlSl410 1~ 27 174 PH Stainless SteelMechanical Tomp J7S middotC ~ 28 Gaskets Stalnl St1
29 SPfinQ Chromium Allov Steel 30 AlSI431c31 Adusitina Rlna SA351 CF3M 32 Stud Al1lQrB7 JJ Alt4i1r2H Accessories
Regular Levr 35 51etUted nozzl
ReqUIred Area 31 927 om Test Gag 495 s q InIl Selected Area 41 2 om
I 839 sq in 15 Onfice p
Reaction loroe DN~ t Flow capacity 101299 Kglh 18 Noise at 30 m acc to APt521 120 dB
apprO)flTlate noise level at 30 m according to API521 (mouth noiso) )perl dlsctlarge
Customer Name TECHNIP FRANCE evlslon ~ lion ate
890 4 20-juin-2005
Cust Item Numb 7U3F RFQ 1545-01 a ely a ype pflllg a a ely alve ea1T
I I J7 Standard API 520 I )
Commercial code S46P3530AmiddotDmiddotVMM I shyI Dimensions
A- 2254 mm B- 2540 mm W - 11800 mrnIA 525PlKd~KnKb Kshl ~ Welghl() s 1523 Kg I A- 89 Inch I bullB- 100 Inch
Dati 01 calcul w - 4115 Inch Mass Capaatv W 18500 KgIh Weight( ) 3357 Pound
P1 5553 bar abs r~ C Gase Constant 143843
() Indicative Values 0 now ooeIficient Kd 0915 0
Ksn 0865 Remarks Napier equation correction Kn 1
~ 2 valves are necessary 10 reach the required capacity
Back pressure correcUon Kb 1a BUlHmiddotup back pressureO 1 berg Same calculallO1 heet lor the 1st va lve and the spare one bull
N
~
GENERAl
PEO
PROCESS
CONDITONS
bull DESIGN
DATA
bull MATERIALS
I
OPT IONS
1 T Nu~
2 Service 3 Line NUrMer 4 P amp to Numbef
5 6 Conform to 961231EC 7 Fluid T
8 NJ licable rED Table 9
0 11
12
13
14
15 16
17 19
20 21 22
PED Cal
Fluid Fluid Servlc Required Capaci
MoltcullWe hI
ratln PrtSi ur
tlll TIm tUri
Badlt Prl$IIure
AJlovtabie Ova sure
Ov esslI10 FactOI Com esslbU Latenl Heal 01 V lion
o Tl 1012812005 Pour Commenta ires
Equipment
Fluid Groo
Fluid S~I
5 cltle Gl1Ivl Set Pressure
Col
HC+H20
15489
5 02
ReHov Temperatlyene 212
Constant Varia1je Total
23 Specific Hnt RItIo lC 24 Relief Densi
25 Relief Viscosity
26 Barometric Pressure 27 28 Nozzle Flit Semi
29 Design Saely Reflef Sale -Relief 30 Type Conventional BelloIN Plot Opefatad 31 BonnetT 32 n Code
33 Sizing Basis 34 Calcula ted Area
35 Selected Area 36 Orifice De nation
37 Size Rating -Inlel 38 Size Rat - Outlet
39 40 41 42 43 Stt 44 Fla es
45 Resilient Seat Seal 46 Guide
471 Spfing 46 Wtted Material
49 50
Bonnt Disc
Ri s Bellows
51 Cap Screwed or Bolted 52 Lever Plain or Packed 53 TestGag
54 55
22-ISV 3310 0 331fD332 SHCOO20150A1A 1 l -Q2S)(l2
y Gaseous Group 1
0 1
0
09
105
4
Note 10
k
C
k p
Safety Corrventlonal
hI Solted
ASME Delaut eau de refroldissement
1812 em
L 3 150 RF 450 RF
A2 16 WCB
NOlet A216WCB
NOle 1
Note 1
NOIot
NOIel
(Note 1
No
No
INSTRUMENT SPECIFICATION
Valve Safety Pressure Relief
oxicFlammable
GasIVapo
7
2564 C
A21 6WCB SS 316 Mini
Note 1
EJflt0nMobil Chemic
Sheet 5middot11 of 46
f
No 8 Date Revision Code 2831 No C3 1052 Amiddot163 1middottVOl Rev 0
i (
II Technical amp Calculation Data Sheet SARASIN-Agt Zllloa-R~
Safety Valve Nt BiOPUIle Gt1wtI bull bull 2110 1-1_
IN I ICustomer Name TECHNIP FRANCE
891 I 4 I bull s~ I
Cuslllem Numb 7273F RFQ 1545-01
Project KHARG OLEFIN COMPLEX I Opened
I 1 I
Quote Ref Tag No PSV pound I Nde Sales Abdeljalill Baigar I
I I uperatIng onaltons
Fluid ~e Superheated Steam 19 tnle ON shy
capaci ty 78500 Kgn 20 Inlet Finish ANSI 600 RF (125-250 AARH)
3 Set presMKC 21 Outlet ON
4935 bar eM 22 OtItlet Finish ANSI 150 RF (125-250 AARH)
DiSCharge Temp 375 middotC ASME B16-5 5 Variable back presslJe bull bar eft
Cold dilf lesc press 4935 bar eft I Bill 01 I
OverptesslKe B() 10 Bod SAl16 wee a Operating ProsslKe bar elf 24 Yoke SA216 wee
25 cabull SA216 weebull bull Tlglt Closing presSlKe (MAOP) 44 415 bar eff 26 Nozzle Sellited AlSI410 bullMlaquohBnIcaI Temp J15 C 21 Disc 174 PH Stilinless Steel 28 Gaskets Stainless $t1 bullSDOM Chromium Alloy Steel 30 Golde AlSI431 31 AcluslthQRinP SAl51 CF3M 32 Stud A183flr81 33 Nul Al94gr2H
gt0 Revulr Lever
Reqllif~ Afea 32023 om 35 middot SlelUted noule
12 496 sq in TU I Gag
1 Sellcl(l(l AIel 41 2 om
I 839 sq in Orirooe p
I ReactIon loree 3016 D I Flow capacity 100996 KgIh
I Noise ill 30 m ace to AP152 1 126 dB approxmate noise level at 30 m aCCOfding to APl521 (mtluth noise) open discharge
II 37 j API52 I I I
Commercial code S46P3530A-D-VMM I
IA= 525 PlKd~Kn KbKsh I I~-middot 2254 mm 2540 mm
11800 mm
bull 1523 Kg
lA shy 89 InCh
Dab 01 COI lcul I ~ - 100 Inch
IH- 465 Inch -jshyMa55 Capaoty W 18500 KgIh 3351 Pound -IP I 553 barabs C C-ase Constant 341143 I () Indicative Values 0 now coeffiCIent Kd 09150
N Ksh 0866 w- Napier equation coffeclion Kn bull 2 valves afe necessary to reach the required capacity lt Back Pfessure correcllon Kb
BUIItmiddotup back pressurecO 1 barg 2nd Ialve set at 05 of set pranure with 10 olelpreSSure in accordill1Ce With API 520
bullbulliii
bull 11 Load cases Ioad case combinations
The following load cases f load case combinations shall be analyzed 1) always or 2) on a casemiddot to-case basis
Static load cases for operating design and pressure test conditions
L6 jillL7 I
I --shy
I --shyI I I I I
L L
I Ll 9 L20
bull ~--
Load types (iC a pplicable load types should be added) W Dead weight (pipe weight + fluid weight + insulation weight) D Displacement T Design temperature P Design internal pressure U Uniform loads (eg snow load seismic load) F External forces (forces andor moments) HP Hydro test pressure H Hanger loads WIN Wind loads (for the main wind directions) WNC Dead weight without contents (pipe weight + insulation weight) WW Water-filled weight for pressure test
bull bull bull
bull
bull ~-
11113
Technip bull
KHARG ETHYLENE PLANT ~ KHARG Olefin Complex
iETltOCHEMICtl OEVEIOPMENT MANArCO
CONTRACTOR DOCUMENT N OWNER DOCUMENT Nmiddot ProIecl N p U Doe TwalMrolerial Code ISen N ReI P_ Proiect N I UNt Doo T~ I ~eriIII Code
7273F 000 WI I 1300 I 000 I 0 I 11113 I I I
22 Setup File ( CAESARCFG )
C A E SAR II VERS450
SETUP FILE PARAMETERS
CONNECT GEOMETRY THRU CNODES YES I MIN ALLOWED BEND ANGLE 500000 I MAXjLLOWED BEND ANGLE bull 135000 I BEND LENGTH ATIACHMENT PERCENT 100000 I MINjNGLE TO ADJACENT BEND PT 500000
LOOP CLOSURE TOLERANCE 254000mm
THERMAL BOWING HORZ TOLERANCE 100000E-04
AUTO NODE NUMBER INCREMENT 100000
ZJXIS UP NO
USE PRESSURE STIFFENING DEFAULT
ALPHA TOLERANCE 500000E-02
RESLDmiddotFORCE NO
HGR_DEF RESWGT STIF
bull 01751200E+12 Nlmm
DECOMP SNG TOL 01 OOOOOOE+ 11
BEND_AXIAL SHAPE NO
FRICT STIF 875600 Ni mm I FRICT NORM FORCE VAR 025000 I FRICT ANGLE VAR 300000 I FRICT SLIDE MULT 100000
ROD TOLERANCE 100000
ROD INC 200000
INCORE NUMERICAL CHECK NO
OUTCORE NUMERICAL CHECK NO
DEFAULT TRANS RESTRAINT STIFF 0175120E+12 Nlmm
DEFAULT ROT RESTRAINT STIFF 0112980E+12 Nmi deaJ
IGNORE SPRING HANGER STIFFNESS bull NO I
WI I middot AiHG bull _ KtVRCUE LOoO CAS ES_Odoc
rmiddot
bull
bull
Technip
KHARG ETHYLENE PLANT KHARG Olefin Complex
Setup File (
CONNECT_GEOMETRY _ THRU_CNODES
WRC-07 VERSION
WRC- 07
DEFAULT
831
WI I middot AIlaquo) Amiddot KHARGJUOAD CASFsOdoc
T
F
YES
NO
181 281
NO
DEFAULT
02206272E+OSbull
bullbull
bull
bull
Thchnip bull
KHARG ETHYLENE PLANT ~ KHARG Olefin Complex
PFffiOCHEMICAL INO bull DEVELOPMENT MANAG ~ENTCO_
CONTRACTOR DOCUMENT Ndeg OWNER DOCUMENT N
Proioct Ndeg Unit Doc TIIDEII Material Code Serial Ndeg Rev I Paae Proiect N Unit Doc Type Material Code Serial N A~ 7273F I 000 I WI I 1300 I 000 I a I 13 13 I 1313
FRP Ratio GmodlEmo(Uaxial) O2500000E+OO
FRP EalEhVhla O1527272E+OO
SetuD File (CAESARCFG Continuation)
FRP Lamina1e Type THREE
FRP Alpha O2159827E+02 C
FRP Density O1660800E+04 kocum bullEXCLUDE 12 FROM UKOOA BENDI NG NO
OUTPUT REPORTS BY LOAD CASE YES
DISPLACEMENT NODAL SORTING YES
DYNAMIC INPUT EXAMPLE TEXT MAX
TIME HIST ANIMATE YES
ENABLE AUTOSAVE YES
AUTOSAVE TIME INTERVAL O3000000E+02
PROMPTED AUTOSAVE YES
DISABLE UNDOREDO NO
STRUCTURAL DATABASE AISC89BIN
VALVE amp FLANGE GENERIC VHD
EXPANSION JT DBASE FLEXPATHJHD
PI PING SIZE SPECIFICATION ANSI
DEFAULT SPRING HANGER TABLE O5000000E+01
SYSTEM DIRECTORY NAME SYSTEM
UNITS FILE NAME 7273FFIL
ENABLE ODBC OUTPUT NO
DEFAULT SPRING HANGER TABLE LlSEGA
- bull -
WI 1 ANG bull IV IlHAAG_IELOAD CAS ES_OdOC
SRMPL6 LOf]) C(15euro5 S V REfK Ti O-l FOeC e- JlUE TO PSv oPttvlNG
bull Sldlle Aymmiddot [CIDO(UMpoundNTS AllD SETIINGSVhBACONI7173FmiddotMBACONICAESAR FILESICNj016_REV ~
bull
bull
bull
Edt
+ t
loadCose Edlcr LoadCoseOptiom Loads WlNeLoads
loads Oefned n IrtJIA loed Casu Stress Type
W -Woltllt L1 W+D1 +T1 +P1 +H Of 01 middot Displcmnt Case ~ L2 wO-iT2+P1 +H-- Of T1 middot Thermal Case tn l3 W~D1~T3~P1H ~(]S-oiit~~ Of LltgtOd e T2 Thermal Case 2 -- - _- ------- -__- T3 Thermal Case U3
l4 W+P1+H SUS __ _- -----PI middot Pr euUle Case 1 LS Wt-P1t-H-t-F1 OCC Hp middot Hydlo Prenae L6 Ul OCC --- ---- _----- H middot Hanger l oads 17 U2 OCC UI middot Unf Load eMe 11 La U3 OCC U2 -UriloodlAse 12 L9 F1 OCC U3 Uri l oad Case 13 L10 L1-l4 EXP F1 middot Cone FOIct Case 11 1 Ll1 L2-l4 J EXP Vlllet Fled W WNC middot W~ no corieris L12 L3-lS EXP
L13 LS+l7+l8 OCC L1 4 L-4+l13 ----l ~~ IL15 L1 lt-l1 3 L1 6 LJl9 (fD lO(ll ch 011 (f~tnlh OCC
STATIQUE LoR)) I- Ill
1
FW FRANCE NDG SHT16F I
CliENT
PROJECT
CPNo
EXXON
18KTA E5000 Expansion
CALCNo ISV 3310
CALC BY BEP
CHKD BY
DATE 13012006
RELIEF VALVE LOADINGS vapour
RV Nos ISV 3310
SIZE 4x3
RATING 150xlSO
ORIFICE L
bull DATA DESCRIPTION
RV SET PRESSURE
PERCENT OVERPRESSURE
Ps (l+PolOO) + 147
REliEF TEMPERATURE
1195492
RATIO OF SPECIFIC HEATS SIZING FLOW
SElECTED ORIFICE AREA
CALCULATED ORIFICE AREA
FACTORED SIZING flOW
MAX No OF WORKING VALVES
SIZING flOW PER VALVE
113600
MOLECULAR WEIGHT
GAS CONSTANT 1544M
SYMBOl UNITS
Ps BARG
Po
P PSIA T1 DegC
T Oeg R
k WI Kg h A sqin Ac sqin W2 Kgh N
W Ib h w Ibsec M
R ftlblb Oeg
bull GRAVITY IQ ftS2
FI=
2 W RI
gPA
VALUE
7 10 F2
12635 256
9528 105
- shyFl
t~ --+
~ middotFI FI
t5489 rTABIJSmn Ow COiiOmON
2853 NOn IIQRIZOllTAL IOItCIS Kt MtA CEil
2853 15489 F2
1 341532 +shy948701 F3
885 174463 ltV AT POICONllIll0N
322 AampUMING IMPACT CTOII OYl
260496 Ib 1159 N
128894 Ib 573 N
520993 Ib 2318 N -
bullbull
SARASIN-lltJ l7Technical amp Calculation Data Sheet ZI 8olto R~62IKI _____ J40 11ap11M GnlCMl
VAlVH e COlTllOlS Safety Valve
e Bomel lype Opened
Project KHARG OLEfiN COMPLEX ~A
Tag No PSV 6 453A C-Quote Ref 3A30880IOOO Sales Engineer Abdeljalill Baigar W de Commande
Operating ondl tlons Connect ons
19 InlelON shy1 fluid type Superheated Stetlm
20 Inlet Finish ANSt600 RF (125-250 AARH) 2 Capacity 78500 Kglh 21 Outlet DN J Set ptesSUe br eft 22 Outlet Finish ANSI 150 ftF 1125-250 AARH) Ol$charoe Tom p J7S C Accordinn 10 ASME 616-5
5 Variable bad pressure 0 bar eft
Cold (If lest lXess 47 bar eft 8111 of material 7 Overpressure 11 () 16 floltfv SA216 wee
SA2115WCC2 Ylt8 Operating Pressure 40 bar eft
SA216 wee Tight Closing pressUIe (MAOP) 423 bar eft 26 NoWe Stllited AlSl410 1~ 27 174 PH Stainless SteelMechanical Tomp J7S middotC ~ 28 Gaskets Stalnl St1
29 SPfinQ Chromium Allov Steel 30 AlSI431c31 Adusitina Rlna SA351 CF3M 32 Stud Al1lQrB7 JJ Alt4i1r2H Accessories
Regular Levr 35 51etUted nozzl
ReqUIred Area 31 927 om Test Gag 495 s q InIl Selected Area 41 2 om
I 839 sq in 15 Onfice p
Reaction loroe DN~ t Flow capacity 101299 Kglh 18 Noise at 30 m acc to APt521 120 dB
apprO)flTlate noise level at 30 m according to API521 (mouth noiso) )perl dlsctlarge
Customer Name TECHNIP FRANCE evlslon ~ lion ate
890 4 20-juin-2005
Cust Item Numb 7U3F RFQ 1545-01 a ely a ype pflllg a a ely alve ea1T
I I J7 Standard API 520 I )
Commercial code S46P3530AmiddotDmiddotVMM I shyI Dimensions
A- 2254 mm B- 2540 mm W - 11800 mrnIA 525PlKd~KnKb Kshl ~ Welghl() s 1523 Kg I A- 89 Inch I bullB- 100 Inch
Dati 01 calcul w - 4115 Inch Mass Capaatv W 18500 KgIh Weight( ) 3357 Pound
P1 5553 bar abs r~ C Gase Constant 143843
() Indicative Values 0 now ooeIficient Kd 0915 0
Ksn 0865 Remarks Napier equation correction Kn 1
~ 2 valves are necessary 10 reach the required capacity
Back pressure correcUon Kb 1a BUlHmiddotup back pressureO 1 berg Same calculallO1 heet lor the 1st va lve and the spare one bull
N
~
GENERAl
PEO
PROCESS
CONDITONS
bull DESIGN
DATA
bull MATERIALS
I
OPT IONS
1 T Nu~
2 Service 3 Line NUrMer 4 P amp to Numbef
5 6 Conform to 961231EC 7 Fluid T
8 NJ licable rED Table 9
0 11
12
13
14
15 16
17 19
20 21 22
PED Cal
Fluid Fluid Servlc Required Capaci
MoltcullWe hI
ratln PrtSi ur
tlll TIm tUri
Badlt Prl$IIure
AJlovtabie Ova sure
Ov esslI10 FactOI Com esslbU Latenl Heal 01 V lion
o Tl 1012812005 Pour Commenta ires
Equipment
Fluid Groo
Fluid S~I
5 cltle Gl1Ivl Set Pressure
Col
HC+H20
15489
5 02
ReHov Temperatlyene 212
Constant Varia1je Total
23 Specific Hnt RItIo lC 24 Relief Densi
25 Relief Viscosity
26 Barometric Pressure 27 28 Nozzle Flit Semi
29 Design Saely Reflef Sale -Relief 30 Type Conventional BelloIN Plot Opefatad 31 BonnetT 32 n Code
33 Sizing Basis 34 Calcula ted Area
35 Selected Area 36 Orifice De nation
37 Size Rating -Inlel 38 Size Rat - Outlet
39 40 41 42 43 Stt 44 Fla es
45 Resilient Seat Seal 46 Guide
471 Spfing 46 Wtted Material
49 50
Bonnt Disc
Ri s Bellows
51 Cap Screwed or Bolted 52 Lever Plain or Packed 53 TestGag
54 55
22-ISV 3310 0 331fD332 SHCOO20150A1A 1 l -Q2S)(l2
y Gaseous Group 1
0 1
0
09
105
4
Note 10
k
C
k p
Safety Corrventlonal
hI Solted
ASME Delaut eau de refroldissement
1812 em
L 3 150 RF 450 RF
A2 16 WCB
NOlet A216WCB
NOle 1
Note 1
NOIot
NOIel
(Note 1
No
No
INSTRUMENT SPECIFICATION
Valve Safety Pressure Relief
oxicFlammable
GasIVapo
7
2564 C
A21 6WCB SS 316 Mini
Note 1
EJflt0nMobil Chemic
Sheet 5middot11 of 46
f
No 8 Date Revision Code 2831 No C3 1052 Amiddot163 1middottVOl Rev 0
i (
II Technical amp Calculation Data Sheet SARASIN-Agt Zllloa-R~
Safety Valve Nt BiOPUIle Gt1wtI bull bull 2110 1-1_
IN I ICustomer Name TECHNIP FRANCE
891 I 4 I bull s~ I
Cuslllem Numb 7273F RFQ 1545-01
Project KHARG OLEFIN COMPLEX I Opened
I 1 I
Quote Ref Tag No PSV pound I Nde Sales Abdeljalill Baigar I
I I uperatIng onaltons
Fluid ~e Superheated Steam 19 tnle ON shy
capaci ty 78500 Kgn 20 Inlet Finish ANSI 600 RF (125-250 AARH)
3 Set presMKC 21 Outlet ON
4935 bar eM 22 OtItlet Finish ANSI 150 RF (125-250 AARH)
DiSCharge Temp 375 middotC ASME B16-5 5 Variable back presslJe bull bar eft
Cold dilf lesc press 4935 bar eft I Bill 01 I
OverptesslKe B() 10 Bod SAl16 wee a Operating ProsslKe bar elf 24 Yoke SA216 wee
25 cabull SA216 weebull bull Tlglt Closing presSlKe (MAOP) 44 415 bar eff 26 Nozzle Sellited AlSI410 bullMlaquohBnIcaI Temp J15 C 21 Disc 174 PH Stilinless Steel 28 Gaskets Stainless $t1 bullSDOM Chromium Alloy Steel 30 Golde AlSI431 31 AcluslthQRinP SAl51 CF3M 32 Stud A183flr81 33 Nul Al94gr2H
gt0 Revulr Lever
Reqllif~ Afea 32023 om 35 middot SlelUted noule
12 496 sq in TU I Gag
1 Sellcl(l(l AIel 41 2 om
I 839 sq in Orirooe p
I ReactIon loree 3016 D I Flow capacity 100996 KgIh
I Noise ill 30 m ace to AP152 1 126 dB approxmate noise level at 30 m aCCOfding to APl521 (mtluth noise) open discharge
II 37 j API52 I I I
Commercial code S46P3530A-D-VMM I
IA= 525 PlKd~Kn KbKsh I I~-middot 2254 mm 2540 mm
11800 mm
bull 1523 Kg
lA shy 89 InCh
Dab 01 COI lcul I ~ - 100 Inch
IH- 465 Inch -jshyMa55 Capaoty W 18500 KgIh 3351 Pound -IP I 553 barabs C C-ase Constant 341143 I () Indicative Values 0 now coeffiCIent Kd 09150
N Ksh 0866 w- Napier equation coffeclion Kn bull 2 valves afe necessary to reach the required capacity lt Back Pfessure correcllon Kb
BUIItmiddotup back pressurecO 1 barg 2nd Ialve set at 05 of set pranure with 10 olelpreSSure in accordill1Ce With API 520
bullbulliii
bull 11 Load cases Ioad case combinations
The following load cases f load case combinations shall be analyzed 1) always or 2) on a casemiddot to-case basis
Static load cases for operating design and pressure test conditions
L6 jillL7 I
I --shy
I --shyI I I I I
L L
I Ll 9 L20
bull ~--
Load types (iC a pplicable load types should be added) W Dead weight (pipe weight + fluid weight + insulation weight) D Displacement T Design temperature P Design internal pressure U Uniform loads (eg snow load seismic load) F External forces (forces andor moments) HP Hydro test pressure H Hanger loads WIN Wind loads (for the main wind directions) WNC Dead weight without contents (pipe weight + insulation weight) WW Water-filled weight for pressure test
bull bull bull
bull
bull ~-
rmiddot
bull
bull
Technip
KHARG ETHYLENE PLANT KHARG Olefin Complex
Setup File (
CONNECT_GEOMETRY _ THRU_CNODES
WRC-07 VERSION
WRC- 07
DEFAULT
831
WI I middot AIlaquo) Amiddot KHARGJUOAD CASFsOdoc
T
F
YES
NO
181 281
NO
DEFAULT
02206272E+OSbull
bullbull
bull
bull
Thchnip bull
KHARG ETHYLENE PLANT ~ KHARG Olefin Complex
PFffiOCHEMICAL INO bull DEVELOPMENT MANAG ~ENTCO_
CONTRACTOR DOCUMENT Ndeg OWNER DOCUMENT N
Proioct Ndeg Unit Doc TIIDEII Material Code Serial Ndeg Rev I Paae Proiect N Unit Doc Type Material Code Serial N A~ 7273F I 000 I WI I 1300 I 000 I a I 13 13 I 1313
FRP Ratio GmodlEmo(Uaxial) O2500000E+OO
FRP EalEhVhla O1527272E+OO
SetuD File (CAESARCFG Continuation)
FRP Lamina1e Type THREE
FRP Alpha O2159827E+02 C
FRP Density O1660800E+04 kocum bullEXCLUDE 12 FROM UKOOA BENDI NG NO
OUTPUT REPORTS BY LOAD CASE YES
DISPLACEMENT NODAL SORTING YES
DYNAMIC INPUT EXAMPLE TEXT MAX
TIME HIST ANIMATE YES
ENABLE AUTOSAVE YES
AUTOSAVE TIME INTERVAL O3000000E+02
PROMPTED AUTOSAVE YES
DISABLE UNDOREDO NO
STRUCTURAL DATABASE AISC89BIN
VALVE amp FLANGE GENERIC VHD
EXPANSION JT DBASE FLEXPATHJHD
PI PING SIZE SPECIFICATION ANSI
DEFAULT SPRING HANGER TABLE O5000000E+01
SYSTEM DIRECTORY NAME SYSTEM
UNITS FILE NAME 7273FFIL
ENABLE ODBC OUTPUT NO
DEFAULT SPRING HANGER TABLE LlSEGA
- bull -
WI 1 ANG bull IV IlHAAG_IELOAD CAS ES_OdOC
SRMPL6 LOf]) C(15euro5 S V REfK Ti O-l FOeC e- JlUE TO PSv oPttvlNG
bull Sldlle Aymmiddot [CIDO(UMpoundNTS AllD SETIINGSVhBACONI7173FmiddotMBACONICAESAR FILESICNj016_REV ~
bull
bull
bull
Edt
+ t
loadCose Edlcr LoadCoseOptiom Loads WlNeLoads
loads Oefned n IrtJIA loed Casu Stress Type
W -Woltllt L1 W+D1 +T1 +P1 +H Of 01 middot Displcmnt Case ~ L2 wO-iT2+P1 +H-- Of T1 middot Thermal Case tn l3 W~D1~T3~P1H ~(]S-oiit~~ Of LltgtOd e T2 Thermal Case 2 -- - _- ------- -__- T3 Thermal Case U3
l4 W+P1+H SUS __ _- -----PI middot Pr euUle Case 1 LS Wt-P1t-H-t-F1 OCC Hp middot Hydlo Prenae L6 Ul OCC --- ---- _----- H middot Hanger l oads 17 U2 OCC UI middot Unf Load eMe 11 La U3 OCC U2 -UriloodlAse 12 L9 F1 OCC U3 Uri l oad Case 13 L10 L1-l4 EXP F1 middot Cone FOIct Case 11 1 Ll1 L2-l4 J EXP Vlllet Fled W WNC middot W~ no corieris L12 L3-lS EXP
L13 LS+l7+l8 OCC L1 4 L-4+l13 ----l ~~ IL15 L1 lt-l1 3 L1 6 LJl9 (fD lO(ll ch 011 (f~tnlh OCC
STATIQUE LoR)) I- Ill
1
FW FRANCE NDG SHT16F I
CliENT
PROJECT
CPNo
EXXON
18KTA E5000 Expansion
CALCNo ISV 3310
CALC BY BEP
CHKD BY
DATE 13012006
RELIEF VALVE LOADINGS vapour
RV Nos ISV 3310
SIZE 4x3
RATING 150xlSO
ORIFICE L
bull DATA DESCRIPTION
RV SET PRESSURE
PERCENT OVERPRESSURE
Ps (l+PolOO) + 147
REliEF TEMPERATURE
1195492
RATIO OF SPECIFIC HEATS SIZING FLOW
SElECTED ORIFICE AREA
CALCULATED ORIFICE AREA
FACTORED SIZING flOW
MAX No OF WORKING VALVES
SIZING flOW PER VALVE
113600
MOLECULAR WEIGHT
GAS CONSTANT 1544M
SYMBOl UNITS
Ps BARG
Po
P PSIA T1 DegC
T Oeg R
k WI Kg h A sqin Ac sqin W2 Kgh N
W Ib h w Ibsec M
R ftlblb Oeg
bull GRAVITY IQ ftS2
FI=
2 W RI
gPA
VALUE
7 10 F2
12635 256
9528 105
- shyFl
t~ --+
~ middotFI FI
t5489 rTABIJSmn Ow COiiOmON
2853 NOn IIQRIZOllTAL IOItCIS Kt MtA CEil
2853 15489 F2
1 341532 +shy948701 F3
885 174463 ltV AT POICONllIll0N
322 AampUMING IMPACT CTOII OYl
260496 Ib 1159 N
128894 Ib 573 N
520993 Ib 2318 N -
bullbull
SARASIN-lltJ l7Technical amp Calculation Data Sheet ZI 8olto R~62IKI _____ J40 11ap11M GnlCMl
VAlVH e COlTllOlS Safety Valve
e Bomel lype Opened
Project KHARG OLEfiN COMPLEX ~A
Tag No PSV 6 453A C-Quote Ref 3A30880IOOO Sales Engineer Abdeljalill Baigar W de Commande
Operating ondl tlons Connect ons
19 InlelON shy1 fluid type Superheated Stetlm
20 Inlet Finish ANSt600 RF (125-250 AARH) 2 Capacity 78500 Kglh 21 Outlet DN J Set ptesSUe br eft 22 Outlet Finish ANSI 150 ftF 1125-250 AARH) Ol$charoe Tom p J7S C Accordinn 10 ASME 616-5
5 Variable bad pressure 0 bar eft
Cold (If lest lXess 47 bar eft 8111 of material 7 Overpressure 11 () 16 floltfv SA216 wee
SA2115WCC2 Ylt8 Operating Pressure 40 bar eft
SA216 wee Tight Closing pressUIe (MAOP) 423 bar eft 26 NoWe Stllited AlSl410 1~ 27 174 PH Stainless SteelMechanical Tomp J7S middotC ~ 28 Gaskets Stalnl St1
29 SPfinQ Chromium Allov Steel 30 AlSI431c31 Adusitina Rlna SA351 CF3M 32 Stud Al1lQrB7 JJ Alt4i1r2H Accessories
Regular Levr 35 51etUted nozzl
ReqUIred Area 31 927 om Test Gag 495 s q InIl Selected Area 41 2 om
I 839 sq in 15 Onfice p
Reaction loroe DN~ t Flow capacity 101299 Kglh 18 Noise at 30 m acc to APt521 120 dB
apprO)flTlate noise level at 30 m according to API521 (mouth noiso) )perl dlsctlarge
Customer Name TECHNIP FRANCE evlslon ~ lion ate
890 4 20-juin-2005
Cust Item Numb 7U3F RFQ 1545-01 a ely a ype pflllg a a ely alve ea1T
I I J7 Standard API 520 I )
Commercial code S46P3530AmiddotDmiddotVMM I shyI Dimensions
A- 2254 mm B- 2540 mm W - 11800 mrnIA 525PlKd~KnKb Kshl ~ Welghl() s 1523 Kg I A- 89 Inch I bullB- 100 Inch
Dati 01 calcul w - 4115 Inch Mass Capaatv W 18500 KgIh Weight( ) 3357 Pound
P1 5553 bar abs r~ C Gase Constant 143843
() Indicative Values 0 now ooeIficient Kd 0915 0
Ksn 0865 Remarks Napier equation correction Kn 1
~ 2 valves are necessary 10 reach the required capacity
Back pressure correcUon Kb 1a BUlHmiddotup back pressureO 1 berg Same calculallO1 heet lor the 1st va lve and the spare one bull
N
~
GENERAl
PEO
PROCESS
CONDITONS
bull DESIGN
DATA
bull MATERIALS
I
OPT IONS
1 T Nu~
2 Service 3 Line NUrMer 4 P amp to Numbef
5 6 Conform to 961231EC 7 Fluid T
8 NJ licable rED Table 9
0 11
12
13
14
15 16
17 19
20 21 22
PED Cal
Fluid Fluid Servlc Required Capaci
MoltcullWe hI
ratln PrtSi ur
tlll TIm tUri
Badlt Prl$IIure
AJlovtabie Ova sure
Ov esslI10 FactOI Com esslbU Latenl Heal 01 V lion
o Tl 1012812005 Pour Commenta ires
Equipment
Fluid Groo
Fluid S~I
5 cltle Gl1Ivl Set Pressure
Col
HC+H20
15489
5 02
ReHov Temperatlyene 212
Constant Varia1je Total
23 Specific Hnt RItIo lC 24 Relief Densi
25 Relief Viscosity
26 Barometric Pressure 27 28 Nozzle Flit Semi
29 Design Saely Reflef Sale -Relief 30 Type Conventional BelloIN Plot Opefatad 31 BonnetT 32 n Code
33 Sizing Basis 34 Calcula ted Area
35 Selected Area 36 Orifice De nation
37 Size Rating -Inlel 38 Size Rat - Outlet
39 40 41 42 43 Stt 44 Fla es
45 Resilient Seat Seal 46 Guide
471 Spfing 46 Wtted Material
49 50
Bonnt Disc
Ri s Bellows
51 Cap Screwed or Bolted 52 Lever Plain or Packed 53 TestGag
54 55
22-ISV 3310 0 331fD332 SHCOO20150A1A 1 l -Q2S)(l2
y Gaseous Group 1
0 1
0
09
105
4
Note 10
k
C
k p
Safety Corrventlonal
hI Solted
ASME Delaut eau de refroldissement
1812 em
L 3 150 RF 450 RF
A2 16 WCB
NOlet A216WCB
NOle 1
Note 1
NOIot
NOIel
(Note 1
No
No
INSTRUMENT SPECIFICATION
Valve Safety Pressure Relief
oxicFlammable
GasIVapo
7
2564 C
A21 6WCB SS 316 Mini
Note 1
EJflt0nMobil Chemic
Sheet 5middot11 of 46
f
No 8 Date Revision Code 2831 No C3 1052 Amiddot163 1middottVOl Rev 0
i (
II Technical amp Calculation Data Sheet SARASIN-Agt Zllloa-R~
Safety Valve Nt BiOPUIle Gt1wtI bull bull 2110 1-1_
IN I ICustomer Name TECHNIP FRANCE
891 I 4 I bull s~ I
Cuslllem Numb 7273F RFQ 1545-01
Project KHARG OLEFIN COMPLEX I Opened
I 1 I
Quote Ref Tag No PSV pound I Nde Sales Abdeljalill Baigar I
I I uperatIng onaltons
Fluid ~e Superheated Steam 19 tnle ON shy
capaci ty 78500 Kgn 20 Inlet Finish ANSI 600 RF (125-250 AARH)
3 Set presMKC 21 Outlet ON
4935 bar eM 22 OtItlet Finish ANSI 150 RF (125-250 AARH)
DiSCharge Temp 375 middotC ASME B16-5 5 Variable back presslJe bull bar eft
Cold dilf lesc press 4935 bar eft I Bill 01 I
OverptesslKe B() 10 Bod SAl16 wee a Operating ProsslKe bar elf 24 Yoke SA216 wee
25 cabull SA216 weebull bull Tlglt Closing presSlKe (MAOP) 44 415 bar eff 26 Nozzle Sellited AlSI410 bullMlaquohBnIcaI Temp J15 C 21 Disc 174 PH Stilinless Steel 28 Gaskets Stainless $t1 bullSDOM Chromium Alloy Steel 30 Golde AlSI431 31 AcluslthQRinP SAl51 CF3M 32 Stud A183flr81 33 Nul Al94gr2H
gt0 Revulr Lever
Reqllif~ Afea 32023 om 35 middot SlelUted noule
12 496 sq in TU I Gag
1 Sellcl(l(l AIel 41 2 om
I 839 sq in Orirooe p
I ReactIon loree 3016 D I Flow capacity 100996 KgIh
I Noise ill 30 m ace to AP152 1 126 dB approxmate noise level at 30 m aCCOfding to APl521 (mtluth noise) open discharge
II 37 j API52 I I I
Commercial code S46P3530A-D-VMM I
IA= 525 PlKd~Kn KbKsh I I~-middot 2254 mm 2540 mm
11800 mm
bull 1523 Kg
lA shy 89 InCh
Dab 01 COI lcul I ~ - 100 Inch
IH- 465 Inch -jshyMa55 Capaoty W 18500 KgIh 3351 Pound -IP I 553 barabs C C-ase Constant 341143 I () Indicative Values 0 now coeffiCIent Kd 09150
N Ksh 0866 w- Napier equation coffeclion Kn bull 2 valves afe necessary to reach the required capacity lt Back Pfessure correcllon Kb
BUIItmiddotup back pressurecO 1 barg 2nd Ialve set at 05 of set pranure with 10 olelpreSSure in accordill1Ce With API 520
bullbulliii
bull 11 Load cases Ioad case combinations
The following load cases f load case combinations shall be analyzed 1) always or 2) on a casemiddot to-case basis
Static load cases for operating design and pressure test conditions
L6 jillL7 I
I --shy
I --shyI I I I I
L L
I Ll 9 L20
bull ~--
Load types (iC a pplicable load types should be added) W Dead weight (pipe weight + fluid weight + insulation weight) D Displacement T Design temperature P Design internal pressure U Uniform loads (eg snow load seismic load) F External forces (forces andor moments) HP Hydro test pressure H Hanger loads WIN Wind loads (for the main wind directions) WNC Dead weight without contents (pipe weight + insulation weight) WW Water-filled weight for pressure test
bull bull bull
bull
bull ~-
bullbull
bull
bull
Thchnip bull
KHARG ETHYLENE PLANT ~ KHARG Olefin Complex
PFffiOCHEMICAL INO bull DEVELOPMENT MANAG ~ENTCO_
CONTRACTOR DOCUMENT Ndeg OWNER DOCUMENT N
Proioct Ndeg Unit Doc TIIDEII Material Code Serial Ndeg Rev I Paae Proiect N Unit Doc Type Material Code Serial N A~ 7273F I 000 I WI I 1300 I 000 I a I 13 13 I 1313
FRP Ratio GmodlEmo(Uaxial) O2500000E+OO
FRP EalEhVhla O1527272E+OO
SetuD File (CAESARCFG Continuation)
FRP Lamina1e Type THREE
FRP Alpha O2159827E+02 C
FRP Density O1660800E+04 kocum bullEXCLUDE 12 FROM UKOOA BENDI NG NO
OUTPUT REPORTS BY LOAD CASE YES
DISPLACEMENT NODAL SORTING YES
DYNAMIC INPUT EXAMPLE TEXT MAX
TIME HIST ANIMATE YES
ENABLE AUTOSAVE YES
AUTOSAVE TIME INTERVAL O3000000E+02
PROMPTED AUTOSAVE YES
DISABLE UNDOREDO NO
STRUCTURAL DATABASE AISC89BIN
VALVE amp FLANGE GENERIC VHD
EXPANSION JT DBASE FLEXPATHJHD
PI PING SIZE SPECIFICATION ANSI
DEFAULT SPRING HANGER TABLE O5000000E+01
SYSTEM DIRECTORY NAME SYSTEM
UNITS FILE NAME 7273FFIL
ENABLE ODBC OUTPUT NO
DEFAULT SPRING HANGER TABLE LlSEGA
- bull -
WI 1 ANG bull IV IlHAAG_IELOAD CAS ES_OdOC
SRMPL6 LOf]) C(15euro5 S V REfK Ti O-l FOeC e- JlUE TO PSv oPttvlNG
bull Sldlle Aymmiddot [CIDO(UMpoundNTS AllD SETIINGSVhBACONI7173FmiddotMBACONICAESAR FILESICNj016_REV ~
bull
bull
bull
Edt
+ t
loadCose Edlcr LoadCoseOptiom Loads WlNeLoads
loads Oefned n IrtJIA loed Casu Stress Type
W -Woltllt L1 W+D1 +T1 +P1 +H Of 01 middot Displcmnt Case ~ L2 wO-iT2+P1 +H-- Of T1 middot Thermal Case tn l3 W~D1~T3~P1H ~(]S-oiit~~ Of LltgtOd e T2 Thermal Case 2 -- - _- ------- -__- T3 Thermal Case U3
l4 W+P1+H SUS __ _- -----PI middot Pr euUle Case 1 LS Wt-P1t-H-t-F1 OCC Hp middot Hydlo Prenae L6 Ul OCC --- ---- _----- H middot Hanger l oads 17 U2 OCC UI middot Unf Load eMe 11 La U3 OCC U2 -UriloodlAse 12 L9 F1 OCC U3 Uri l oad Case 13 L10 L1-l4 EXP F1 middot Cone FOIct Case 11 1 Ll1 L2-l4 J EXP Vlllet Fled W WNC middot W~ no corieris L12 L3-lS EXP
L13 LS+l7+l8 OCC L1 4 L-4+l13 ----l ~~ IL15 L1 lt-l1 3 L1 6 LJl9 (fD lO(ll ch 011 (f~tnlh OCC
STATIQUE LoR)) I- Ill
1
FW FRANCE NDG SHT16F I
CliENT
PROJECT
CPNo
EXXON
18KTA E5000 Expansion
CALCNo ISV 3310
CALC BY BEP
CHKD BY
DATE 13012006
RELIEF VALVE LOADINGS vapour
RV Nos ISV 3310
SIZE 4x3
RATING 150xlSO
ORIFICE L
bull DATA DESCRIPTION
RV SET PRESSURE
PERCENT OVERPRESSURE
Ps (l+PolOO) + 147
REliEF TEMPERATURE
1195492
RATIO OF SPECIFIC HEATS SIZING FLOW
SElECTED ORIFICE AREA
CALCULATED ORIFICE AREA
FACTORED SIZING flOW
MAX No OF WORKING VALVES
SIZING flOW PER VALVE
113600
MOLECULAR WEIGHT
GAS CONSTANT 1544M
SYMBOl UNITS
Ps BARG
Po
P PSIA T1 DegC
T Oeg R
k WI Kg h A sqin Ac sqin W2 Kgh N
W Ib h w Ibsec M
R ftlblb Oeg
bull GRAVITY IQ ftS2
FI=
2 W RI
gPA
VALUE
7 10 F2
12635 256
9528 105
- shyFl
t~ --+
~ middotFI FI
t5489 rTABIJSmn Ow COiiOmON
2853 NOn IIQRIZOllTAL IOItCIS Kt MtA CEil
2853 15489 F2
1 341532 +shy948701 F3
885 174463 ltV AT POICONllIll0N
322 AampUMING IMPACT CTOII OYl
260496 Ib 1159 N
128894 Ib 573 N
520993 Ib 2318 N -
bullbull
SARASIN-lltJ l7Technical amp Calculation Data Sheet ZI 8olto R~62IKI _____ J40 11ap11M GnlCMl
VAlVH e COlTllOlS Safety Valve
e Bomel lype Opened
Project KHARG OLEfiN COMPLEX ~A
Tag No PSV 6 453A C-Quote Ref 3A30880IOOO Sales Engineer Abdeljalill Baigar W de Commande
Operating ondl tlons Connect ons
19 InlelON shy1 fluid type Superheated Stetlm
20 Inlet Finish ANSt600 RF (125-250 AARH) 2 Capacity 78500 Kglh 21 Outlet DN J Set ptesSUe br eft 22 Outlet Finish ANSI 150 ftF 1125-250 AARH) Ol$charoe Tom p J7S C Accordinn 10 ASME 616-5
5 Variable bad pressure 0 bar eft
Cold (If lest lXess 47 bar eft 8111 of material 7 Overpressure 11 () 16 floltfv SA216 wee
SA2115WCC2 Ylt8 Operating Pressure 40 bar eft
SA216 wee Tight Closing pressUIe (MAOP) 423 bar eft 26 NoWe Stllited AlSl410 1~ 27 174 PH Stainless SteelMechanical Tomp J7S middotC ~ 28 Gaskets Stalnl St1
29 SPfinQ Chromium Allov Steel 30 AlSI431c31 Adusitina Rlna SA351 CF3M 32 Stud Al1lQrB7 JJ Alt4i1r2H Accessories
Regular Levr 35 51etUted nozzl
ReqUIred Area 31 927 om Test Gag 495 s q InIl Selected Area 41 2 om
I 839 sq in 15 Onfice p
Reaction loroe DN~ t Flow capacity 101299 Kglh 18 Noise at 30 m acc to APt521 120 dB
apprO)flTlate noise level at 30 m according to API521 (mouth noiso) )perl dlsctlarge
Customer Name TECHNIP FRANCE evlslon ~ lion ate
890 4 20-juin-2005
Cust Item Numb 7U3F RFQ 1545-01 a ely a ype pflllg a a ely alve ea1T
I I J7 Standard API 520 I )
Commercial code S46P3530AmiddotDmiddotVMM I shyI Dimensions
A- 2254 mm B- 2540 mm W - 11800 mrnIA 525PlKd~KnKb Kshl ~ Welghl() s 1523 Kg I A- 89 Inch I bullB- 100 Inch
Dati 01 calcul w - 4115 Inch Mass Capaatv W 18500 KgIh Weight( ) 3357 Pound
P1 5553 bar abs r~ C Gase Constant 143843
() Indicative Values 0 now ooeIficient Kd 0915 0
Ksn 0865 Remarks Napier equation correction Kn 1
~ 2 valves are necessary 10 reach the required capacity
Back pressure correcUon Kb 1a BUlHmiddotup back pressureO 1 berg Same calculallO1 heet lor the 1st va lve and the spare one bull
N
~
GENERAl
PEO
PROCESS
CONDITONS
bull DESIGN
DATA
bull MATERIALS
I
OPT IONS
1 T Nu~
2 Service 3 Line NUrMer 4 P amp to Numbef
5 6 Conform to 961231EC 7 Fluid T
8 NJ licable rED Table 9
0 11
12
13
14
15 16
17 19
20 21 22
PED Cal
Fluid Fluid Servlc Required Capaci
MoltcullWe hI
ratln PrtSi ur
tlll TIm tUri
Badlt Prl$IIure
AJlovtabie Ova sure
Ov esslI10 FactOI Com esslbU Latenl Heal 01 V lion
o Tl 1012812005 Pour Commenta ires
Equipment
Fluid Groo
Fluid S~I
5 cltle Gl1Ivl Set Pressure
Col
HC+H20
15489
5 02
ReHov Temperatlyene 212
Constant Varia1je Total
23 Specific Hnt RItIo lC 24 Relief Densi
25 Relief Viscosity
26 Barometric Pressure 27 28 Nozzle Flit Semi
29 Design Saely Reflef Sale -Relief 30 Type Conventional BelloIN Plot Opefatad 31 BonnetT 32 n Code
33 Sizing Basis 34 Calcula ted Area
35 Selected Area 36 Orifice De nation
37 Size Rating -Inlel 38 Size Rat - Outlet
39 40 41 42 43 Stt 44 Fla es
45 Resilient Seat Seal 46 Guide
471 Spfing 46 Wtted Material
49 50
Bonnt Disc
Ri s Bellows
51 Cap Screwed or Bolted 52 Lever Plain or Packed 53 TestGag
54 55
22-ISV 3310 0 331fD332 SHCOO20150A1A 1 l -Q2S)(l2
y Gaseous Group 1
0 1
0
09
105
4
Note 10
k
C
k p
Safety Corrventlonal
hI Solted
ASME Delaut eau de refroldissement
1812 em
L 3 150 RF 450 RF
A2 16 WCB
NOlet A216WCB
NOle 1
Note 1
NOIot
NOIel
(Note 1
No
No
INSTRUMENT SPECIFICATION
Valve Safety Pressure Relief
oxicFlammable
GasIVapo
7
2564 C
A21 6WCB SS 316 Mini
Note 1
EJflt0nMobil Chemic
Sheet 5middot11 of 46
f
No 8 Date Revision Code 2831 No C3 1052 Amiddot163 1middottVOl Rev 0
i (
II Technical amp Calculation Data Sheet SARASIN-Agt Zllloa-R~
Safety Valve Nt BiOPUIle Gt1wtI bull bull 2110 1-1_
IN I ICustomer Name TECHNIP FRANCE
891 I 4 I bull s~ I
Cuslllem Numb 7273F RFQ 1545-01
Project KHARG OLEFIN COMPLEX I Opened
I 1 I
Quote Ref Tag No PSV pound I Nde Sales Abdeljalill Baigar I
I I uperatIng onaltons
Fluid ~e Superheated Steam 19 tnle ON shy
capaci ty 78500 Kgn 20 Inlet Finish ANSI 600 RF (125-250 AARH)
3 Set presMKC 21 Outlet ON
4935 bar eM 22 OtItlet Finish ANSI 150 RF (125-250 AARH)
DiSCharge Temp 375 middotC ASME B16-5 5 Variable back presslJe bull bar eft
Cold dilf lesc press 4935 bar eft I Bill 01 I
OverptesslKe B() 10 Bod SAl16 wee a Operating ProsslKe bar elf 24 Yoke SA216 wee
25 cabull SA216 weebull bull Tlglt Closing presSlKe (MAOP) 44 415 bar eff 26 Nozzle Sellited AlSI410 bullMlaquohBnIcaI Temp J15 C 21 Disc 174 PH Stilinless Steel 28 Gaskets Stainless $t1 bullSDOM Chromium Alloy Steel 30 Golde AlSI431 31 AcluslthQRinP SAl51 CF3M 32 Stud A183flr81 33 Nul Al94gr2H
gt0 Revulr Lever
Reqllif~ Afea 32023 om 35 middot SlelUted noule
12 496 sq in TU I Gag
1 Sellcl(l(l AIel 41 2 om
I 839 sq in Orirooe p
I ReactIon loree 3016 D I Flow capacity 100996 KgIh
I Noise ill 30 m ace to AP152 1 126 dB approxmate noise level at 30 m aCCOfding to APl521 (mtluth noise) open discharge
II 37 j API52 I I I
Commercial code S46P3530A-D-VMM I
IA= 525 PlKd~Kn KbKsh I I~-middot 2254 mm 2540 mm
11800 mm
bull 1523 Kg
lA shy 89 InCh
Dab 01 COI lcul I ~ - 100 Inch
IH- 465 Inch -jshyMa55 Capaoty W 18500 KgIh 3351 Pound -IP I 553 barabs C C-ase Constant 341143 I () Indicative Values 0 now coeffiCIent Kd 09150
N Ksh 0866 w- Napier equation coffeclion Kn bull 2 valves afe necessary to reach the required capacity lt Back Pfessure correcllon Kb
BUIItmiddotup back pressurecO 1 barg 2nd Ialve set at 05 of set pranure with 10 olelpreSSure in accordill1Ce With API 520
bullbulliii
bull 11 Load cases Ioad case combinations
The following load cases f load case combinations shall be analyzed 1) always or 2) on a casemiddot to-case basis
Static load cases for operating design and pressure test conditions
L6 jillL7 I
I --shy
I --shyI I I I I
L L
I Ll 9 L20
bull ~--
Load types (iC a pplicable load types should be added) W Dead weight (pipe weight + fluid weight + insulation weight) D Displacement T Design temperature P Design internal pressure U Uniform loads (eg snow load seismic load) F External forces (forces andor moments) HP Hydro test pressure H Hanger loads WIN Wind loads (for the main wind directions) WNC Dead weight without contents (pipe weight + insulation weight) WW Water-filled weight for pressure test
bull bull bull
bull
bull ~-
SRMPL6 LOf]) C(15euro5 S V REfK Ti O-l FOeC e- JlUE TO PSv oPttvlNG
bull Sldlle Aymmiddot [CIDO(UMpoundNTS AllD SETIINGSVhBACONI7173FmiddotMBACONICAESAR FILESICNj016_REV ~
bull
bull
bull
Edt
+ t
loadCose Edlcr LoadCoseOptiom Loads WlNeLoads
loads Oefned n IrtJIA loed Casu Stress Type
W -Woltllt L1 W+D1 +T1 +P1 +H Of 01 middot Displcmnt Case ~ L2 wO-iT2+P1 +H-- Of T1 middot Thermal Case tn l3 W~D1~T3~P1H ~(]S-oiit~~ Of LltgtOd e T2 Thermal Case 2 -- - _- ------- -__- T3 Thermal Case U3
l4 W+P1+H SUS __ _- -----PI middot Pr euUle Case 1 LS Wt-P1t-H-t-F1 OCC Hp middot Hydlo Prenae L6 Ul OCC --- ---- _----- H middot Hanger l oads 17 U2 OCC UI middot Unf Load eMe 11 La U3 OCC U2 -UriloodlAse 12 L9 F1 OCC U3 Uri l oad Case 13 L10 L1-l4 EXP F1 middot Cone FOIct Case 11 1 Ll1 L2-l4 J EXP Vlllet Fled W WNC middot W~ no corieris L12 L3-lS EXP
L13 LS+l7+l8 OCC L1 4 L-4+l13 ----l ~~ IL15 L1 lt-l1 3 L1 6 LJl9 (fD lO(ll ch 011 (f~tnlh OCC
STATIQUE LoR)) I- Ill
1
FW FRANCE NDG SHT16F I
CliENT
PROJECT
CPNo
EXXON
18KTA E5000 Expansion
CALCNo ISV 3310
CALC BY BEP
CHKD BY
DATE 13012006
RELIEF VALVE LOADINGS vapour
RV Nos ISV 3310
SIZE 4x3
RATING 150xlSO
ORIFICE L
bull DATA DESCRIPTION
RV SET PRESSURE
PERCENT OVERPRESSURE
Ps (l+PolOO) + 147
REliEF TEMPERATURE
1195492
RATIO OF SPECIFIC HEATS SIZING FLOW
SElECTED ORIFICE AREA
CALCULATED ORIFICE AREA
FACTORED SIZING flOW
MAX No OF WORKING VALVES
SIZING flOW PER VALVE
113600
MOLECULAR WEIGHT
GAS CONSTANT 1544M
SYMBOl UNITS
Ps BARG
Po
P PSIA T1 DegC
T Oeg R
k WI Kg h A sqin Ac sqin W2 Kgh N
W Ib h w Ibsec M
R ftlblb Oeg
bull GRAVITY IQ ftS2
FI=
2 W RI
gPA
VALUE
7 10 F2
12635 256
9528 105
- shyFl
t~ --+
~ middotFI FI
t5489 rTABIJSmn Ow COiiOmON
2853 NOn IIQRIZOllTAL IOItCIS Kt MtA CEil
2853 15489 F2
1 341532 +shy948701 F3
885 174463 ltV AT POICONllIll0N
322 AampUMING IMPACT CTOII OYl
260496 Ib 1159 N
128894 Ib 573 N
520993 Ib 2318 N -
bullbull
SARASIN-lltJ l7Technical amp Calculation Data Sheet ZI 8olto R~62IKI _____ J40 11ap11M GnlCMl
VAlVH e COlTllOlS Safety Valve
e Bomel lype Opened
Project KHARG OLEfiN COMPLEX ~A
Tag No PSV 6 453A C-Quote Ref 3A30880IOOO Sales Engineer Abdeljalill Baigar W de Commande
Operating ondl tlons Connect ons
19 InlelON shy1 fluid type Superheated Stetlm
20 Inlet Finish ANSt600 RF (125-250 AARH) 2 Capacity 78500 Kglh 21 Outlet DN J Set ptesSUe br eft 22 Outlet Finish ANSI 150 ftF 1125-250 AARH) Ol$charoe Tom p J7S C Accordinn 10 ASME 616-5
5 Variable bad pressure 0 bar eft
Cold (If lest lXess 47 bar eft 8111 of material 7 Overpressure 11 () 16 floltfv SA216 wee
SA2115WCC2 Ylt8 Operating Pressure 40 bar eft
SA216 wee Tight Closing pressUIe (MAOP) 423 bar eft 26 NoWe Stllited AlSl410 1~ 27 174 PH Stainless SteelMechanical Tomp J7S middotC ~ 28 Gaskets Stalnl St1
29 SPfinQ Chromium Allov Steel 30 AlSI431c31 Adusitina Rlna SA351 CF3M 32 Stud Al1lQrB7 JJ Alt4i1r2H Accessories
Regular Levr 35 51etUted nozzl
ReqUIred Area 31 927 om Test Gag 495 s q InIl Selected Area 41 2 om
I 839 sq in 15 Onfice p
Reaction loroe DN~ t Flow capacity 101299 Kglh 18 Noise at 30 m acc to APt521 120 dB
apprO)flTlate noise level at 30 m according to API521 (mouth noiso) )perl dlsctlarge
Customer Name TECHNIP FRANCE evlslon ~ lion ate
890 4 20-juin-2005
Cust Item Numb 7U3F RFQ 1545-01 a ely a ype pflllg a a ely alve ea1T
I I J7 Standard API 520 I )
Commercial code S46P3530AmiddotDmiddotVMM I shyI Dimensions
A- 2254 mm B- 2540 mm W - 11800 mrnIA 525PlKd~KnKb Kshl ~ Welghl() s 1523 Kg I A- 89 Inch I bullB- 100 Inch
Dati 01 calcul w - 4115 Inch Mass Capaatv W 18500 KgIh Weight( ) 3357 Pound
P1 5553 bar abs r~ C Gase Constant 143843
() Indicative Values 0 now ooeIficient Kd 0915 0
Ksn 0865 Remarks Napier equation correction Kn 1
~ 2 valves are necessary 10 reach the required capacity
Back pressure correcUon Kb 1a BUlHmiddotup back pressureO 1 berg Same calculallO1 heet lor the 1st va lve and the spare one bull
N
~
GENERAl
PEO
PROCESS
CONDITONS
bull DESIGN
DATA
bull MATERIALS
I
OPT IONS
1 T Nu~
2 Service 3 Line NUrMer 4 P amp to Numbef
5 6 Conform to 961231EC 7 Fluid T
8 NJ licable rED Table 9
0 11
12
13
14
15 16
17 19
20 21 22
PED Cal
Fluid Fluid Servlc Required Capaci
MoltcullWe hI
ratln PrtSi ur
tlll TIm tUri
Badlt Prl$IIure
AJlovtabie Ova sure
Ov esslI10 FactOI Com esslbU Latenl Heal 01 V lion
o Tl 1012812005 Pour Commenta ires
Equipment
Fluid Groo
Fluid S~I
5 cltle Gl1Ivl Set Pressure
Col
HC+H20
15489
5 02
ReHov Temperatlyene 212
Constant Varia1je Total
23 Specific Hnt RItIo lC 24 Relief Densi
25 Relief Viscosity
26 Barometric Pressure 27 28 Nozzle Flit Semi
29 Design Saely Reflef Sale -Relief 30 Type Conventional BelloIN Plot Opefatad 31 BonnetT 32 n Code
33 Sizing Basis 34 Calcula ted Area
35 Selected Area 36 Orifice De nation
37 Size Rating -Inlel 38 Size Rat - Outlet
39 40 41 42 43 Stt 44 Fla es
45 Resilient Seat Seal 46 Guide
471 Spfing 46 Wtted Material
49 50
Bonnt Disc
Ri s Bellows
51 Cap Screwed or Bolted 52 Lever Plain or Packed 53 TestGag
54 55
22-ISV 3310 0 331fD332 SHCOO20150A1A 1 l -Q2S)(l2
y Gaseous Group 1
0 1
0
09
105
4
Note 10
k
C
k p
Safety Corrventlonal
hI Solted
ASME Delaut eau de refroldissement
1812 em
L 3 150 RF 450 RF
A2 16 WCB
NOlet A216WCB
NOle 1
Note 1
NOIot
NOIel
(Note 1
No
No
INSTRUMENT SPECIFICATION
Valve Safety Pressure Relief
oxicFlammable
GasIVapo
7
2564 C
A21 6WCB SS 316 Mini
Note 1
EJflt0nMobil Chemic
Sheet 5middot11 of 46
f
No 8 Date Revision Code 2831 No C3 1052 Amiddot163 1middottVOl Rev 0
i (
II Technical amp Calculation Data Sheet SARASIN-Agt Zllloa-R~
Safety Valve Nt BiOPUIle Gt1wtI bull bull 2110 1-1_
IN I ICustomer Name TECHNIP FRANCE
891 I 4 I bull s~ I
Cuslllem Numb 7273F RFQ 1545-01
Project KHARG OLEFIN COMPLEX I Opened
I 1 I
Quote Ref Tag No PSV pound I Nde Sales Abdeljalill Baigar I
I I uperatIng onaltons
Fluid ~e Superheated Steam 19 tnle ON shy
capaci ty 78500 Kgn 20 Inlet Finish ANSI 600 RF (125-250 AARH)
3 Set presMKC 21 Outlet ON
4935 bar eM 22 OtItlet Finish ANSI 150 RF (125-250 AARH)
DiSCharge Temp 375 middotC ASME B16-5 5 Variable back presslJe bull bar eft
Cold dilf lesc press 4935 bar eft I Bill 01 I
OverptesslKe B() 10 Bod SAl16 wee a Operating ProsslKe bar elf 24 Yoke SA216 wee
25 cabull SA216 weebull bull Tlglt Closing presSlKe (MAOP) 44 415 bar eff 26 Nozzle Sellited AlSI410 bullMlaquohBnIcaI Temp J15 C 21 Disc 174 PH Stilinless Steel 28 Gaskets Stainless $t1 bullSDOM Chromium Alloy Steel 30 Golde AlSI431 31 AcluslthQRinP SAl51 CF3M 32 Stud A183flr81 33 Nul Al94gr2H
gt0 Revulr Lever
Reqllif~ Afea 32023 om 35 middot SlelUted noule
12 496 sq in TU I Gag
1 Sellcl(l(l AIel 41 2 om
I 839 sq in Orirooe p
I ReactIon loree 3016 D I Flow capacity 100996 KgIh
I Noise ill 30 m ace to AP152 1 126 dB approxmate noise level at 30 m aCCOfding to APl521 (mtluth noise) open discharge
II 37 j API52 I I I
Commercial code S46P3530A-D-VMM I
IA= 525 PlKd~Kn KbKsh I I~-middot 2254 mm 2540 mm
11800 mm
bull 1523 Kg
lA shy 89 InCh
Dab 01 COI lcul I ~ - 100 Inch
IH- 465 Inch -jshyMa55 Capaoty W 18500 KgIh 3351 Pound -IP I 553 barabs C C-ase Constant 341143 I () Indicative Values 0 now coeffiCIent Kd 09150
N Ksh 0866 w- Napier equation coffeclion Kn bull 2 valves afe necessary to reach the required capacity lt Back Pfessure correcllon Kb
BUIItmiddotup back pressurecO 1 barg 2nd Ialve set at 05 of set pranure with 10 olelpreSSure in accordill1Ce With API 520
bullbulliii
bull 11 Load cases Ioad case combinations
The following load cases f load case combinations shall be analyzed 1) always or 2) on a casemiddot to-case basis
Static load cases for operating design and pressure test conditions
L6 jillL7 I
I --shy
I --shyI I I I I
L L
I Ll 9 L20
bull ~--
Load types (iC a pplicable load types should be added) W Dead weight (pipe weight + fluid weight + insulation weight) D Displacement T Design temperature P Design internal pressure U Uniform loads (eg snow load seismic load) F External forces (forces andor moments) HP Hydro test pressure H Hanger loads WIN Wind loads (for the main wind directions) WNC Dead weight without contents (pipe weight + insulation weight) WW Water-filled weight for pressure test
bull bull bull
bull
bull ~-
1
FW FRANCE NDG SHT16F I
CliENT
PROJECT
CPNo
EXXON
18KTA E5000 Expansion
CALCNo ISV 3310
CALC BY BEP
CHKD BY
DATE 13012006
RELIEF VALVE LOADINGS vapour
RV Nos ISV 3310
SIZE 4x3
RATING 150xlSO
ORIFICE L
bull DATA DESCRIPTION
RV SET PRESSURE
PERCENT OVERPRESSURE
Ps (l+PolOO) + 147
REliEF TEMPERATURE
1195492
RATIO OF SPECIFIC HEATS SIZING FLOW
SElECTED ORIFICE AREA
CALCULATED ORIFICE AREA
FACTORED SIZING flOW
MAX No OF WORKING VALVES
SIZING flOW PER VALVE
113600
MOLECULAR WEIGHT
GAS CONSTANT 1544M
SYMBOl UNITS
Ps BARG
Po
P PSIA T1 DegC
T Oeg R
k WI Kg h A sqin Ac sqin W2 Kgh N
W Ib h w Ibsec M
R ftlblb Oeg
bull GRAVITY IQ ftS2
FI=
2 W RI
gPA
VALUE
7 10 F2
12635 256
9528 105
- shyFl
t~ --+
~ middotFI FI
t5489 rTABIJSmn Ow COiiOmON
2853 NOn IIQRIZOllTAL IOItCIS Kt MtA CEil
2853 15489 F2
1 341532 +shy948701 F3
885 174463 ltV AT POICONllIll0N
322 AampUMING IMPACT CTOII OYl
260496 Ib 1159 N
128894 Ib 573 N
520993 Ib 2318 N -
bullbull
SARASIN-lltJ l7Technical amp Calculation Data Sheet ZI 8olto R~62IKI _____ J40 11ap11M GnlCMl
VAlVH e COlTllOlS Safety Valve
e Bomel lype Opened
Project KHARG OLEfiN COMPLEX ~A
Tag No PSV 6 453A C-Quote Ref 3A30880IOOO Sales Engineer Abdeljalill Baigar W de Commande
Operating ondl tlons Connect ons
19 InlelON shy1 fluid type Superheated Stetlm
20 Inlet Finish ANSt600 RF (125-250 AARH) 2 Capacity 78500 Kglh 21 Outlet DN J Set ptesSUe br eft 22 Outlet Finish ANSI 150 ftF 1125-250 AARH) Ol$charoe Tom p J7S C Accordinn 10 ASME 616-5
5 Variable bad pressure 0 bar eft
Cold (If lest lXess 47 bar eft 8111 of material 7 Overpressure 11 () 16 floltfv SA216 wee
SA2115WCC2 Ylt8 Operating Pressure 40 bar eft
SA216 wee Tight Closing pressUIe (MAOP) 423 bar eft 26 NoWe Stllited AlSl410 1~ 27 174 PH Stainless SteelMechanical Tomp J7S middotC ~ 28 Gaskets Stalnl St1
29 SPfinQ Chromium Allov Steel 30 AlSI431c31 Adusitina Rlna SA351 CF3M 32 Stud Al1lQrB7 JJ Alt4i1r2H Accessories
Regular Levr 35 51etUted nozzl
ReqUIred Area 31 927 om Test Gag 495 s q InIl Selected Area 41 2 om
I 839 sq in 15 Onfice p
Reaction loroe DN~ t Flow capacity 101299 Kglh 18 Noise at 30 m acc to APt521 120 dB
apprO)flTlate noise level at 30 m according to API521 (mouth noiso) )perl dlsctlarge
Customer Name TECHNIP FRANCE evlslon ~ lion ate
890 4 20-juin-2005
Cust Item Numb 7U3F RFQ 1545-01 a ely a ype pflllg a a ely alve ea1T
I I J7 Standard API 520 I )
Commercial code S46P3530AmiddotDmiddotVMM I shyI Dimensions
A- 2254 mm B- 2540 mm W - 11800 mrnIA 525PlKd~KnKb Kshl ~ Welghl() s 1523 Kg I A- 89 Inch I bullB- 100 Inch
Dati 01 calcul w - 4115 Inch Mass Capaatv W 18500 KgIh Weight( ) 3357 Pound
P1 5553 bar abs r~ C Gase Constant 143843
() Indicative Values 0 now ooeIficient Kd 0915 0
Ksn 0865 Remarks Napier equation correction Kn 1
~ 2 valves are necessary 10 reach the required capacity
Back pressure correcUon Kb 1a BUlHmiddotup back pressureO 1 berg Same calculallO1 heet lor the 1st va lve and the spare one bull
N
~
GENERAl
PEO
PROCESS
CONDITONS
bull DESIGN
DATA
bull MATERIALS
I
OPT IONS
1 T Nu~
2 Service 3 Line NUrMer 4 P amp to Numbef
5 6 Conform to 961231EC 7 Fluid T
8 NJ licable rED Table 9
0 11
12
13
14
15 16
17 19
20 21 22
PED Cal
Fluid Fluid Servlc Required Capaci
MoltcullWe hI
ratln PrtSi ur
tlll TIm tUri
Badlt Prl$IIure
AJlovtabie Ova sure
Ov esslI10 FactOI Com esslbU Latenl Heal 01 V lion
o Tl 1012812005 Pour Commenta ires
Equipment
Fluid Groo
Fluid S~I
5 cltle Gl1Ivl Set Pressure
Col
HC+H20
15489
5 02
ReHov Temperatlyene 212
Constant Varia1je Total
23 Specific Hnt RItIo lC 24 Relief Densi
25 Relief Viscosity
26 Barometric Pressure 27 28 Nozzle Flit Semi
29 Design Saely Reflef Sale -Relief 30 Type Conventional BelloIN Plot Opefatad 31 BonnetT 32 n Code
33 Sizing Basis 34 Calcula ted Area
35 Selected Area 36 Orifice De nation
37 Size Rating -Inlel 38 Size Rat - Outlet
39 40 41 42 43 Stt 44 Fla es
45 Resilient Seat Seal 46 Guide
471 Spfing 46 Wtted Material
49 50
Bonnt Disc
Ri s Bellows
51 Cap Screwed or Bolted 52 Lever Plain or Packed 53 TestGag
54 55
22-ISV 3310 0 331fD332 SHCOO20150A1A 1 l -Q2S)(l2
y Gaseous Group 1
0 1
0
09
105
4
Note 10
k
C
k p
Safety Corrventlonal
hI Solted
ASME Delaut eau de refroldissement
1812 em
L 3 150 RF 450 RF
A2 16 WCB
NOlet A216WCB
NOle 1
Note 1
NOIot
NOIel
(Note 1
No
No
INSTRUMENT SPECIFICATION
Valve Safety Pressure Relief
oxicFlammable
GasIVapo
7
2564 C
A21 6WCB SS 316 Mini
Note 1
EJflt0nMobil Chemic
Sheet 5middot11 of 46
f
No 8 Date Revision Code 2831 No C3 1052 Amiddot163 1middottVOl Rev 0
i (
II Technical amp Calculation Data Sheet SARASIN-Agt Zllloa-R~
Safety Valve Nt BiOPUIle Gt1wtI bull bull 2110 1-1_
IN I ICustomer Name TECHNIP FRANCE
891 I 4 I bull s~ I
Cuslllem Numb 7273F RFQ 1545-01
Project KHARG OLEFIN COMPLEX I Opened
I 1 I
Quote Ref Tag No PSV pound I Nde Sales Abdeljalill Baigar I
I I uperatIng onaltons
Fluid ~e Superheated Steam 19 tnle ON shy
capaci ty 78500 Kgn 20 Inlet Finish ANSI 600 RF (125-250 AARH)
3 Set presMKC 21 Outlet ON
4935 bar eM 22 OtItlet Finish ANSI 150 RF (125-250 AARH)
DiSCharge Temp 375 middotC ASME B16-5 5 Variable back presslJe bull bar eft
Cold dilf lesc press 4935 bar eft I Bill 01 I
OverptesslKe B() 10 Bod SAl16 wee a Operating ProsslKe bar elf 24 Yoke SA216 wee
25 cabull SA216 weebull bull Tlglt Closing presSlKe (MAOP) 44 415 bar eff 26 Nozzle Sellited AlSI410 bullMlaquohBnIcaI Temp J15 C 21 Disc 174 PH Stilinless Steel 28 Gaskets Stainless $t1 bullSDOM Chromium Alloy Steel 30 Golde AlSI431 31 AcluslthQRinP SAl51 CF3M 32 Stud A183flr81 33 Nul Al94gr2H
gt0 Revulr Lever
Reqllif~ Afea 32023 om 35 middot SlelUted noule
12 496 sq in TU I Gag
1 Sellcl(l(l AIel 41 2 om
I 839 sq in Orirooe p
I ReactIon loree 3016 D I Flow capacity 100996 KgIh
I Noise ill 30 m ace to AP152 1 126 dB approxmate noise level at 30 m aCCOfding to APl521 (mtluth noise) open discharge
II 37 j API52 I I I
Commercial code S46P3530A-D-VMM I
IA= 525 PlKd~Kn KbKsh I I~-middot 2254 mm 2540 mm
11800 mm
bull 1523 Kg
lA shy 89 InCh
Dab 01 COI lcul I ~ - 100 Inch
IH- 465 Inch -jshyMa55 Capaoty W 18500 KgIh 3351 Pound -IP I 553 barabs C C-ase Constant 341143 I () Indicative Values 0 now coeffiCIent Kd 09150
N Ksh 0866 w- Napier equation coffeclion Kn bull 2 valves afe necessary to reach the required capacity lt Back Pfessure correcllon Kb
BUIItmiddotup back pressurecO 1 barg 2nd Ialve set at 05 of set pranure with 10 olelpreSSure in accordill1Ce With API 520
bullbulliii
bull 11 Load cases Ioad case combinations
The following load cases f load case combinations shall be analyzed 1) always or 2) on a casemiddot to-case basis
Static load cases for operating design and pressure test conditions
L6 jillL7 I
I --shy
I --shyI I I I I
L L
I Ll 9 L20
bull ~--
Load types (iC a pplicable load types should be added) W Dead weight (pipe weight + fluid weight + insulation weight) D Displacement T Design temperature P Design internal pressure U Uniform loads (eg snow load seismic load) F External forces (forces andor moments) HP Hydro test pressure H Hanger loads WIN Wind loads (for the main wind directions) WNC Dead weight without contents (pipe weight + insulation weight) WW Water-filled weight for pressure test
bull bull bull
bull
bull ~-
bullbull
SARASIN-lltJ l7Technical amp Calculation Data Sheet ZI 8olto R~62IKI _____ J40 11ap11M GnlCMl
VAlVH e COlTllOlS Safety Valve
e Bomel lype Opened
Project KHARG OLEfiN COMPLEX ~A
Tag No PSV 6 453A C-Quote Ref 3A30880IOOO Sales Engineer Abdeljalill Baigar W de Commande
Operating ondl tlons Connect ons
19 InlelON shy1 fluid type Superheated Stetlm
20 Inlet Finish ANSt600 RF (125-250 AARH) 2 Capacity 78500 Kglh 21 Outlet DN J Set ptesSUe br eft 22 Outlet Finish ANSI 150 ftF 1125-250 AARH) Ol$charoe Tom p J7S C Accordinn 10 ASME 616-5
5 Variable bad pressure 0 bar eft
Cold (If lest lXess 47 bar eft 8111 of material 7 Overpressure 11 () 16 floltfv SA216 wee
SA2115WCC2 Ylt8 Operating Pressure 40 bar eft
SA216 wee Tight Closing pressUIe (MAOP) 423 bar eft 26 NoWe Stllited AlSl410 1~ 27 174 PH Stainless SteelMechanical Tomp J7S middotC ~ 28 Gaskets Stalnl St1
29 SPfinQ Chromium Allov Steel 30 AlSI431c31 Adusitina Rlna SA351 CF3M 32 Stud Al1lQrB7 JJ Alt4i1r2H Accessories
Regular Levr 35 51etUted nozzl
ReqUIred Area 31 927 om Test Gag 495 s q InIl Selected Area 41 2 om
I 839 sq in 15 Onfice p
Reaction loroe DN~ t Flow capacity 101299 Kglh 18 Noise at 30 m acc to APt521 120 dB
apprO)flTlate noise level at 30 m according to API521 (mouth noiso) )perl dlsctlarge
Customer Name TECHNIP FRANCE evlslon ~ lion ate
890 4 20-juin-2005
Cust Item Numb 7U3F RFQ 1545-01 a ely a ype pflllg a a ely alve ea1T
I I J7 Standard API 520 I )
Commercial code S46P3530AmiddotDmiddotVMM I shyI Dimensions
A- 2254 mm B- 2540 mm W - 11800 mrnIA 525PlKd~KnKb Kshl ~ Welghl() s 1523 Kg I A- 89 Inch I bullB- 100 Inch
Dati 01 calcul w - 4115 Inch Mass Capaatv W 18500 KgIh Weight( ) 3357 Pound
P1 5553 bar abs r~ C Gase Constant 143843
() Indicative Values 0 now ooeIficient Kd 0915 0
Ksn 0865 Remarks Napier equation correction Kn 1
~ 2 valves are necessary 10 reach the required capacity
Back pressure correcUon Kb 1a BUlHmiddotup back pressureO 1 berg Same calculallO1 heet lor the 1st va lve and the spare one bull
N
~
GENERAl
PEO
PROCESS
CONDITONS
bull DESIGN
DATA
bull MATERIALS
I
OPT IONS
1 T Nu~
2 Service 3 Line NUrMer 4 P amp to Numbef
5 6 Conform to 961231EC 7 Fluid T
8 NJ licable rED Table 9
0 11
12
13
14
15 16
17 19
20 21 22
PED Cal
Fluid Fluid Servlc Required Capaci
MoltcullWe hI
ratln PrtSi ur
tlll TIm tUri
Badlt Prl$IIure
AJlovtabie Ova sure
Ov esslI10 FactOI Com esslbU Latenl Heal 01 V lion
o Tl 1012812005 Pour Commenta ires
Equipment
Fluid Groo
Fluid S~I
5 cltle Gl1Ivl Set Pressure
Col
HC+H20
15489
5 02
ReHov Temperatlyene 212
Constant Varia1je Total
23 Specific Hnt RItIo lC 24 Relief Densi
25 Relief Viscosity
26 Barometric Pressure 27 28 Nozzle Flit Semi
29 Design Saely Reflef Sale -Relief 30 Type Conventional BelloIN Plot Opefatad 31 BonnetT 32 n Code
33 Sizing Basis 34 Calcula ted Area
35 Selected Area 36 Orifice De nation
37 Size Rating -Inlel 38 Size Rat - Outlet
39 40 41 42 43 Stt 44 Fla es
45 Resilient Seat Seal 46 Guide
471 Spfing 46 Wtted Material
49 50
Bonnt Disc
Ri s Bellows
51 Cap Screwed or Bolted 52 Lever Plain or Packed 53 TestGag
54 55
22-ISV 3310 0 331fD332 SHCOO20150A1A 1 l -Q2S)(l2
y Gaseous Group 1
0 1
0
09
105
4
Note 10
k
C
k p
Safety Corrventlonal
hI Solted
ASME Delaut eau de refroldissement
1812 em
L 3 150 RF 450 RF
A2 16 WCB
NOlet A216WCB
NOle 1
Note 1
NOIot
NOIel
(Note 1
No
No
INSTRUMENT SPECIFICATION
Valve Safety Pressure Relief
oxicFlammable
GasIVapo
7
2564 C
A21 6WCB SS 316 Mini
Note 1
EJflt0nMobil Chemic
Sheet 5middot11 of 46
f
No 8 Date Revision Code 2831 No C3 1052 Amiddot163 1middottVOl Rev 0
i (
II Technical amp Calculation Data Sheet SARASIN-Agt Zllloa-R~
Safety Valve Nt BiOPUIle Gt1wtI bull bull 2110 1-1_
IN I ICustomer Name TECHNIP FRANCE
891 I 4 I bull s~ I
Cuslllem Numb 7273F RFQ 1545-01
Project KHARG OLEFIN COMPLEX I Opened
I 1 I
Quote Ref Tag No PSV pound I Nde Sales Abdeljalill Baigar I
I I uperatIng onaltons
Fluid ~e Superheated Steam 19 tnle ON shy
capaci ty 78500 Kgn 20 Inlet Finish ANSI 600 RF (125-250 AARH)
3 Set presMKC 21 Outlet ON
4935 bar eM 22 OtItlet Finish ANSI 150 RF (125-250 AARH)
DiSCharge Temp 375 middotC ASME B16-5 5 Variable back presslJe bull bar eft
Cold dilf lesc press 4935 bar eft I Bill 01 I
OverptesslKe B() 10 Bod SAl16 wee a Operating ProsslKe bar elf 24 Yoke SA216 wee
25 cabull SA216 weebull bull Tlglt Closing presSlKe (MAOP) 44 415 bar eff 26 Nozzle Sellited AlSI410 bullMlaquohBnIcaI Temp J15 C 21 Disc 174 PH Stilinless Steel 28 Gaskets Stainless $t1 bullSDOM Chromium Alloy Steel 30 Golde AlSI431 31 AcluslthQRinP SAl51 CF3M 32 Stud A183flr81 33 Nul Al94gr2H
gt0 Revulr Lever
Reqllif~ Afea 32023 om 35 middot SlelUted noule
12 496 sq in TU I Gag
1 Sellcl(l(l AIel 41 2 om
I 839 sq in Orirooe p
I ReactIon loree 3016 D I Flow capacity 100996 KgIh
I Noise ill 30 m ace to AP152 1 126 dB approxmate noise level at 30 m aCCOfding to APl521 (mtluth noise) open discharge
II 37 j API52 I I I
Commercial code S46P3530A-D-VMM I
IA= 525 PlKd~Kn KbKsh I I~-middot 2254 mm 2540 mm
11800 mm
bull 1523 Kg
lA shy 89 InCh
Dab 01 COI lcul I ~ - 100 Inch
IH- 465 Inch -jshyMa55 Capaoty W 18500 KgIh 3351 Pound -IP I 553 barabs C C-ase Constant 341143 I () Indicative Values 0 now coeffiCIent Kd 09150
N Ksh 0866 w- Napier equation coffeclion Kn bull 2 valves afe necessary to reach the required capacity lt Back Pfessure correcllon Kb
BUIItmiddotup back pressurecO 1 barg 2nd Ialve set at 05 of set pranure with 10 olelpreSSure in accordill1Ce With API 520
bullbulliii
bull 11 Load cases Ioad case combinations
The following load cases f load case combinations shall be analyzed 1) always or 2) on a casemiddot to-case basis
Static load cases for operating design and pressure test conditions
L6 jillL7 I
I --shy
I --shyI I I I I
L L
I Ll 9 L20
bull ~--
Load types (iC a pplicable load types should be added) W Dead weight (pipe weight + fluid weight + insulation weight) D Displacement T Design temperature P Design internal pressure U Uniform loads (eg snow load seismic load) F External forces (forces andor moments) HP Hydro test pressure H Hanger loads WIN Wind loads (for the main wind directions) WNC Dead weight without contents (pipe weight + insulation weight) WW Water-filled weight for pressure test
bull bull bull
bull
bull ~-
GENERAl
PEO
PROCESS
CONDITONS
bull DESIGN
DATA
bull MATERIALS
I
OPT IONS
1 T Nu~
2 Service 3 Line NUrMer 4 P amp to Numbef
5 6 Conform to 961231EC 7 Fluid T
8 NJ licable rED Table 9
0 11
12
13
14
15 16
17 19
20 21 22
PED Cal
Fluid Fluid Servlc Required Capaci
MoltcullWe hI
ratln PrtSi ur
tlll TIm tUri
Badlt Prl$IIure
AJlovtabie Ova sure
Ov esslI10 FactOI Com esslbU Latenl Heal 01 V lion
o Tl 1012812005 Pour Commenta ires
Equipment
Fluid Groo
Fluid S~I
5 cltle Gl1Ivl Set Pressure
Col
HC+H20
15489
5 02
ReHov Temperatlyene 212
Constant Varia1je Total
23 Specific Hnt RItIo lC 24 Relief Densi
25 Relief Viscosity
26 Barometric Pressure 27 28 Nozzle Flit Semi
29 Design Saely Reflef Sale -Relief 30 Type Conventional BelloIN Plot Opefatad 31 BonnetT 32 n Code
33 Sizing Basis 34 Calcula ted Area
35 Selected Area 36 Orifice De nation
37 Size Rating -Inlel 38 Size Rat - Outlet
39 40 41 42 43 Stt 44 Fla es
45 Resilient Seat Seal 46 Guide
471 Spfing 46 Wtted Material
49 50
Bonnt Disc
Ri s Bellows
51 Cap Screwed or Bolted 52 Lever Plain or Packed 53 TestGag
54 55
22-ISV 3310 0 331fD332 SHCOO20150A1A 1 l -Q2S)(l2
y Gaseous Group 1
0 1
0
09
105
4
Note 10
k
C
k p
Safety Corrventlonal
hI Solted
ASME Delaut eau de refroldissement
1812 em
L 3 150 RF 450 RF
A2 16 WCB
NOlet A216WCB
NOle 1
Note 1
NOIot
NOIel
(Note 1
No
No
INSTRUMENT SPECIFICATION
Valve Safety Pressure Relief
oxicFlammable
GasIVapo
7
2564 C
A21 6WCB SS 316 Mini
Note 1
EJflt0nMobil Chemic
Sheet 5middot11 of 46
f
No 8 Date Revision Code 2831 No C3 1052 Amiddot163 1middottVOl Rev 0
i (
II Technical amp Calculation Data Sheet SARASIN-Agt Zllloa-R~
Safety Valve Nt BiOPUIle Gt1wtI bull bull 2110 1-1_
IN I ICustomer Name TECHNIP FRANCE
891 I 4 I bull s~ I
Cuslllem Numb 7273F RFQ 1545-01
Project KHARG OLEFIN COMPLEX I Opened
I 1 I
Quote Ref Tag No PSV pound I Nde Sales Abdeljalill Baigar I
I I uperatIng onaltons
Fluid ~e Superheated Steam 19 tnle ON shy
capaci ty 78500 Kgn 20 Inlet Finish ANSI 600 RF (125-250 AARH)
3 Set presMKC 21 Outlet ON
4935 bar eM 22 OtItlet Finish ANSI 150 RF (125-250 AARH)
DiSCharge Temp 375 middotC ASME B16-5 5 Variable back presslJe bull bar eft
Cold dilf lesc press 4935 bar eft I Bill 01 I
OverptesslKe B() 10 Bod SAl16 wee a Operating ProsslKe bar elf 24 Yoke SA216 wee
25 cabull SA216 weebull bull Tlglt Closing presSlKe (MAOP) 44 415 bar eff 26 Nozzle Sellited AlSI410 bullMlaquohBnIcaI Temp J15 C 21 Disc 174 PH Stilinless Steel 28 Gaskets Stainless $t1 bullSDOM Chromium Alloy Steel 30 Golde AlSI431 31 AcluslthQRinP SAl51 CF3M 32 Stud A183flr81 33 Nul Al94gr2H
gt0 Revulr Lever
Reqllif~ Afea 32023 om 35 middot SlelUted noule
12 496 sq in TU I Gag
1 Sellcl(l(l AIel 41 2 om
I 839 sq in Orirooe p
I ReactIon loree 3016 D I Flow capacity 100996 KgIh
I Noise ill 30 m ace to AP152 1 126 dB approxmate noise level at 30 m aCCOfding to APl521 (mtluth noise) open discharge
II 37 j API52 I I I
Commercial code S46P3530A-D-VMM I
IA= 525 PlKd~Kn KbKsh I I~-middot 2254 mm 2540 mm
11800 mm
bull 1523 Kg
lA shy 89 InCh
Dab 01 COI lcul I ~ - 100 Inch
IH- 465 Inch -jshyMa55 Capaoty W 18500 KgIh 3351 Pound -IP I 553 barabs C C-ase Constant 341143 I () Indicative Values 0 now coeffiCIent Kd 09150
N Ksh 0866 w- Napier equation coffeclion Kn bull 2 valves afe necessary to reach the required capacity lt Back Pfessure correcllon Kb
BUIItmiddotup back pressurecO 1 barg 2nd Ialve set at 05 of set pranure with 10 olelpreSSure in accordill1Ce With API 520
bullbulliii
bull 11 Load cases Ioad case combinations
The following load cases f load case combinations shall be analyzed 1) always or 2) on a casemiddot to-case basis
Static load cases for operating design and pressure test conditions
L6 jillL7 I
I --shy
I --shyI I I I I
L L
I Ll 9 L20
bull ~--
Load types (iC a pplicable load types should be added) W Dead weight (pipe weight + fluid weight + insulation weight) D Displacement T Design temperature P Design internal pressure U Uniform loads (eg snow load seismic load) F External forces (forces andor moments) HP Hydro test pressure H Hanger loads WIN Wind loads (for the main wind directions) WNC Dead weight without contents (pipe weight + insulation weight) WW Water-filled weight for pressure test
bull bull bull
bull
bull ~-
II Technical amp Calculation Data Sheet SARASIN-Agt Zllloa-R~
Safety Valve Nt BiOPUIle Gt1wtI bull bull 2110 1-1_
IN I ICustomer Name TECHNIP FRANCE
891 I 4 I bull s~ I
Cuslllem Numb 7273F RFQ 1545-01
Project KHARG OLEFIN COMPLEX I Opened
I 1 I
Quote Ref Tag No PSV pound I Nde Sales Abdeljalill Baigar I
I I uperatIng onaltons
Fluid ~e Superheated Steam 19 tnle ON shy
capaci ty 78500 Kgn 20 Inlet Finish ANSI 600 RF (125-250 AARH)
3 Set presMKC 21 Outlet ON
4935 bar eM 22 OtItlet Finish ANSI 150 RF (125-250 AARH)
DiSCharge Temp 375 middotC ASME B16-5 5 Variable back presslJe bull bar eft
Cold dilf lesc press 4935 bar eft I Bill 01 I
OverptesslKe B() 10 Bod SAl16 wee a Operating ProsslKe bar elf 24 Yoke SA216 wee
25 cabull SA216 weebull bull Tlglt Closing presSlKe (MAOP) 44 415 bar eff 26 Nozzle Sellited AlSI410 bullMlaquohBnIcaI Temp J15 C 21 Disc 174 PH Stilinless Steel 28 Gaskets Stainless $t1 bullSDOM Chromium Alloy Steel 30 Golde AlSI431 31 AcluslthQRinP SAl51 CF3M 32 Stud A183flr81 33 Nul Al94gr2H
gt0 Revulr Lever
Reqllif~ Afea 32023 om 35 middot SlelUted noule
12 496 sq in TU I Gag
1 Sellcl(l(l AIel 41 2 om
I 839 sq in Orirooe p
I ReactIon loree 3016 D I Flow capacity 100996 KgIh
I Noise ill 30 m ace to AP152 1 126 dB approxmate noise level at 30 m aCCOfding to APl521 (mtluth noise) open discharge
II 37 j API52 I I I
Commercial code S46P3530A-D-VMM I
IA= 525 PlKd~Kn KbKsh I I~-middot 2254 mm 2540 mm
11800 mm
bull 1523 Kg
lA shy 89 InCh
Dab 01 COI lcul I ~ - 100 Inch
IH- 465 Inch -jshyMa55 Capaoty W 18500 KgIh 3351 Pound -IP I 553 barabs C C-ase Constant 341143 I () Indicative Values 0 now coeffiCIent Kd 09150
N Ksh 0866 w- Napier equation coffeclion Kn bull 2 valves afe necessary to reach the required capacity lt Back Pfessure correcllon Kb
BUIItmiddotup back pressurecO 1 barg 2nd Ialve set at 05 of set pranure with 10 olelpreSSure in accordill1Ce With API 520
bullbulliii
bull 11 Load cases Ioad case combinations
The following load cases f load case combinations shall be analyzed 1) always or 2) on a casemiddot to-case basis
Static load cases for operating design and pressure test conditions
L6 jillL7 I
I --shy
I --shyI I I I I
L L
I Ll 9 L20
bull ~--
Load types (iC a pplicable load types should be added) W Dead weight (pipe weight + fluid weight + insulation weight) D Displacement T Design temperature P Design internal pressure U Uniform loads (eg snow load seismic load) F External forces (forces andor moments) HP Hydro test pressure H Hanger loads WIN Wind loads (for the main wind directions) WNC Dead weight without contents (pipe weight + insulation weight) WW Water-filled weight for pressure test
bull bull bull
bull
bull ~-
bull 11 Load cases Ioad case combinations
The following load cases f load case combinations shall be analyzed 1) always or 2) on a casemiddot to-case basis
Static load cases for operating design and pressure test conditions
L6 jillL7 I
I --shy
I --shyI I I I I
L L
I Ll 9 L20
bull ~--
Load types (iC a pplicable load types should be added) W Dead weight (pipe weight + fluid weight + insulation weight) D Displacement T Design temperature P Design internal pressure U Uniform loads (eg snow load seismic load) F External forces (forces andor moments) HP Hydro test pressure H Hanger loads WIN Wind loads (for the main wind directions) WNC Dead weight without contents (pipe weight + insulation weight) WW Water-filled weight for pressure test
bull bull bull
bull
bull ~-
bull bull bull
bull
bull ~-
