Cl-r Mec-mc-ot-791-01 Rev. 0 Modificado
Transcript of Cl-r Mec-mc-ot-791-01 Rev. 0 Modificado
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CONSTRUCTORA HOSTOTIPAQUILLO
CARRETERA TULA - BOJAY, S/N, KM.0+300PARQUE INDUSTRIAL ATITALAQUIA.
ATITALAQUIA, HGO . MXICO
COMPRESS Pressure Vessel Design Calculations
EQUIPO: SEGUNDO ENFRIADOR DE FONDOS DEL AGOTADORTAG: MT-1-EA-3005-A
CLIENTE : PEMEXZ REFINACIN, AGUAS AMARGAS CD. MADERO
CONTRATO:
DISEADOR : RICARDO BARCENAS
FECHA: 29 OCT. 2013
You can edit this page by selecting Cover Page settings...in the reportmenu.
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Table of ContentsGeneral Arrangement Drawing..............................................................................................................................1/229
Deficiencies Summary............................................................................................................................................2/229
Nozzle Schedule......................................................................................................................................................3/229
Nozzle Summary.....................................................................................................................................................4/229
Pressure Summary.................................................................................................................................................5/229
Revision History......................................................................................................................................................9/229
Settings Summary.................................................................................................................................................10/229
Radiography Summary.........................................................................................................................................12/229
Thickness Summary.............................................................................................................................................14/229
Weight Summary...................................................................................................................................................15/229
Long Seam Summary...........................................................................................................................................17/229
Test Report............................................................................................................................................................19/229
Vacuum Summary.................................................................................................................................................21/229
ENVOLVENTE CANAL..........................................................................................................................................22/229
ENVOLVENTE 1.....................................................................................................................................................24/229
ENVOLVENTE 2.....................................................................................................................................................27/229
Rear Shell Cylinder...............................................................................................................................................30/229
TAPA BRIDADA CANAL.......................................................................................................................................33/229
Straight Flange on Rear Shell Head....................................................................................................................34/229
Rear Shell Head.....................................................................................................................................................37/229
BRIDA BIPARTIDA................................................................................................................................................39/229
BRIDA BONET -- CUERPO....................................................................................................................................44/229
BRIDA CANAL --ESPEJO......................................................................................................................................51/229
BRIDA CUERPO -- BONETE.................................................................................................................................58/229
BRIDA CUERPO ESPEJO FIJO............................................................................................................................65/229
BRIDA TAPA DEL CANAL....................................................................................................................................72/229
IP1 INSTRUMENTO DE PRESION (IP1)................................................................................................................79/229
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Tableof ContentsIP2 INSTRUMENTO DE PRESION (IP2)................................................................................................................84/229
IP3 INSTRUMENTO DE PRESION (IP3)................................................................................................................89/229
IP4 INSTRUMENTO DE PRESION (IP4)................................................................................................................94/229
IT1 INDICADOR DE TEMPERATURA (IT1)...........................................................................................................99/229
IT2 INSTRUMENTO DE TEMPERATUIRA (IT2)..................................................................................................104/229
IT3 INSTRUMENTO DE TEMPERATUIRA (IT3)..................................................................................................109/229
IT4 INSTRUMENTO DE TEMPERATURA (IT4)...................................................................................................114/229
N1 ENTRADA DEL FONDO DEL AGOTADOR (N1)...........................................................................................119/229
N2 INTERCONEXION DE ENVOLVENTE (N2)...................................................................................................127/229
N5 INTERCONEXION DE CANALES (N5)..........................................................................................................135/229
N6 SALIDA DE AGUA DE ENFRIAMIENTO (N6)...............................................................................................143/229
N7A CONEXION PARA LIMPIEZA QUIMICA (N7A)...........................................................................................151/229
N7B CONEXION PARA LIMPIEZA QUIMICA (N7B)...........................................................................................157/229
SILLETA...............................................................................................................................................................163/229
Baffle Summary Report......................................................................................................................................169/229
Data Inputs Summary.........................................................................................................................................170/229
Design Conditions Summary.............................................................................................................................171/229
Front Stationary Tubesheet -- ASME.................................................................................................................172/229
Materials and Gaskets Summary.......................................................................................................................196/229
TEMA RCB-9.132 Pass Partition Plate Calculations........................................................................................198/229
Rear Floating Tubesheet -- ASME......................................................................................................................199/229
Shell side liquid level..........................................................................................................................................214/229
TAPA FLOTANTE................................................................................................................................................215/229
Tube side liquid level..........................................................................................................................................224/229
Tubes....................................................................................................................................................................225/229
Tubesheet Maximum Pressure Report..............................................................................................................227/229
Front Stationary Tubesheet -- TEMA.................................................................................................................228/229
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General Arrangement Drawing
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Deficiencies Summary
No deficiencies found.
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Nozzle Schedule
Nozzlemark
Service Size MaterialsImpactTested
NormalizedFineGrain
Flange Blind
IP1 IP1 INSTRUMENTO DE PRESIONNPS 0.5 Class 6000 DN 15 -threaded
Nozzle SA-105 No No No N/A No
IP2 IP2 INSTRUMENTO DE PRESIONNPS 0.5 Class 6000 DN 15 -threaded
Nozzle SA-105 No No No N/A No
IP3 IP3 INSTRUMENTO DE PRESIONNPS 0.5 Class 6000 DN 15 -threaded
Nozzle SA-105 No No No N/A No
IP4 IP4 INSTRUMENTO DE PRESIONNPS 0.5 Class 6000 DN 15 -threaded
Nozzle SA-105 No No No N/A No
IT1IT1 INDICADOR DETEMPERATURA
NPS 0.5 Class 6000 DN 15 -threaded
Nozzle SA-105 No No No N/A No
IT2IT2 INSTRUMENTO DETEMPERATUIRA
NPS 0.5 Class 6000 DN 15 -threaded
Nozzle SA-105 No No No N/A No
IT3IT3 INSTRUMENTO DETEMPERATUIRA
NPS 0.5 Class 6000 DN 15 -threaded
Nozzle SA-105 No No No N/A No
IT4IT4 INSTRUMENTO DETEMPERATURA
NPS 0.5 Class 6000 DN 15 -threaded
Nozzle SA-105 No No No N/A No
N1N1 ENTRADA DEL FONDO DELAGOTADOR
NPS 6 Sch 80 (XS) DN 150 NozzleSA-106 B Smls.Pipe
No No NoNPS 6 Class150WN A105
No
N2N2 INTERCONEXION DEENVOLVENTE
NPS 6 Sch 80 (XS) DN 150 NozzleSA-106 B Smls.Pipe
No No NoNPS 6 Class150WN A105
No
N5 N5 INTERCONEXION DE CANALES NPS 6 Sch 80 (XS) DN 150 NozzleSA-106 B Smls.Pipe
No No NoNPS 6 Class150WN A105
No
N6N6 SALIDA DE AGUA DEENFRIAMIENTO
NPS 6 Sch 80 (XS) DN 150 NozzleSA-106 B Smls.Pipe
No No NoNPS 6 Class150WN A105
No
N7AN7A CONEXION PARA LIMPIEZAQUIMICA
NPS 2 Sch 160 DN 50 NozzleSA-106 B Smls.Pipe
No No NoNPS 2 Class150WN A105
No
N7BN7B CONEXION PARA LIMPIEZAQUIMICA
NPS 2 Sch 160 DN 50 NozzleSA-106 B Smls.Pipe
No No NoNPS 2 Class150WN A105
No
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Nozzle Summary
Nozzlemark
OD(mm)
tn
(mm)Req t
n(mm)
A1? A2?
ShellReinforcement
Pad Corr(mm)
Aa/A
r(%)
Nom t(mm)
Design t(mm)
User t(mm)
Width(mm)
tpad
(mm)
IP1 38.1 8.38 4.7 Yes Yes 10.97 N/A N/A N/A 3.2 Exempt
IP2 38.1 8.38 4.7 Yes Yes 10.97 N/A N/A N/A 3.2 Exempt
IP3 38.1 8.38 4.7 Yes Yes 10.97 N/A N/A N/A 3.2 Exempt
IP4 38.1 8.38 4.7 Yes Yes 10.97 N/A N/A N/A 3.2 Exempt
IT1 38.1 8.38 4.7 Yes Yes 10.97 N/A N/A N/A 3.2 Exempt
IT2 38.1 8.38 4.7 Yes Yes 10.97 N/A N/A N/A 3.2 Exempt
IT3 38.1 8.38 4.7 Yes Yes 10.97 N/A N/A N/A 3.2 Exempt
IT4 38.1 8.38 4.7 Yes Yes 10.97 N/A N/A N/A 3.2 Exempt
N1 168.27 10.97 8.33 Yes Yes 9.5 7.29 N/A N/A 3.2 100.0
N2 168.27 10.97 8.33 Yes Yes 9.5 7.29 N/A N/A 3.2 100.0
N5 168.27 10.97 8.32 Yes Yes 9.5 7.28 N/A N/A 3.17 100.0
N6 168.27 10.97 8.32 Yes Yes 9.5 7.28 N/A N/A 3.17 100.0
N7A 60.33 8.74 5.34 Yes Yes 10.97 N/A N/A N/A 3.17 Exempt
N7B 60.33 8.74 5.34 Yes Yes 10.97 N/A N/A N/A 3.17 Exempt
tn: Nozzle thickness
Req tn: Nozzle thickness required per UG-45/UG-16Nom t: Vessel wall thickness
Design t: Required vessel wall thickness due to pressure + corrosion allowance per UG-37
User t: Local vessel wall thickness (near opening)Aa: Area available per UG-37, governing condition
Ar: Area required per UG-37, governing condition
Corr: Corrosion allowance on nozzle wall
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Pressure Summary
Pressure Summary for Tube side chamber
IdentifierP
Design( kg/cm2)
T
Design( C)
MAWP( kg/cm2)
MAP( kg/cm2)
MAEP( kg/cm2)
Te
external( C)
MDMT( C)
MDMTExemption
ImpactTested
TAPA BRIDADA CANAL 7 66 8.3 8.36 N/A 66 -48 Note 1 No
ENVOLVENTE CANAL 7 66 27.39 41.36 N/A 66 -105 Note 2 No
Front Stationary Tubesheet(seeMaximum PressureRating note)
7 90 16.16 17.97 11.51 90 -48 Note 3 No
Rear Floating Tubesheet(see Maximum PressureRating note)
7 90 16.16 17.97 11.51 90 -48 Note 3 No
TAPA FLOTANTE 7 90 15.38 15.66 17 90 -48 Note 4 No
Tubes 7 90 198.3 198.36 125.47 90 -105 Note 5 No
BRIDA TAPA DEL CANAL 7 66 16.27 23.86 N/A 66 -48 Note 6 No
BRIDA TAPA DEL CANAL - Flange Hub 7 66 27.39 41.36 N/A 66 -105 Note 2 No
BRIDA CANAL --ESPEJO 7 66 16.7 23.86 N/A 66 -48 Note 6 No
BRIDA CANAL --ESPEJO - Flange Hub 7 66 27.39 41.36 N/A 66 -105 Note 2 No
BRIDA BIPARTIDA 7 90 14.51 14.51 70.24 90 -44.58 Note 7 No
IP2 INSTRUMENTO DE PRESION (IP2) 7 66 96.5 146.38 N/A 66 -105 Note 8 No
IP3 INSTRUMENTO DE PRESION (IP3) 7 66 96.43 146.38 N/A 66 -105 Note 9 No
IT2 INSTRUMENTO DE TEMPERATUIRA (IT2) 7 66 96.5 146.38 N/A 66 -105 Note 8 No
IT3 INSTRUMENTO DE TEMPERATUIRA (IT3) 7 66 96.43 146.38 N/A 66 -105 Note 9 No
N5 INTERCONEXION DE CANALES (N5) 7 66 17.84 19.99 N/A 66 -48 Note 10 No
N6 SALIDA DE AGUA DE ENFRIAMIENTO (N6) 7 66 17.91 19.99 N/A 66 -48 Note 10 No
N7A CONEXION PARA LIMPIEZA QUIMICA (N7A) 7 66 19.09 19.99 N/A 66 -48 Note 10 No
N7B CONEXION PARA LIMPIEZA QUIMICA (N7B) 7 66 19.02 19.99 N/A 66 -48 Note 10 No
Chamber design MDMT is -17.78 C
Chamber rated MDMT is -44.58 C @ 8.3 kg/cm2
Chamber MAWP hot & corroded is 8.3 kg/cm2@ 66 C
Chamber MAP cold & new is 8.36 kg/cm2@ 21.11 C
This pressure chamber is not designed for external pressure.
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Pressure Summary for Shell side chamber
IdentifierP
Design( kg/cm2)
T
Design( C)
MAWP( kg/cm2)
MAP( kg/cm2)
MAEP( kg/cm2)
Te
external( C)
MDMT( C)
MDMTExemption
ImpactTested
Front Stationary Tubesheet(seeMaximum PressureRating note)
11.5 90 11.51 13.32 16.16 90 -48 Note 3 No
ENVOLVENTE 1 11.5 90 27.26 41.36 N/A 90 -48 Note 11 No
ENVOLVENTE 2 11.5 90 27.26 41.36 N/A 90 -48 Note 11 NoRear Shell Cylinder 11.5 90 24.39 37.01 N/A 90 -48 Note 12 No
Straight Flange on Rear Shell Head 11.5 90 24.39 37.01 N/A 90 -48 Note 12 No
Rear Shell Head 11.5 90 24.9 37.5 N/A 90 -48 Note 13 No
Rear Floating Tubesheet(see Maximum PressureRating note)
11.5 90 11.51 13.32 16.16 90 -48 Note 3 No
TAPA FLOTANTE 11.5 90 17 31.36 15.38 90 N/A Note 14 No
BRIDA BIPARTIDA 11.5 90 70.24 70.24 14.51 90 -44.58 Note 7 No
Tubes 11.5 90 125.47 125.47 198.3 90 N/A N/A No
BRIDA CUERPO ESPEJO FIJO 11.5 90 16.84 24.06 N/A 90 -48 Note 15 No
BRIDA CUERPO ESPEJO FIJO - Flange Hub 11.5 90 27.39 41.36 N/A 90 -48 Note 16 No
BRIDA CUERPO -- BONETE 11.5 90 11.67 14.77 N/A 90 -48 Note 17 No
BRIDA CUERPO -- BONETE - Flange Hub 11.5 90 27.39 41.36 N/A 90 -48 Note 16 No
SILLETA 11.5 90 11.51 N/A N/A N/A N/A N/A N/A
BRIDA BONET -- CUERPO 11.5 90 11.66 14.77 N/A 90 -48 Note 17 No
BRIDA BONET -- CUERPO - Flange Hub 11.5 90 24.51 37.01 N/A 90 -48 Note 18 No
IP1 INSTRUMENTO DE PRESION (IP1) 11.5 90 96.03 146.38 N/A 90 -105 Note 19 No
IP4 INSTRUMENTO DE PRESION (IP4) 11.5 90 95.96 146.38 N/A 90 -105 Note 20 No
IT1 INDICADOR DE TEMPERATURA (IT1) 11.5 90 96.03 146.38 N/A 90 -105 Note 19 No
IT4 INSTRUMENTO DE TEMPERATURA (IT4) 11.5 90 95.96 146.38 N/A 90 -105 Note 20 No
N1 ENTRADA DEL FONDO DEL AGOTADOR (N1) 11.5 90 17.82 19.99 N/A 90 -48 Note 21 No
N2 INTERCONEXION DE ENVOLVENTE (N2) 11.5 90 17.75 19.99 N/A 90 -48 Note 22 No
Chamber design MDMT is -17.78 CChamber rated MDMT is -44.58 C @ 11.51 kg/cm2
Chamber MAWP hot & corroded is 11.51 kg/cm2@ 90 CMAWPis the maximum allowable shell side pressure for the component.
Chamber MAP cold & new is 13.32 kg/cm2@ 21.11 C
This pressure chamber is not designed for external pressure.
Notes for Maximum Pressure Rating:
Note # Details
1.The largest tubesheet MAWP/MAP values have been selected from the multiple design conditions to maximize the hydrotest pressure and to complywith UG-20(b). The MAWP/MAP selected for the shell side may not be coincident with the MAWP/MAP selected for the tube side (and vice versa).
2.The chamber MAWP listed above is based on the largest tubesheet MAWP values from the multiple design conditions. The lowest tubesheet MAWPvalues should be considered when determining the final chamber MAWP. Refer to the Tubesheet Maximum Pressure Reportfor the lowest tubesheetmaximum pressure ratings.
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Notes for MDMT Rating:
Note # Exemption Details
1.Bolted cover impact test exemption temperature from Fig UCS-66M Curve D = -48 C17 C MDMT reduction per UCS-68(c) applies.Rated MDMT of -65C is limited to -48C by UCS-66(b)(2)
UCS-66 governing thickness = 8 mm
2. Material is impact test exempt to -105 C per UCS-66(b)(3) (coincident ratio = 0.302)
3.Tubesheet impact test exemption temperature from Fig UCS-66M Curve D = -48 C17 C MDMT reduction per UCS-68(c) applies.Rated MDMT of -65C is limited to -48C by UCS-66(b)(2)
UCS-66 governing thickness = 9.23 mm
4.
impact test exemption temperature from Fig UCS-66M Curve B = -15.04 C17 C MDMT reduction per UCS-68(c) applies.Fig UCS-66.1M MDMT reduction = 17.5 C, (coincident ratio = 0.6874)Rated MDMT of -49.54C is limited to -48C by UCS-66(b)(2)UCS-66 governing thickness = 15.88 mm
Flange limits MDMT rating.
5. Material is impact test exempt per UCS-66(d) (NPS 4 or smaller pipe)
6.UCS-66(b)(1)(b) has been applied.Flange is impact test exempt to -105 C per UCS-66(b)(3) (coincident ratio = 0.3477)
Bolts rated MDMT per Fig UCS-66 note (c) = -48 C
7.
UCS-66(b)(1)(b) has been applied.Flange impact test exemption temperature from Fig UCS-66M Curve B = -19.38 CFig UCS-66.1M MDMT reduction = 25.2 C, (coincident ratio = 0.5716)UCS-66 governing thickness = 13.75 mm
Bolts rated MDMT per Fig UCS-66 note (c) = -48 C
8. Nozzle is impact test exempt to -105 C per UCS-66(b)(3) (coincident ratio = 0.0158).
9. Nozzle is impact test exempt to -105 C per UCS-66(b)(3) (coincident ratio = 0.016).
10.Flange rating governs:Flange rated MDMT = -65 C (UCS-68(c) applies.)Bolts rated MDMT per Fig UCS-66 note (c) = -48 C
UCS-66(b)(1)(b)
11.
Material impact test exemption temperature from Fig UCS-66M Curve D = -48 C17 C MDMT reduction per UCS-68(c) applies.Fig UCS-66.1M MDMT reduction = 45.3 C, (coincident ratio = 0.4207)Rated MDMT of -110.3C is limited to -48C by UCS-66(b)(2)
UCS-66 governing thickness = 9.5 mm
12.
Material impact test exemption temperature from Fig UCS-66M Curve B = -29 C17 C MDMT reduction per UCS-68(c) applies.Fig UCS-66.1M MDMT reduction = 35.3 C, (coincident ratio = 0.4707)Rated MDMT of -81.3C is limited to -48C by UCS-66(b)(2)
UCS-66 governing thickness = 9.5 mm
13. Straight Flangegoverns MDMT
14. UCS-66 does not apply. Reference Fig. UCS-66.2 General Note (2)
15.
UCS-66(b)(1)(b) has been applied.Flange impact test exemption temperature from Fig UCS-66M Curve B = -29 C17 C MDMT reduction per UCS-68(c) applies.Fig UCS-66.1M MDMT reduction = 34.3 C, (coincident ratio = 0.4782)Rated MDMT of -80.3C is limited to -48C by UCS-66(b)(2)UCS-66 governing thickness = 9.5 mm
Bolts rated MDMT per Fig UCS-66 note (c) = -48 C
16.
Material impact test exemption temperature from Fig UCS-66M Curve B = -29 C17 C MDMT reduction per UCS-68(c) applies.Fig UCS-66.1M MDMT reduction = 45.9 C, (coincident ratio = 0.4186)Rated MDMT of -91.9C is limited to -48C by UCS-66(b)(2)
UCS-66 governing thickness = 9.5 mm
17.
UCS-66(b)(1)(b) has been applied.Flange impact test exemption temperature from Fig UCS-66M Curve B = -29 C17 C MDMT reduction per UCS-68(c) applies.Fig UCS-66.1M MDMT reduction = 12.4 C, (coincident ratio = 0.779)Rated MDMT of -58.4C is limited to -48C by UCS-66(b)(2)UCS-66 governing thickness = 9.5 mm
Bolts rated MDMT per Fig UCS-66 note (c) = -48 C
18.Material impact test exemption temperature from Fig UCS-66M Curve B = -29 C17 C MDMT reduction per UCS-68(c) applies.Fig UCS-66.1M MDMT reduction = 35.7 C, (coincident ratio = 0.4684)Rated MDMT of -81.7C is limited to -48C by UCS-66(b)(2)
UCS-66 governing thickness = 9.5 mm
19. Nozzle is impact test exempt to -105 C per UCS-66(b)(3) (coincident ratio = 0.022).
20. Nozzle is impact test exempt to -105 C per UCS-66(b)(3) (coincident ratio = 0.0221).
21.
Nozzle impact test exemption temperature from Fig UCS-66M Curve B = -29 C17 C MDMT reduction per UCS-68(c) applies.Fig UCS-66.1M MDMT reduction = 46 C, (coincident ratio = 0.4183)Rated MDMT of -92C is limited to -48C by UCS-66(b)(2)
UCS-66 governing thickness = 9.5 mm.
22. UCS-66 governing thickness = 9.5 mm.
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Nozzle impact test exemption temperature from Fig UCS-66M Curve B = -29 C17 C MDMT reduction per UCS-68(c) applies.Fig UCS-66.1M MDMT reduction = 45.3 C, (coincident ratio = 0.4207)Rated MDMT of -91.3C is limited to -48C by UCS-66(b)(2)
Design notes are available on the Settings Summarypage.
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Revision History
No. Date Operator Notes
0 10/28/2013 rbarcenas New vessel created Heat Exchanger. [COMPRESS 2013 Build 7330]
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Settings Summary
COMPRESS 2013 Build 7330
Units: MKS
Datum Line Location: -34.00 mm from left seam
Design
ASME Section VIII Division 1, 2010 Edition, A11 Addenda Metric
Design or Rating: Get Thickness from Pressure
Minimum thickness: 1.5 mm per UG-16(b)Design for cold shut down only: No
Design for lethal service (full radiography required): No
Design nozzles for: Design P, find nozzle MAWP and MAPCorrosion weight loss: 100% of theoretical loss
UG-23 Stress Increase: 1.20
Skirt/legs stress increase: 1.0
Minimum nozzle projection: 152.4 mmJuncture calculations for > 30 only: Yes
Preheat P-No 1 Materials > 1.25" and
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UG-22 Loadings
UG-22(a) Internal or External Design Pressure : YesUG-22(b) Weight of the vessel and normal contents under operating or test conditions: Yes
UG-22(c) Superimposed static reactions from weight of attached equipment (external loads): No
UG-22(d)(2) Vessel supports such as lugs, rings, skirts, saddles and legs: YesUG-22(f) Wind reactions: No
UG-22(f) Seismic reactions: No
UG-22(j) Test pressure and coincident static head acting during the test: NoNote: UG-22(b),(c) and (f) loads only considered when supports are present.
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Radiography Summary
Radiography for Tube side chamber
Component
Longitudinal Seam Left Circumferential Seam Right Circumferential Seam
MarkCategory(Fig
UW-3)
Radiography /Joint Type
Category(Fig
UW-3)
Radiography /Joint Type
Category(Fig
UW-3)
Radiography / JointType
TAPA BRIDADA CANAL N/A Seamless No RT N/A N/A N/A N/A / Gasketed N/A
ENVOLVENTE CANAL A Full UW-11(a) /Type 1
C Full UW-11(a) /Type 1
C Full UW-11(a) / Type1
RT1
BRIDA TAPA DEL CANAL N/A Seamless No RT N/A N/A / Gasketed CFull UW-11(a) / Type1
RT1
BRIDA CANAL --ESPEJO N/A Seamless No RT CFull UW-11(a) /Type 1
N/A N/A / Gasketed RT1
Front Stationary Tubesheet N/A Seamless No RT N/A N/A / Gasketed N/A N/A / Gasketed N/A
Rear Floating Tubesheet N/A Seamless No RT C N/A / Gasketed N/A N/A / Gasketed N/A
BRIDA BIPARTIDA N/A Seamless No RT N/A N/A / Gasketed C N/A N/A
TAPA FLOTANTE N/A Seamless No RT C N/A / Gasketed N/A N/A N/A
Tubes N/A Seamless No RT N/A N/A / Type 7 N/A N/A / Type 7 N/A
Nozzle Longitudinal SeamNozzle to Vessel
Circumferential Seam
Nozzle free end Circumferential
Seam
N6 SALIDA DE AGUA DE ENFRIAMIENTO (N6) N/A Seamless No RT D N/A / Type 7 CUW-11(a)(4) exempt/ Type 1
N/A
N7A CONEXION PARA LIMPIEZA QUIMICA (N7A) N/A Seamless No RT D N/A / Type 7 CUW-11(a)(4) exempt/ Type 1
N/A
IT2 INSTRUMENTO DE TEMPERATUIRA (IT2) N/A Seamless No RT D N/A / Type 7 N/A N/A N/A
IP2 INSTRUMENTO DE PRESION (IP2) N/A Seamless No RT D N/A / Type 7 N/A N/A N/A
N5 INTERCONEXION DE CANALES (N5) N/A Seamless No RT D N/A / Type 7 CUW-11(a)(4) exempt/ Type 1
N/A
N7B CONEXION PARA LIMPIEZA QUIMICA (N7B) N/A Seamless No RT D N/A / Type 7 CUW-11(a)(4) exempt/ Type 1
N/A
IP3 INSTRUMENTO DE PRESION (IP3) N/A Seamless No RT D N/A / Type 7 N/A N/A N/A
IT3 INSTRUMENTO DE TEMPERATUIRA (IT3) N/A Seamless No RT D N/A / Type 7 N/A N/A N/A
Nozzle Flange Longitudinal Seam Flange FaceNozzle to Flange
Circumferential Seam
ASME B16.5/16.47 flange attached to N6 SALIDADE AGUA DE ENFRIAMIENTO (N6)
N/A Seamless No RT N/A N/A / Gasketed CUW-11(a)(4) exempt/ Type 1
N/A
ASME B16.5/16.47 flange attached to N7ACONEXION PARA LIMPIEZA QUIMICA (N7A)
N/A Seamless No RT N/A N/A / Gasketed CUW-11(a)(4) exempt/ Type 1
N/A
ASME B16.5/16.47 flange attached to N5INTERCONEXION DE CANALES (N5)
N/A Seamless No RT N/A N/A / Gasketed CUW-11(a)(4) exempt/ Type 1
N/A
ASME B16.5/16.47 flange attached to N7BCONEXION PARA LIMPIEZA QUIMICA (N7B)
N/A Seamless No RT N/A N/A / Gasketed CUW-11(a)(4) exempt/ Type 1
N/A
Tube side chamber - UG-116(e) Radiography:RT1
Radiography for Shell side chamber
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Component
Longitudinal Seam Left Circumferential Seam Right Circumferential Seam
MarkCategory(Fig
UW-3)
Radiography /Joint Type
Category(Fig
UW-3)
Radiography /Joint Type
Category(Fig
UW-3)
Radiography / JointType
Front Stationary Tubesheet N/A Seamless No RT N/A N/A / Gasketed N/A N/A / Gasketed N/A
ENVOLVENTE 1 AFull UW-11(a) /Type 1
CFull UW-11(a) /Type 1
BFull UW-11(a) / Type1
RT1
BRIDA CUERPO ESPEJO FIJO N/A Seamless No RT N/A N/A / Gasketed CFull UW-11(a) / Type1
RT1
ENVOLVENTE 2 A Full UW-11(a) /Type 1 B Full UW-11(a) /Type 1 C Full UW-11(a) / Type1 RT1
BRIDA CUERPO -- BONETE N/A Seamless No RT CFull UW-11(a) /Type 1
N/A N/A / Gasketed RT1
Rear Shell Cylinder AFull UW-11(a) /Type 1
CFull UW-11(a) /Type 1
BFull UW-11(a) / Type1
RT1
BRIDA BONET --CUERPO N/A Seamless No RT N/A N/A / Gasketed CFull UW-11(a) / Type1
RT1
Rear Shell Head N/A Seamless No RT BFull UW-11(a) /Type 1
N/A N/A RT1
Rear Floating Tubesheet N/A Seamless No RT C N/A / Gasketed N/A N/A / Gasketed N/A
Nozzle Longitudinal SeamNozzle to Vessel
Circumferential SeamNozzle free end Circumferential
Seam
N2 INTERCONEXION DE ENVOLVENTE (N2) N/A Seamless No RT D N/A / Type 7 C UW-11(a)(4) exempt/ Type 1
N/A
IP4 INSTRUMENTO DE PRESION (IP4) N/A Seamless No RT D N/A / Type 7 N/A N/A N/A
IT4 INSTRUMENTO DE TEMPERATURA (IT4) N/A Seamless No RT D N/A / Type 7 N/A N/A N/A
N1 ENTRADA DEL FONDO DEL AGOTADOR (N1) N/A Seamless No RT D N/A / Type 7 CUW-11(a)(4) exempt/ Type 1
N/A
IP1 INSTRUMENTO DE PRESION (IP1) N/A Seamless No RT D N/A / Type 7 N/A N/A N/A
IT1 INDICADOR DE TEMPERATURA (IT1) N/A Seamless No RT D N/A / Type 7 N/A N/A N/A
Nozzle Flange Longitudinal Seam Flange FaceNozzle to Flange
Circumferential Seam
ASME B16.5/16.47 flange attached to N2INTERCONEXION DE ENVOLVENTE (N2)
N/A Seamless No RT N/A N/A / Gasketed CUW-11(a)(4) exempt/ Type 1
N/A
ASME B16.5/16.47 flange attached to N1 ENTRADADEL FONDO DEL AGOTADOR (N1) N/A Seamless No RT N/A N/A / Gasketed C UW-11(a)(4) exempt/ Type 1 N/A
Shell side chamber - UG-116(e) Radiography:RT1
Tubesheets are always considered to be seamless.
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Thickness Summary
ComponentIdentifier
Material Diameter(mm)
Length(mm)
Nominal t(mm)
Design t(mm)
Total Corrosion(mm)
JointE
Load
TAPA BRIDADA CANAL SA-516 70 788 OD 32 32* 29.42 0 1.00 Internal
ENVOLVENTE CANAL SA-516 70 635 ID 355 9.5 4.79 3.17 1.00 Internal
Front Stationary Tubesheet SA-516 70 665 OD 36.94 36.94 36.93 6.37 1.00 Unknown
Rear Floating Tubesheet SA-516 70 630 OD 36.94 36.94 36.93 6.37 1.00 Unknown
Tubes SA-179 Smls. Tube 19 OD 4,877 2.11 0.37 0 1.00 External
ENVOLVENTE 1 SA-516 70 635 ID 2,214 9.5 5.85 3.2 1.00 Internal
ENVOLVENTE 2 SA-516 70 635 ID 2,214 9.5 5.85 3.2 1.00 Internal
Rear Shell Cylinder SA-516 70 711 ID 243 9.5 6.16 3.2 1.00 Internal
Straight Flange on Rear Shell Head SA-516 70 711 ID 50.8 9.5 6.16 3.2 1.00 Internal
Rear Shell Head SA-516 70 711 ID 187.25 9.5* 6.12 3.2 1.00 Internal
Flange - TAPA FLOTANTE SA-105 609 ID 51.49 51.49 57.73 3.17 1.00 Unknown
TAPA FLOTANTE SA-516 70 609 ID 120.2 15.88* 13.46 6.37 1.00 External
Nominal t: Vessel wall nominal thickness
Design t: Required vessel thickness due to governing loading + corrosionJoint E: Longitudinal seam joint efficiency
* Head minimum thickness after forming
Load
internal: Circumferential stress due to internal pressure governs
external: External pressure governs
Wind: Combined longitudinal stress of pressure + weight + wind governs
Seismic: Combined longitudinal stress of pressure + weight + seismic governs
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Weight Summary
Component
Weight ( kg) Contributed by Vessel Elements SurfaceAream2Metal
New*
Metal
Corroded* InsulationInsulationSupports
LiningPiping
+ Liquid
Operating Liquid Test Liquid
New Corroded New Corroded
TAPA BRIDADA CANAL 122.2 122.2 0 0 0 0 0 0 0 0 0.57
ENVOLVENTE CANAL 50.2 33.6 0 0 0 0 176.1 179.8 179.4 183.5 0.68
Front Stationary Tubesheet 80.6 47.8 0 0 0 0 0 0 0 0 0.08
Rear Floating Tubesheet 64.3 36.3 0 0 0 0 0 0 0 0 N/A
TAPA FLOTANTE 76.9 59.3 0 0 0 0 18.4 19.4 18.4 19.5 0
ENVOLVENTE 1 331.9 221.2 0 0 0 0 491.8 506.6 491.8 506.9 4.53
ENVOLVENTE 2 331.9 221.2 0 0 0 0 487 501.4 489.9 505 4.53
Tubes 1,581.3 1,581.3 0 0 0 0 309.5 309.5 309.5 309.5 N/A
Rear Shell Cylinder 40.9 27.3 0 0 0 0 76 79.1 77.6 80.9 0.56
Rear Shell Head 53.4 35.7 0 0 0 0 66.4 68.3 63.6 66 0.76
SILLETA 74.4 74.4 0 0 0 0 0 0 0 0 1.59
TOTAL: 2,808 2,460.3 0 0 0 0 1,625.1 1,664 1,630.2 1,671.3 13.29
* Shells with attached nozzles have weight reduced by material cut out for opening.
Component
Weight ( kg) Contributed by Attachments
Surface Aream2Body Flanges Nozzles &Flanges
PackedBeds
TraysBaffles
Pass Partitions
TraySupports
Rings &Clips
VerticalLoads
New Corroded New Corroded
TAPA BRIDADA CANAL 0 0 0 0 0 0 0 0 0 0
ENVOLVENTE CANAL 175.4 166.1 46.4 40.7 0 0 0 0 0 1.02
Front Stationary Tubesheet 0 0 0 0 0 47.9 0 0 0 0
Rear Floating Tubesheet 29.8 27.1 0 0 0 0 0 0 0 0
TAPA FLOTANTE 0 0 0 0 0 0 0 0 0 0
ENVOLVENTE 1 87.7 83.1 19.6 17 0 49.8 0 0 0 0.45
ENVOLVENTE 2 113.6 109.4 19.6 17 0 49.8 0 0 0 0.45
Rear Shell Cylinder 90.8 85.6 0 0 0 0 0 0 0 0.25
Rear Shell Head 0 0 0 0 0 0 0 0 0 0
TOTAL: 497.3 471.3 85.5 74.7 0 147.4 0 0 0 2.17
Vessel operating weight, Corroded: 4,794 kg
Vessel operating weight, New: 5,163 kgVessel empty weight, Corroded: 3,130 kg
Vessel empty weight, New: 3,538 kg
Vessel test weight, New: 5,150 kgVessel test weight, Corroded: 4,782 kg
Vessel surface area: 15.47 m2
Vessel center of gravity location - from datum - lift condition
Vessel Lift Weight, New: 3,538 kg
Center of Gravity: 2,843.58 mm
Vessel Capacity
Shell side Capacity** (New): 1,130 litersShell side Capacity** (Corroded): 1,165 liters
Tube side Capacity** (New): 502 liters
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Tube side Capacity** (Corroded): 506 liters**The shell and tube capacity does not include volume of nozzle, piping or other attachments.
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Long Seam Summary
Shell Long Seam Angles
Component Seam 1
ENVOLVENTE CANAL 45
ENVOLVENTE 1 30
ENVOLVENTE 2 315
Rear Shell Cylinder 30
Shell Plate Lengths
ComponentStartingAngle
Plate 1
ENVOLVENTE CANAL 45 2,024.76 mm
ENVOLVENTE 1 30 2,024.76 mm
ENVOLVENTE 2 315 2,024.76 mm
Rear Shell Cylinder 30 2,263.52 mm
*Plate Lengths use the circumference of the vessel based on the mid diameter of the components
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Shell Rollout
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Test Report
Shop test pressure determination for Tube side chamber based on user defined pressure
Shop test gauge pressure is 9.1 kg f/cm2at 21.11 C
The shop test is performed with the vessel in the horizontal position.
IdentifierLocal testpressurekgf/cm
2
Testliquidstatichead
kgf/cm2
ENVOLVENTE CANAL 9.19 0.09
TAPA FLOTANTE 9.19 0.09
Tubes 9.19 0.09
BRIDA TAPA DEL CANAL - Flange Hub 9.19 0.09
BRIDA CANAL --ESPEJO - Flange Hub 9.19 0.09
TAPA BRIDADA CANAL 9.19 0.09BRIDA TAPA DEL CANAL 9.19 0.09
BRIDA CANAL --ESPEJO 9.19 0.09
Front Stationary Tubesheet 9.19 0.09
Rear Floating Tubesheet 9.19 0.09
BRIDA BIPARTIDA 9.19 0.09
IP2 INSTRUMENTO DE PRESION (IP2) 9.12 0.02
IP3 INSTRUMENTO DE PRESION (IP3) 9.2 0.1
IT2 INSTRUMENTO DE TEMPERATUIRA (IT2) 9.12 0.02
IT3 INSTRUMENTO DE TEMPERATUIRA (IT3) 9.2 0.1
N5 INTERCONEXION DE CANALES (N5) 9.22 0.12
N6 SALIDA DE AGUA DE ENFRIAMIENTO (N6) 9.13 0.03
N7A CONEXION PARA LIMPIEZA QUIMICA (N7A) 9.12 0.02
N7B CONEXION PARA LIMPIEZA QUIMICA (N7B) 9.2 0.1
Notes:(1) The zero degree angular position is assumed to be up, and the test liquid height is assumed to the top-mostflange.
The field test condition has not been investigated for the Tube side chamber.
The test temperature of 21.11 C is warmer than the minimum recommended temperature of -27.58 C so the brittlefracture provision of UG-99(h) has been met.
Shop test pressure determination for Shell side chamber based on user defined pressure
Shop test gauge pressure is 14.95 kg f/cm2at 21.11 C
The shop test is performed with the vessel in the horizontal position.
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IdentifierLocal testpressurekgf/cm
2
Testliquidstatichead
kgf/cm2
ENVOLVENTE 1 15.04 0.09
ENVOLVENTE 2 15.04 0.09
Rear Shell Cylinder 15.04 0.09
TAPA FLOTANTE 15.04 0.09
Straight Flange on Rear Shell Head 15.04 0.09
Rear Shell Head 15.04 0.09
Tubes 15.04 0.09
BRIDA CUERPO ESPEJO FIJO - Flange Hub 15.04 0.09
BRIDA CUERPO -- BONETE - Flange Hub 15.04 0.09
BRIDA BONET -- CUERPO - Flange Hub 15.04 0.09
Front Stationary Tubesheet 15.04 0.09
BRIDA CUERPO ESPEJO FIJO 15.04 0.09
BRIDA CUERPO -- BONETE 15.04 0.09
BRIDA BONET -- CUERPO 15.04 0.09Rear Floating Tubesheet 15.04 0.09
BRIDA BIPARTIDA 15.04 0.09
IP1 INSTRUMENTO DE PRESION (IP1) 14.97 0.02
IP4 INSTRUMENTO DE PRESION (IP4) 15.05 0.1
IT1 INDICADOR DE TEMPERATURA (IT1) 14.97 0.02
IT4 INSTRUMENTO DE TEMPERATURA (IT4) 15.05 0.1
N1 ENTRADA DEL FONDO DEL AGOTADOR (N1) 14.98 0.03
N2 INTERCONEXION DE ENVOLVENTE (N2) 15.07 0.12
Notes:
(1) The zero degree angular position is assumed to be up, and the test liquid height is assumed to the top-mostflange.
The field test condition has not been investigated for the Shell side chamber.
The test temperature of 21.11 C is warmer than the minimum recommended temperature of -27.58 C so the brittlefracture provision of UG-99(h) has been met.
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Vacuum Summary
Component Line of Support
Elevation
aboveDatum(mm)
Length Le(mm)
TAPA BRIDADA CANAL - 2 N/A
- TAPA BRIDADA CANAL 34 N/A
ENVOLVENTE CANAL Left - 130.2 545.8
ENVOLVENTE CANAL Right - 485.2 545.8
Front Stationary Tubesheet - 575 N/A
- BRIDA CANAL --ESPEJO 579.8 N/A
- BRIDA CUERPO ESPEJO FIJO 613.54 N/A
ENVOLVENTE 1 Left - 708.14 4,607.6
ENVOLVENTE 1 Right - 2,922.14 4,607.6
ENVOLVENTE 2 Left - 2,922.14 4,607.6
ENVOLVENTE 2 Right - 5,136.14 4,607.6
- BRIDA CUERPO -- BONETE 5,221.14 N/A
- BRIDA BONET -- CUERPO 5,224.34 N/A
Rear Shell Cylinder Left - 5,316.34 446.12
Rear Floating Tubesheet - 5,415.06 N/A
- Flange - TAPA FLOTANTE 5,479.34 N/A
- 1/3 depth of TAPA FLOTANTE 5,479.34 N/A
Rear Shell Cylinder Right - 5,559.34 446.12
Straight Flange on Rear Shell Head Left - 5,559.34 446.12
TAPA FLOTANTE - 5,599.55 N/A
Straight Flange on Rear Shell Head Right - 5,610.14 446.12
- 1/3 depth of Rear Shell Head 5,670.45 N/A
Rear Shell Head - 5,797.39 N/A
NoteFor main components, the listed value of 'Le' is the largest unsupported length for the component.
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ENVOLVENTE CANAL
ASME Section VIII Division 1, 2010 Edition, A11 Addenda Metric
Component: CylinderMaterial specification: SA-516 70 (II-D Metric p. 18, ln. 19)Material is impact test exempt to -105 C per UCS-66(b)(3) (coincident ratio = 0.302)
Internal design pressure: P = 7 kg/cm2@ 66 C
Static liquid head:
Ps = 0.06 kg/cm2 (SG = 1, Hs= 638.17 mm,Operating head)
Pth = 0.09 kg/cm2 (SG = 1, Hs= 907.5 mm, Horizontal test
head)
Corrosion allowance Inner C = 3.17 mm Outer C = 0 mm
Design MDMT = -17.78 C No impact test performedRated MDMT = -105 C Material is not normalized
Material is not produced to Fine Grain PracticePWHT is performed
Radiography: Longitudinal joint - Full UW-11(a) Type 1Left circumferential joint - Full UW-11(a) Type 1Right circumferential joint - Full UW-11(a) Type 1
Estimated weight New = 50.2 kg corr = 33.6 kgCapacity New = 112.43 liters corr = 114.68 liters
ID = 635 mmLengthLc
= 355 mm
t = 9.5 mm
Design thickness, (at 66 C) UG-27(c)(1)
t = P*R / (S*E - 0.60*P) + Corrosion= 7.06*320.67 / (1,407.21*1.00 - 0.60*7.06) + 3.17= 4.79 mm
Maximum allowable working pressure, (at 66 C) UG-27(c)(1)
P = S*E*t / (R + 0.60*t) - Ps= 1,407.21*1.00*6.33 / (320.67 + 0.60*6.33) - 0.06= 27.39 kg/cm2
Maximum allowable pressure, (at 21.11 C) UG-27(c)(1)
P = S*E*t / (R + 0.60*t)= 1,407.21*1.00*9.5 / (317.5 + 0.60*9.5)= 41.36 kg/cm2
% Extreme fiber elongation - UCS-79(d)
EFE = (50*t / Rf)*(1 - Rf/ Ro)
= (50*9.5 / 322.25)*(1 - 322.25 / infinity)
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= 1.474%
The extreme fiber elongation does not exceed 5%.
Allowable Compressive Stress, Hot and Corroded- ScHC, (table CS-2Metric)
A = 0.125 / (Ro/ t)
= 0.125 / (327 / 6.33)
= 0.002420B = 1,092.5 kg/cm2
S = 1,407.2 / 1.00 = 1,407.2 kg/cm2
ScHC = min(B, S) = 1,092.5 kg/cm2
Allowable Compressive Stress, Hot and New- ScHN, (table CS-2 Metric)
A = 0.125 / (Ro/ t)
= 0.125 / (327 / 9.5)= 0.003631
B = 1,169 kg/cm2
S = 1,407.2 / 1.00 = 1,407.2 kg/cm2
ScHN = min(B, S) = 1,169 kg/cm2
Allowable Compressive Stress, Cold and New- ScCN, (table CS-2 Metric)
A = 0.125 / (Ro/ t)= 0.125 / (327 / 9.5)
= 0.003631
B = 1,169 kg/cm2
S = 1,407.2 / 1.00 = 1,407.2 kg/cm2
ScCN = min(B, S) = 1,169 kg/cm2
Allowable Compressive Stress, Cold and Corroded- ScCC, (table CS-2Metric)
A = 0.125 / (Ro/ t)
= 0.125 / (327 / 6.33)= 0.002420
B = 1,092.5 kg/cm2
S = 1,407.2 / 1.00 = 1,407.2 kg/cm2
ScCC = min(B, S) = 1,092.5 kg/cm2
Allowable Compressive Stress, Vacuum and Corroded- ScVC, (tableCS-2 Metric)
A = 0.125 / (Ro/ t)
= 0.125 / (327 / 6.33)
= 0.002420B = 1,092.5 kg/cm2
S = 1,407.2 / 1.00 = 1,407.2 kg/cm2
ScVC = min(B, S) = 1,092.5 kg/cm2
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ENVOLVENTE 1
ASME Section VIII Division 1, 2010 Edition, A11 Addenda Metric
Component: CylinderMaterial specification: SA-516 70 (II-D Metric p. 18, ln. 19)Material impact test exemption temperature from Fig UCS-66M Curve D = -48 C17 C MDMT reduction per UCS-68(c) applies.Fig UCS-66.1M MDMT reduction = 45.3 C, (coincident ratio = 0.4207)
Rated MDMT of -110.3C is limited to -48C by UCS-66(b)(2)UCS-66 governing thickness = 9.5 mm
Internal design pressure: P = 11.5 kg/cm2@ 90 C
Static liquid head:
Ps = 0.06 kg/cm2 (SG = 1, Hs= 638.2 mm,Operating head)
Pth = 0.09 kg/cm2 (SG = 1, Hs= 907.5 mm, Horizontal test
head)
Corrosion allowance Inner C = 3.2 mm Outer C = 0 mm
Design MDMT = -17.78 C No impact test performedRated MDMT = -48 C Material is normalized
Material is not produced to Fine Grain PracticePWHT is performed
Radiography: Longitudinal joint - Full UW-11(a) Type 1Left circumferential joint - Full UW-11(a) Type 1Right circumferential joint - Full UW-11(a) Type 1
Estimated weight New = 331.9 kg corr = 221.2 kg
Capacity New = 468.9 liters corr = 483.1 liters
ID = 635 mmLengthLc
= 2,214 mm
t = 9.5 mm
Design thickness, (at 90 C) UG-27(c)(1)
t = P*R / (S*E - 0.60*P) + Corrosion= 11.56*320.7 / (1,407.21*1.00 - 0.60*11.56) + 3.2= 5.85 mm
Maximum allowable working pressure, (at 90 C) UG-27(c)(1)
P = S*E*t / (R + 0.60*t) - Ps= 1,407.21*1.00*6.3 / (320.7 + 0.60*6.3) - 0.06= 27.26 kg/cm2
Maximum allowable pressure, (at 21.11 C) UG-27(c)(1)
P = S*E*t / (R + 0.60*t)= 1,407.21*1.00*9.5 / (317.5 + 0.60*9.5)= 41.36 kg/cm2
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% Extreme fiber elongation - UCS-79(d)
EFE = (50*t / Rf)*(1 - Rf/ Ro)= (50*9.5 / 322.25)*(1 - 322.25 / infinity)
= 1.474%
The extreme fiber elongation does not exceed 5%.
Allowable Compressive Stress, Hot and Corroded- ScHC, (table CS-2Metric)
A = 0.125 / (Ro/ t)
= 0.125 / (327 / 6.3)
= 0.002408B = 1,091.4 kg/cm2
S = 1,407.2 / 1.00 = 1,407.2 kg/cm2
ScHC = min(B, S) = 1,091.4 kg/cm2
Allowable Compressive Stress, Hot and New- ScHN, (table CS-2 Metric)
A = 0.125 / (Ro/ t)
= 0.125 / (327 / 9.5)
= 0.003631B = 1,169 kg/cm2
S = 1,407.2 / 1.00 = 1,407.2 kg/cm2
ScHN = min(B, S) = 1,169 kg/cm2
Allowable Compressive Stress, Cold and New- ScCN, (table CS-2 Metric)
A = 0.125 / (Ro/ t)
= 0.125 / (327 / 9.5)= 0.003631
B = 1,169 kg/cm2
S = 1,407.2 / 1.00 = 1,407.2 kg/cm2
ScCN = min(B, S) = 1,169 kg/cm2
Allowable Compressive Stress, Cold and Corroded- ScCC, (table CS-2Metric)
A = 0.125 / (Ro/ t)
= 0.125 / (327 / 6.3)
= 0.002408B = 1,091.4 kg/cm2
S = 1,407.2 / 1.00 = 1,407.2 kg/cm2
ScCC = min(B, S) = 1,091.4 kg/cm2
Allowable Compressive Stress, Vacuum and Corroded- ScVC, (tableCS-2 Metric)
A = 0.125 / (Ro/ t)
= 0.125 / (327 / 6.3)
= 0.002408
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B = 1,091.4 kg/cm2
S = 1,407.2 / 1.00 = 1,407.2 kg/cm2
ScVC = min(B, S) = 1,091.4 kg/cm2
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ENVOLVENTE 2
ASME Section VIII Division 1, 2010 Edition, A11 Addenda Metric
Component: CylinderMaterial specification: SA-516 70 (II-D Metric p. 18, ln. 19)Material impact test exemption temperature from Fig UCS-66M Curve D = -48 C17 C MDMT reduction per UCS-68(c) applies.Fig UCS-66.1M MDMT reduction = 45.3 C, (coincident ratio = 0.4207)
Rated MDMT of -110.3C is limited to -48C by UCS-66(b)(2)UCS-66 governing thickness = 9.5 mm
Internal design pressure: P = 11.5 kg/cm2@ 90 C
Static liquid head:
Ps = 0.06 kg/cm2 (SG = 1, Hs= 638.2 mm,Operating head)
Pth = 0.09 kg/cm2 (SG = 1, Hs= 907.5 mm, Horizontal test
head)
Corrosion allowance Inner C = 3.2 mm Outer C = 0 mm
Design MDMT = -17.78 C No impact test performedRated MDMT = -48 C Material is normalized
Material is not produced to Fine Grain PracticePWHT is performed
Radiography: Longitudinal joint - Full UW-11(a) Type 1Left circumferential joint - Full UW-11(a) Type 1Right circumferential joint - Full UW-11(a) Type 1
Estimated weight New = 331.9 kg corr = 221.2 kg
Capacity New = 468.9 liters corr = 483.1 liters
ID = 635 mmLengthLc
= 2,214 mm
t = 9.5 mm
Design thickness, (at 90 C) UG-27(c)(1)
t = P*R / (S*E - 0.60*P) + Corrosion= 11.56*320.7 / (1,407.21*1.00 - 0.60*11.56) + 3.2= 5.85 mm
Maximum allowable working pressure, (at 90 C) UG-27(c)(1)
P = S*E*t / (R + 0.60*t) - Ps= 1,407.21*1.00*6.3 / (320.7 + 0.60*6.3) - 0.06= 27.26 kg/cm2
Maximum allowable pressure, (at 21.11 C) UG-27(c)(1)
P = S*E*t / (R + 0.60*t)= 1,407.21*1.00*9.5 / (317.5 + 0.60*9.5)= 41.36 kg/cm2
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% Extreme fiber elongation - UCS-79(d)
EFE = (50*t / Rf)*(1 - Rf/ Ro)= (50*9.5 / 322.25)*(1 - 322.25 / infinity)
= 1.474%
The extreme fiber elongation does not exceed 5%.
Allowable Compressive Stress, Hot and Corroded- ScHC, (table CS-2Metric)
A = 0.125 / (Ro/ t)
= 0.125 / (327 / 6.3)
= 0.002408B = 1,091.4 kg/cm2
S = 1,407.2 / 1.00 = 1,407.2 kg/cm2
ScHC = min(B, S) = 1,091.4 kg/cm2
Allowable Compressive Stress, Hot and New- ScHN, (table CS-2 Metric)
A = 0.125 / (Ro/ t)
= 0.125 / (327 / 9.5)
= 0.003631B = 1,169 kg/cm2
S = 1,407.2 / 1.00 = 1,407.2 kg/cm2
ScHN = min(B, S) = 1,169 kg/cm2
Allowable Compressive Stress, Cold and New- ScCN, (table CS-2 Metric)
A = 0.125 / (Ro/ t)
= 0.125 / (327 / 9.5)= 0.003631
B = 1,169 kg/cm2
S = 1,407.2 / 1.00 = 1,407.2 kg/cm2
ScCN = min(B, S) = 1,169 kg/cm2
Allowable Compressive Stress, Cold and Corroded- ScCC, (table CS-2Metric)
A = 0.125 / (Ro/ t)
= 0.125 / (327 / 6.3)
= 0.002408B = 1,091.4 kg/cm2
S = 1,407.2 / 1.00 = 1,407.2 kg/cm2
ScCC = min(B, S) = 1,091.4 kg/cm2
Allowable Compressive Stress, Vacuum and Corroded- ScVC, (tableCS-2 Metric)
A = 0.125 / (Ro/ t)
= 0.125 / (327 / 6.3)
= 0.002408
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B = 1,091.4 kg/cm2
S = 1,407.2 / 1.00 = 1,407.2 kg/cm2
ScVC = min(B, S) = 1,091.4 kg/cm2
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Rear Shell Cylinder
ASME Section VIII Division 1, 2010 Edition, A11 Addenda Metric
Component: CylinderMaterial specification: SA-516 70 (II-D Metric p. 18, ln. 19)Material impact test exemption temperature from Fig UCS-66M Curve B = -29 C17 C MDMT reduction per UCS-68(c) applies.Fig UCS-66.1M MDMT reduction = 35.3 C, (coincident ratio = 0.4707)
Rated MDMT of -81.3C is limited to -48C by UCS-66(b)(2)UCS-66 governing thickness = 9.5 mm
Internal design pressure: P = 11.5 kg/cm2@ 90 C
Static liquid head:
Ps = 0.07 kg/cm2 (SG = 1, Hs= 676.2 mm,Operating head)
Pth = 0.09 kg/cm2 (SG = 1, Hs= 945.5 mm, Horizontal test
head)
Corrosion allowance Inner C = 3.2 mm Outer C = 0 mm
Design MDMT = -17.78 C No impact test performedRated MDMT = -48 C Material is not normalized
Material is not produced to Fine Grain PracticePWHT is performed
Radiography: Longitudinal joint - Full UW-11(a) Type 1Left circumferential joint - Full UW-11(a) Type 1Right circumferential joint - Full UW-11(a) Type 1
Estimated weight New = 40.9 kg corr = 27.3 kg
Capacity New = 50.12 liters corr = 52.84 liters
ID = 711 mmLengthLc
= 243 mm
t = 9.5 mm
Design thickness, (at 90 C) UG-27(c)(1)
t = P*R / (S*E - 0.60*P) + Corrosion= 11.57*358.7 / (1,407.21*1.00 - 0.60*11.57) + 3.2= 6.16 mm
Maximum allowable working pressure, (at 90 C) UG-27(c)(1)
P = S*E*t / (R + 0.60*t) - Ps= 1,407.21*1.00*6.3 / (358.7 + 0.60*6.3) - 0.07= 24.39 kg/cm2
Maximum allowable pressure, (at 21.11 C) UG-27(c)(1)
P = S*E*t / (R + 0.60*t)= 1,407.21*1.00*9.5 / (355.5 + 0.60*9.5)= 37.01 kg/cm2
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% Extreme fiber elongation - UCS-79(d)
EFE = (50*t / Rf)*(1 - Rf/ Ro)= (50*9.5 / 360.25)*(1 - 360.25 / infinity)
= 1.3185%
The extreme fiber elongation does not exceed 5%.
Allowable Compressive Stress, Hot and Corroded- ScHC, (table CS-2Metric)
A = 0.125 / (Ro/ t)
= 0.125 / (365 / 6.3)
= 0.002157B = 1,066.9 kg/cm2
S = 1,407.2 / 1.00 = 1,407.2 kg/cm2
ScHC = min(B, S) = 1,066.9 kg/cm2
Allowable Compressive Stress, Hot and New- ScHN, (table CS-2 Metric)
A = 0.125 / (Ro/ t)
= 0.125 / (365 / 9.5)
= 0.003253B = 1,153.4 kg/cm2
S = 1,407.2 / 1.00 = 1,407.2 kg/cm2
ScHN = min(B, S) = 1,153.4 kg/cm2
Allowable Compressive Stress, Cold and New- ScCN, (table CS-2 Metric)
A = 0.125 / (Ro/ t)
= 0.125 / (365 / 9.5)= 0.003253
B = 1,153.4 kg/cm2
S = 1,407.2 / 1.00 = 1,407.2 kg/cm2
ScCN = min(B, S) = 1,153.4 kg/cm2
Allowable Compressive Stress, Cold and Corroded- ScCC, (table CS-2Metric)
A = 0.125 / (Ro/ t)
= 0.125 / (365 / 6.3)
= 0.002157B = 1,066.9 kg/cm2
S = 1,407.2 / 1.00 = 1,407.2 kg/cm2
ScCC = min(B, S) = 1,066.9 kg/cm2
Allowable Compressive Stress, Vacuum and Corroded- ScVC, (tableCS-2 Metric)
A = 0.125 / (Ro/ t)
= 0.125 / (365 / 6.3)
= 0.002157
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B = 1,066.9 kg/cm2
S = 1,407.2 / 1.00 = 1,407.2 kg/cm2
ScVC = min(B, S) = 1,066.9 kg/cm2
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TAPA BRIDADA CANAL
ASME Section VIII Division 1, 2010 Edition, A11 Addenda Metric
Component: Bolted CoverAttached to: BRIDA TAPA DEL CANALMaterial specification: SA-516 70 (II-D Metric p. 18, ln. 19)Bolted cover impact test exemption temperature from Fig UCS-66M Curve D = -48 C17 C MDMT reduction per UCS-68(c) applies.
Rated MDMT of -65C is limited to -48C by UCS-66(b)(2)UCS-66 governing thickness = 8 mm
Internal design pressure: P = 7 kg/cm2@ 66 C
Static liquid head:
Ps = 0.06 kg/cm2 (SG = 1, Hs= 638.17 mm, Operating head)
Pth = 0.09 kg/cm2 (SG = 1, Hs= 907.5 mm, Horizontal testhead)
Corrosion allowance: Inner C = 0 mm Outer C = 0 mm
Design MDMT = -17.78 C No impact test performedRated MDMT = -48 C Material is normalized
Material is not produced to Fine Grain PracticePWHT is performed
Radiography: Category A joints - Seamless No RT
Estimated weight: New = 122.2 kg corr = 122.2 kg
Head diameter, d = 675 mm
Cover thickness, t = 32 mmDesign thickness, (at 66 C) UG-34 (c)(2), flange operating
t = d*Sqr(C*P / (S*E) + 1.9*W*hG/ (S*E*d3)) + Corrosion
= 675*Sqr(0.3*7.06 / (1,407.207*1) + 100*1.9*30,880.81*29 / (1,407.207*1*6753)) + 0= 29.42 mm
Design thickness, (at 21.11 C) UG-34 (c)(2), gasket seating
t = d*Sqr(1.9*W*hG/ (S*E*d3)) + Corrosion
= 10*675*Sqr(1.9*80,471.86*29 / (1,407.207*1*6753)) + 0= 21.61 mm
Maximum allowable working pressure, (at 66 C )
P = (S*E / C)*((t / d)2- (1.9*W*hG/ (S*E*d3))) - Ps= (1,407.207*1 / 0.3)*((32 / 675)2- (1.9*100*36,546.12*29 / (1,407.207*1*6753))) - 0.0638= 8.3 kgf/cm
2
Maximum allowable pressure, (At 21.11 C )
P = (S*E / C)*((t / d)2- (1.9*W*hG/ (S*E*d3)))
= (1,407.207*1 / 0.3)*((32 / 675)2- (1.9*100*36,546.12*29 / (1,407.207*1*6753)))= 8.36 kgf/cm
2
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% Extreme fiber elongation - UCS-79(d)
EFE = (50*t / Rf)*(1 - Rf/ Ro)= (50*9.5 / 360.25)*(1 - 360.25 / infinity)
= 1.3185%
The extreme fiber elongation does not exceed 5%.
Allowable Compressive Stress, Hot and Corroded- ScHC, (table CS-2Metric)
A = 0.125 / (Ro/ t)
= 0.125 / (365 / 6.3)
= 0.002157B = 1,066.9 kg/cm2
S = 1,407.2 / 1.00 = 1,407.2 kg/cm2
ScHC = min(B, S) = 1,066.9 kg/cm2
Allowable Compressive Stress, Hot and New- ScHN, (table CS-2 Metric)
A = 0.125 / (Ro/ t)
= 0.125 / (365 / 9.5)
= 0.003253B = 1,153.4 kg/cm2
S = 1,407.2 / 1.00 = 1,407.2 kg/cm2
ScHN = min(B, S) = 1,153.4 kg/cm2
Allowable Compressive Stress, Cold and New- ScCN, (table CS-2 Metric)
A = 0.125 / (Ro/ t)
= 0.125 / (365 / 9.5)= 0.003253
B = 1,153.4 kg/cm2
S = 1,407.2 / 1.00 = 1,407.2 kg/cm2
ScCN = min(B, S) = 1,153.4 kg/cm2
Allowable Compressive Stress, Cold and Corroded- ScCC, (table CS-2Metric)
A = 0.125 / (Ro/ t)
= 0.125 / (365 / 6.3)
= 0.002157B = 1,066.9 kg/cm2
S = 1,407.2 / 1.00 = 1,407.2 kg/cm2
ScCC = min(B, S) = 1,066.9 kg/cm2
Allowable Compressive Stress, Vacuum and Corroded- ScVC, (tableCS-2 Metric)
A = 0.125 / (Ro/ t)
= 0.125 / (365 / 6.3)
= 0.002157
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B = 1,066.9 kg/cm2
S = 1,407.2 / 1.00 = 1,407.2 kg/cm2
ScVC = min(B, S) = 1,066.9 kg/cm2
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Rear Shell Head
ASME Section VIII Division 1, 2010 Edition, A11 Addenda Metric
Component: Ellipsoidal HeadMaterial Specification: SA-516 70 (II-D Metric p.18, ln. 19)Straight Flangegoverns MDMT
Internal design pressure: P = 11.5 kg f/cm2
@ 90 C
Static liquid head:
Ps= 0.07 kgf/cm2(SG=1, Hs=676.2 mm Operating head)
Pth= 0.09 kgf/cm2(SG=1, Hs=945.5 mm Horizontal test head)
Corrosion allowance: Inner C = 3.2 mm Outer C = 0 mm
Design MDMT = -17.78C No impact test performedRated MDMT = -48C Material is not normalized
Material is not produced to fine grain practicePWHT is performed
Do not Optimize MDMT / Find MAWP
Radiography: Category A joints - Seamless No RTHead to shell seam - Full UW-11(a) Type 1
Estimated weight*: new = 53.4 kg corr = 35.7 kgCapacity*: new = 63.7 liters corr = 66 liters* includes straight flange
Inner diameter = 711 mmMinimum head thickness = 9.5 mmHead ratio D/2h = 2 (new)Head ratio D/2h = 1.9823 (corroded)Straight flange length Lsf = 50.8 mmNominal straight flange thickness tsf = 9.5 mmResults Summary
The governing condition is internal pressure.Minimum thickness per UG-16 = 1.5 mm + 3.2 mm= 4.7 mmDesign thickness due to internal pressure (t) = 6.12mmMaximum allowable working pressure (MAWP) = 24.9kgf/cm
2
Maximum allowable pressure (MAP) = 37.5kgf/cm2
K (Corroded)K=(1/6)*[2 + (D / (2*h))2]=(1/6)*[2 + (717.4 / (2*180.95))2]=0.988261
K (New)
K=(1/6)*[2 + (D / (2*h))2]=(1/6)*[2 + (711 / (2*177.75))2]=1
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Design thickness for internal pressure, (Corroded at 90 C) Appendix 1-4(c)
t = P*D*K / (2*S*E - 0.2*P) + Corrosion= 11.57*717.4*0.988261 / (2*1,407.21*1 - 0.2*11.57) + 3.2= 6.12 mm
The head internal pressure design thickness is 6.12mm.
Maximum allowable working pressure, (Corroded at 90 C) Appendix 1-4(c)
P = 2*S*E*t / (K*D + 0.2*t) - Ps= 2*1,407.21*1*6.3 / (0.988261*717.4 +0.2*6.3) - 0.07= 24.9 kgf/cm
2
The maximum allowable working pressure (MAWP) is 24.9kgf/cm2.
Maximum allowable pressure, (New at 21.11 C) Appendix 1-4(c)
P = 2*S*E*t / (K*D + 0.2*t) - Ps= 2*1,407.21*1*9.5 / (1*711 +0.2*9.5) - 0= 37.5 kgf/cm
2
The maximum allowable pressure (MAP) is 37.5kgf/cm2.
% Extreme fiber elongation - UCS-79(d)
EFE = (75*t / Rf)*(1 - Rf/ Ro)
= (75*9.5 / 125.62)*(1 - 125.62 / infinity)= 5.6719%
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BRIDA BIPARTIDA
ASME VIII-1, 2010 Edition, A11 Addenda Metric, Appendix 2 Flange Calculations
Flange is attached to: Rear Floating TubesheetFlange type: Lap joint loose
Flange material specification: SA-105 (II-D Metric p. 18, ln. 5)
Bolt material specification:SA-193 B7 Bolt
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UCS-66(b)(1)(b) has been applied.Flange impact test exemption temperature from Fig UCS-66M Curve B = -19.38 C
Fig UCS-66.1M MDMT reduction = 26 C, (coincident ratio = 0.5614)UCS-66 governing thickness = 13.75 mmBolts rated MDMT per Fig UCS-66 note (c) = -48 C
The rated flange MDMT is -45.38 C
Flange calculations for Internal Pressure + Weight Only
Gasket details from facing sketch 1(a) or (b), Column II
Gasket width N = 10 mm
b0= N/2 = 5 mm
Effective gasket seating width, b = b0= 5 mm
hG= (C - G)/2 = (660 - 619)/2 = 20.5 mm
hD= (C - B)/2 = (660 - 608)/2 = 26 mm
hT= (C - G)/2 = (660 - 619)/2 = 20.5 mm
Hp= 2*b*3.14*G*m*P= 0.01*2*5*3.14*619*3.75*7
= 5,102.11 kgf
H = 0.785*G2*P
= 0.01*0.785*6192*7= 21,054.7 kgf
HD= 0.785*B2*P
= 0.01*0.785*6082*7
= 20,313.04 kgf
HT= H - HD= 21,054.7 - 20,313.04
= 741.66 kgf
Wm1= H + Hp= 21,054.7 + 5,102.11
= 26,156.81 kgf
Wm2= 3.14*b*G*y
= 0.01*3.14*5*619*534.3324= 51,928.08 kgf
Required bolt area, Am= greater of Am1, Am2= 29.607 cm2
Am1= Wm1/Sb= 26,156.81/1,753.911 = 14.9134 cm2
Am2= Wm2/Sa= 51,928.08/1,753.911 = 29.607 cm2
Total area for 32- 0.625 in dia bolts, corroded, Ab= 41.7031 cm2
W = (Am+ Ab)*Sa/2
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= (29.607 + 41.7031)*1,753.911/2= 62,535.86 kgf
MD= HD*hD= 20,313.04*0.026 = 528.1 kgf-mMT= HT*hT= 741.66*0.0205 = 15.2 kgf-m
HG= Wm1- H = 26,156.81 - 21,054.7 = 5,102.11 kgf
MG= HG*hG= 5,102.11*0.0205 = 104.6 kgf-m
Mo= MD+ MT+ MG= 528.1 + 15.2 + 104.6 = 647.9 kgf-m
Mg= W*hG= 62,535.86*0.0205 = 1,282 kgf-m
From FIG. 2-7.1, where K = A/B = 700/608 = 1.1513, Y = 13.8319
Stresses at operating conditions - VIII-1 Appendix 2-7
SR= SH= 0
ST= Y*Mo/(t2*B)
= 1e5*13.8319*647.9/(552*608)
= 487.287 kgf/cm2
Allowable stress Sfo= 1,407.207 kgf/cm2
STdoes not exceed Sfo
Stresses at gasket seating - VIII-1 Appendix 2-7
ST= Y*Mg/(t2*B)
= 1e5*13.8319*1,282/(552*608)
= 964.13 kgf/cm2
Allowable stress Sfa
= 1,407.207 kgf
/cm2
STdoes not exceed Sfa
Flange rigidity per VIII-1 Appendix 2-14
J = 109.4*Mo/(E*t3*KL*ln(K))
= 109.4*1,282/(20.52E+05*553*0.3*ln(1.1513))
= 0.9718
The flange rigidity index J does not exceed 1; satisfactory.
Flange calculations for External Pressure + Weight Only per VIII-1, Appendix 2-11
Gasket details from facing sketch 1(a) or (b), Column II
Gasket width N = 10 mm
b0= N/2 = 5 mm
Effective gasket seating width, b = b0= 5 mm
hG= (C - G)/2 = (660 - 619)/2 = 20.5 mm
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hD= (C - B)/2 = (660 - 608)/2 = 26 mm
hT= (C - G)/2 = (660 - 619)/2 = 20.5 mm
Hp= 2*b*3.14*G*m*P= 0.01*2*5*3.14*619*3.75*11.5
= 8,382.03 kgf
H = 0.785*G2
*P= 0.01*0.785*6192*11.5= 34,589.86 kgf
HD= 0.785*B2*P
= 0.01*0.785*6082*11.5= 33,371.42 kgf
HT= H - HD= 34,589.86 - 33,371.42
= 1,218.44 kgf
Wm1= H + Hp
= 34,589.86 + 8,382.03= 42,971.89 kgf
Wm2= 3.14*b*G*y= 0.01*3.14*5*619*534.3324= 51,928.08 kgf
Required bolt area, Am= greater of Am1, Am2= 29.607 cm2
Am1= 0.785*G2*(Pm- Pr)/Sb= 0/1,753.911 = 0 cm
2
Am2= Wm2/Sa= 51,928.08/1,753.911 = 29.607 cm2
Total area for 32- 0.625 in dia bolts, corroded, Ab= 41.7031 cm2
W = (Am2+ Ab)*Sa/2= (29.607 + 41.7031)*1,753.911/2
= 62,535.86 kgf
Mo= HD*(hD- hG) + HT*(hT- hG)
= 33,371.42*(0.026 - 0.0205) + 1,218.44*(0.0205 - 0.0205)= 183.5 kgf-m
Mg= W*hG= 62,535.86*0.0205 = 1,282 kgf-m
From FIG. 2-7.1, where K = A/B = 700/608 = 1.1513, Y = 13.8319
Stresses at operating conditions - VIII-1 Appendix 2-7
SR= SH= 0
ST= Y*Mo/(t2*B)
= 1e5*13.8319*183.5/(552*608)= 138.035 kgf/cm
2
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Allowable stress Sfo= 1,407.207 kgf/cm2
STdoes not exceed Sfo
Stresses at gasket seating - VIII-1 Appendix 2-7
ST= Y*Mg/(t2*B)
= 1e5*13.8319*1,282/(552*608)= 964.13 kgf/cm
2
Allowable stress Sfa= 1,407.207 kgf/cm2
STdoes not exceed Sfa
Flange rigidity per VIII-1 Appendix 2-14
J = 109.4*Mo/(E*t3*KL*ln(K))
= 109.4*1,282/(20.52E+05*553*0.3*ln(1.1513))= 0.9718
The flange rigidity index J does not exceed 1; satisfactory.
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BRIDA BONET -- CUERPO
ASME VIII-1, 2010 Edition, A11 Addenda Metric, Appendix 2 Flange Calculations
Flange is attached to: Rear Shell Cylinder (Left)Flange type: Weld neck integralFlange material specification: SA-105 (II-D Metric p. 18, ln. 5)
Bolt material specification:SA-193 B7 Bolt
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17 C MDMT reduction per UCS-68(c) applies.Fig UCS-66.1M MDMT reduction = 12.4 C, (coincident ratio = 0.779)Rated MDMT of -58.4C is limited to -48C by UCS-66(b)(2)UCS-66 governing thickness = 9.5 mmBolts rated MDMT per Fig UCS-66 note (c) = -48 C
The rated flange MDMT is -48 C
Flange calculations for Internal Pressure + Weight Only
Gasket details from facing sketch 1(a) or (b), Column II
Gasket width N = 13 mm
b0= N/2 = 6.5 mm
Effective gasket seating width, b = 2.5*b01/2= 6.37 mm
G = gasket OD - 2*b = 743 - 2*6.37 = 730.25 mm
hG= (C - G)/2 = (799 - 730.25)/2 = 34.37 mm
hD= R + g1/2 = 25 + 15.83/2 = 32.92 mm
hT= (R + g1+ hG)/2 = (25 + 15.83 + 34.37)/2 = 37.6 mm
Hp= 2*b*3.14*G*m*P= 0.01*2*6.37*3.14*730.25*3.75*11.5675= 12,677.72 kgf
H = 0.785*G2*P= 0.01*0.785*730.252*11.5675= 48,423.88 kgf
HD= 0.785*B2
*P= 0.01*0.785*717.342*11.5675= 46,726.29 kgf
HT= H - HD= 48,423.88 - 46,726.29= 1,697.59 kgf
Wm1= H + Hp= 48,423.88 + 12,677.72= 61,101.6 kgf
Wm2= 3.14*b*G*y
= 0.01*3.14*6.37*730.25*534.3324= 78,081.84 kgf
Required bolt area, Am= greater of Am1, Am2= 44.5187 cm2
Am1= Wm1/Sb= 61,101.6/1,753.911 = 34.8373 cm2
Am2= Wm2/Sa= 78,081.84/1,753.911 = 44.5187 cm2
Total area for 26- 0.875 in dia bolts, corroded, Ab= 48.1251 cm2
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W = (Am+ Ab)*Sa/2= (44.5187 + 70.2837)*1,753.911/2= 100,676.66 kgf
MD= HD*hD= 46,726.29*0.0329 = 1,538 kgf-mMT= HT*hT= 1,697.59*0.0376 = 63.8 kgf-m
HG= Wm1- H = 61,101.6 - 48,423.88 = 12,677.72 kgf
MG= HG*hG= 12,677.72*0.0344 = 435.8 kgf-m
Mo= MD+ MT+ MG= 1,538 + 63.8 + 435.8 = 2,037.6 kgf-m
Mg= W*hG= 100,676.66*0.0344 = 3,460.5 kgf-m
The bolts are adequately spaced so the TEMA RCB-11.23 load concentration factor does not apply.
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Hub and Flange Factors
g0= min(g0, tn) = min(6.33, 6.3) = 6.3
h0= (B*g0)1/2= (717.34*6.3)1/2= 67.22 mm
From FIG. 2-7.1, where K = A/B = 854/717.34 = 1.1905
T = 1.8428 Z = 5.7926 Y = 11.2272 U = 12.3376
h/h0= 0.476 g1/g0= 2.5129
F = 0.8234 V = 0.1921 e = F/h0= 0.1225
d = (U/V)*h0*g02= (12.3376/0.1921)*6.7223*0.632
= 171.3114 cm3
Stresses at operating conditions - VIII-1 Appendix 2-7
f = 2.1263
L = (t*e + 1)/T + t3/d
= (6*0.1225 + 1)/1.8428 + 63
/171.3114= 2.2023
SH= f*Mo/(L*g12*B)
= 1e5*2.1263*2,037.6/(2.2023*15.832*717.34)= 1,094.397 kgf/cm
2
SR= (1.33*t*e + 1)*Mo/(L*t2*B)
= (1.33*60*0.0122 + 1)*1e5*2,037.6/(2.2023*602*717.34)= 70.845 kgf/cm
2
ST= Y*Mo/(t2*B) - Z*SR
= 1e5*11.2272*2,037.6/(602*717.34) - 5.7926*70.845
= 475.482 kgf/cm2
Allowable stress Sfo= 1,407.207 kgf/cm2
Allowable stress Sno= 1,407.207 kgf/cm2
STdoes not exceed SfoSHdoes not exceed Min[ 1.5*Sfo, 2.5*Sno] = 2,110.811 kgf/cm
2
SRdoes not exceed Sfo0.5(SH+ SR) = 582.621 kgf/cm
2does not exceed Sfo0.5(SH+ ST) = 784.94 kgf/cm
2does not exceed Sfo
Stresses at gasket seating - VIII-1 Appendix 2-7
SH= f*Mg/(L*g12*B)= 1e5*2.1263*3,460.5/(2.2023*15.832*717.34)= 1,858.663 kgf/cm
2
SR= (1.33*t*e + 1)*Mg/(L*t2*B)
= (1.33*60*0.0122 + 1)*1e5*3,460.5/(2.2023*602*717.34)= 120.319 kgf/cm
2
ST= Y*Mg/(t2*B) - Z*SR
= 11.2272*1e5*3,460.5/(602*717.34) - 5.7926*120.319
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= 807.533 kgf/cm2
Allowable stress Sfa= 1,407.207 kgf/cm2
Allowable stress Sna= 1,407.207 kgf/cm2
STdoes not exceed SfaSHdoes not exceed Min[ 1.5*Sfa, 2.5*Sna] = 2,110.811 kgf/cm
2
SRdoes not exceed Sfa0.5(SH+ SR) = 989.491 kgf/cm
2does not exceed Sfa
0.5(SH+ ST) = 1,333.098 kgf/cm2
does not exceed Sfa
Flange rigidity per VIII-1 Appendix 2-14
J = 52.14*V*Mo/(L*E*g02*KI*h0)
= 1e5*52.14*0.1921*3,460.5/(2.2023*20.52E+05*6.32*0.3*67.22)= 0.9585
The flange rigidity index J does not exceed 1; satisfactory.
BRIDA BONET -- CUERPO - Flange hub
ASME Section VIII Division 1, 2010 Edition, A11 Addenda Metric
Component: Flange hubMaterial specification: SA-105 (II-D Metric p. 18, ln. 5)Material impact test exemption temperature from Fig UCS-66M Curve B = -29 C17 C MDMT reduction per UCS-68(c) applies.Fig UCS-66.1M MDMT reduction = 35.7 C, (coincident ratio = 0.4684)Rated MDMT of -81.7C is limited to -48C by UCS-66(b)(2)UCS-66 governing thickness = 9.5 mm
Internal design pressure: P = 11.5 kg/cm2@ 90 C
Static liquid head:
Ps = 0.07 kg/cm2 (SG = 1, Hs= 676.17 mm,Operating head)
Pth = 0.09 kg/cm2 (SG = 1, Hs= 945.5 mm, Horizontal test
head)
Corrosion allowance Inner C = 3.17 mm Outer C = 0 mm
Design MDMT = -17.78 C No impact test performedRated MDMT = -48 C Material is normalized
Material is not produced to Fine Grain PracticePWHT is performed
Radiography: Longitudinal joint - Seamless No RT
Left circumferential joint - N/ARight circumferential joint - Full UW-11(a) Type 1
Estimated weight New = 5.3 kg corr = 3.6 kg
Capacity New = 12.71 liters corr = 12.93 liters
ID = 711 mmLengthLc
= 32 mm
t = 9.5 mm
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Design thickness, (at 90 C) UG-27(c)(1)
t = P*R / (S*E - 0.60*P) + Corrosion= 11.57*358.67 / (1,407.21*1.00 - 0.60*11.57) + 3.17= 6.13 mm
Maximum allowable working pressure, (at 90 C) UG-27(c)(1)
P = S*E*t / (R + 0.60*t) - Ps
= 1,407.21*1.00*6.33 / (358.67 + 0.60*6.33) - 0.07= 24.51 kg/cm2
Maximum allowable pressure, (at 21.11 C) UG-27(c)(1)
P = S*E*t / (R + 0.60*t)= 1,407.21*1.00*9.5 / (355.5 + 0.60*9.5)= 37.01 kg/cm2
Allowable Compressive Stress, Hot and Corroded- ScHC, (table CS-2Metric)
A = 0.125 / (Ro/ t)= 0.125 / (365 / 6.33)
= 0.002168B = 1,067.9 kg/cm2
S = 1,407.2 / 1.00 = 1,407.2 kg/cm2
ScHC = min(B, S) = 1,067.9 kg/cm2
Allowable Compressive Stress, Hot and New- ScHN, (table CS-2 Metric)
A = 0.125 / (Ro/ t)
= 0.125 / (365 / 9.5)
= 0.003253B = 1,153.4 kg/cm2
S = 1,407.2 / 1.00 = 1,407.2 kg/cm2
ScHN = min(B, S) = 1,153.4 kg/cm2
Allowable Compressive Stress, Cold and New- ScCN, (table CS-2 Metric)
A = 0.125 / (Ro/ t)
= 0.125 / (365 / 9.5)= 0.003253
B = 1,153.4 kg/cm2
S = 1,407.2 / 1.00 = 1,407.2 kg/cm2
ScCN = min(B, S) = 1,153.4 kg/cm2
Allowable Compressive Stress, Cold and Corroded- ScCC, (table CS-2Metric)
A = 0.125 / (Ro/ t)
= 0.125 / (365 / 6.33)
= 0.002168B = 1,067.9 kg/cm2
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S = 1,407.2 / 1.00 = 1,407.2 kg/cm2
ScCC = min(B, S) = 1,067.9 kg/cm2
Allowable Compressive Stress, Vacuum and Corroded- ScVC, (tableCS-2 Metric)
A = 0.125 / (Ro/ t)
= 0.125 / (365 / 6.33)
= 0.002168B = 1,067.9 kg/cm2
S = 1,407.2 / 1.00 = 1,407.2 kg/cm2
ScVC = min(B, S) = 1,067.9 kg/cm2
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BRIDA CANAL --ESPEJO
ASME VIII-1, 2010 Edition, A11 Addenda Metric, Appendix 2 Flange Calculations
Flange is attached to: ENVOLVENTE CANAL (Right)Flange type: Weld neck integralFlange material specification: SA-105 (II-D Metric p. 18, ln. 5)
Bolt material specification:SA-193 B7 Bolt
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Bolts rated MDMT per Fig UCS-66 note (c) = -48 C
The rated flange MDMT is -48 C
Flange calculations for Internal Pressure + Weight Only
Gasket details from facing sketch 1(a) or (b), Column II
Gasket width N = 10 mm
b0= N/2 = 5 mm
Effective gasket seating width, b = b0= 5 mm
G = (gasket OD + gasket ID) / 2 = (685 + 665) / 2 = 675 mm
hG= (C - G)/2 = (733 - 675)/2 = 29 mm
hD= R + g1/2 = 35 + 10.83/2 = 40.42 mm
hT= (R + g1+ hG)/2 = (35 + 10.83 + 29)/2 = 37.42 mm
Hp= 2*P*(b*3.14*G*m + br*rl*m')= 0.01*2*7.0638*(5*3.14*675*3.75 + 3.17*2*2)= 5,616.16 kgf
H = 0.785*G2*P= 0.01*0.785*6752*7.0638= 25,264.65 kgf
HD= 0.785*B2*P
= 0.01*0.785*641.342*7.0638= 22,807.73 kgf
HT= H - HD= 25,264.65 - 22,807.73= 2,456.91 kgf
Wm1= H + Hp= 25,264.65 + 5,616.16= 30,880.8 kgf
Per VIII-1 Appendix 2-5(a)(2): Wm1from the mating flange governs so Wm1= 50,122.39 kgf
Wm2= 3.14*b*G*y + br*rl*Y'= 0.01*3.14*5*675*534.3324 + 3.17*2*175.767= 56,637.07 kgf
The pass partition gasket load has been included in the calculation of Wm1and Wm2per TEMA RGP-RCB-11.7.
Per VIII-1 Appendix 2-5(a)(2): Wm2from the mating flange governs so Wm2= 71,049.43 kgf
Required bolt area, Am= greater of Am1, Am2= 40.5091 cm2
Am1= Wm1/Sb= 50,122.39/1,753.911 = 28.5775 cm2
Am2= Wm2/Sa= 71,049.43/1,753.911 = 40.5091 cm2
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Total area for 22- 0.875 in dia bolts, corroded, Ab= 41.7857 cm2
W = (Am+ Ab)*Sa/2= (40.5091 + 59.4708)*1,753.911/2= 87,678.03 kgf
MD= HD*hD= 22,807.73*0.0404 = 921.8 kgf-mMT= HT*hT= 2,456.91*0.0374 = 91.9 kgf-m
HG= Wm1- H = 50,122.39 - 25,264.65 = 24,857.75 kgf
MG= HG*hG= 24,857.75*0.029 = 720.9 kgf-m
Mo= MD+ MT+ MG= 921.8 + 91.9 + 720.9 = 1,734.6 kgf-m
Mg= W*hG= 87,678.03*0.029 = 2,542.7 kgf-m
The bolts are adequately spaced so the TEMA RCB-11.23 load concentration factor does not apply.
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Hub and Flange Factors
g0= min(g0, tn) = min(6.33, 6.33) = 6.33
h0= (B*g0)1/2= (641.34*6.33)1/2= 63.72 mm
From FIG. 2-7.1, where K = A/B = 788/641.34 = 1.2287
T = 1.8273 Z = 4.9243 Y = 9.5462 U = 10.4904
h/h0= 0.5022 g1/g0= 1.7109
F = 0.8359 V = 0.2675 e = F/h0= 0.1312
d = (U/V)*h0*g02= (10.4904/0.2675)*6.3716*0.6332
= 100.1071 cm3
Stresses at operating conditions - VIII-1 Appendix 2-7
f = 1
L = (t*e + 1)/T + t3/d
= (6.1*0.1312 + 1)/1.8273 + 6.13
/100.1071= 3.2526
SH= f*Mo/(L*g12*B)
= 1e5*1*1,734.6/(3.2526*10.832*641.34)= 708.945 kgf/cm
2
SR= (1.33*t*e + 1)*Mo/(L*t2*B)
= (1.33*61*0.0131 + 1)*1e5*1,734.6/(3.2526*612*641.34)= 46.131 kgf/cm
2
ST= Y*Mo/(t2*B) - Z*SR
= 1e5*9.5462*1,734.6/(612*641.34) - 4.9243*46.131
= 466.706 kgf/cm2
Allowable stress Sfo= 1,407.207 kgf/cm2
Allowable stress Sno= 1,407.207 kgf/cm2
STdoes not exceed SfoSHdoes not exceed Min[ 1.5*Sfo, 2.5*Sno] = 2,110.811 kgf/cm
2
SRdoes not exceed Sfo0.5(SH+ SR) = 377.538 kgf/cm
2does not exceed Sfo0.5(SH+ ST) = 587.826 kgf/cm
2does not exceed Sfo
Stresses at gasket seating - VIII-1 Appendix 2-7
SH= f*Mg/(L*g12*B)= 1e5*1*2,542.7/(3.2526*10.832*641.34)= 1,039.221 kgf/cm
2
SR= (1.33*t*e + 1)*Mg/(L*t2*B)
= (1.33*61*0.0131 + 1)*1e5*2,542.7/(3.2526*612*641.34)= 67.622 kgf/cm
2
ST= Y*Mg/(t2*B) - Z*SR
= 9.5462*1e5*2,542.7/(612*641.34) - 4.9243*67.622
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= 684.131 kgf/cm2
Allowable stress Sfa= 1,407.207 kgf/cm2
Allowable stress Sna= 1,407.207 kgf/cm2
STdoes not exceed SfaSHdoes not exceed Min[ 1.5*Sfa, 2.5*Sna] = 2,110.811 kgf/cm
2
SRdoes not exceed Sfa0.5(SH+ SR) = 553.422 kgf/cm
2does not exceed Sfa
0.5(SH+ ST) = 861.676 kgf/cm2
does not exceed Sfa
Flange rigidity per VIII-1 Appendix 2-14
J = 52.14*V*Mo/(L*E*g02*KI*h0)
= 1e5*52.14*0.2675*2,542.7/(3.2526*20.52E+05*6.332*0.3*63.72)= 0.6938
The flange rigidity index J does not exceed 1; satisfactory.
BRIDA CANAL --ESPEJO - Flange hub
ASME Section VIII Division 1, 2010 Edition, A11 Addenda Metric
Component: Flange hubMaterial specification: SA-105 (II-D Metric p. 18, ln. 5)Material is impact test exempt to -105 C per UCS-66(b)(3) (coincident ratio = 0.302)
Internal design pressure: P = 7 kg/cm2@ 66 C
Static liquid head:
Ps = 0.06 kg/cm2 (SG = 1, Hs= 638.17 mm,Operating head)
Pth = 0.09 kg/cm2 (SG = 1, Hs= 907.5 mm, Horizontal test
head)
Corrosion allowance Inner C = 3.17 mm Outer C = 0 mm
Design MDMT = -17.78 C No impact test performedRated MDMT = -105 C Material is normalized
Material is not produced to Fine Grain PracticePWHT is performed
Radiography: Longitudinal joint - Seamless No RTLeft circumferential joint - Full UW-11(a) Type 1Right circumferential joint - N/A
Estimated weight New = 4.8 kg corr = 3.2 kg
Capacity New = 10.13 liters corr = 10.34 liters
ID = 635 mmLengthLc
= 32 mm
t = 9.5 mm
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Design thickness, (at 66 C) UG-27(c)(1)
t = P*R / (S*E - 0.60*P) + Corrosion= 7.06*320.67 / (1,407.21*1.00 - 0.60*7.06) + 3.17= 4.79 mm
Maximum allowable working pressure, (at 66 C) UG-27(c)(1)
P = S*E*t / (R + 0.60*t) - Ps
= 1,407.21*1.00*6.33 / (320.67 + 0.60*6.33) - 0.06= 27.39 kg/cm2
Maximum allowable pressure, (at 21.11 C) UG-27(c)(1)
P = S*E*t / (R + 0.60*t)= 1,407.21*1.00*9.5 / (317.5 + 0.60*9.5)= 41.36 kg/cm2
Allowable Compressive Stress, Hot and Corroded- ScHC, (table CS-2Metric)
A = 0.125 / (Ro/ t)= 0.125 / (327 / 6.33)
= 0.002420B = 1,092.5 kg/cm2
S = 1,407.2 / 1.00 = 1,407.2 kg/cm2
ScHC = min(B, S) = 1,092.5 kg/cm2
Allowable Compressive Stress, Hot and New- ScHN, (table CS-2 Metric)
A = 0.125 / (Ro/ t)
= 0.125 / (327 / 9.5)
= 0.003631B = 1,169 kg/cm2
S = 1,407.2 / 1.00 = 1,407.2 kg/cm2
ScHN = min(B, S) = 1,169 kg/cm2
Allowable Compressive Stress, Cold and New- ScCN, (table CS-2 Metric)
A = 0.125 / (Ro/ t)
= 0.125 / (327 / 9.5)= 0.003631
B = 1,169 kg/cm2
S = 1,407.2 / 1.00 = 1,407.2 kg/cm2
ScCN = min(B, S) = 1,169 kg/cm2
Allowable Compressive Stress, Cold and Corroded- ScCC, (table CS-2Metric)
A = 0.125 / (Ro/ t)
= 0.125 / (327 / 6.33)
= 0.002420B = 1,092.5 kg/cm2
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S = 1,407.2 / 1.00 = 1,407.2 kg/cm2
ScCC = min(B, S) = 1,092.5 kg/cm2
Allowable Compressive Stress, Vacuum and Corroded- ScVC, (tableCS-2 Metric)
A = 0.125 / (Ro/ t)
= 0.125 / (327 / 6.33)
= 0.002420B = 1,092.5 kg/cm2
S = 1,407.2 / 1.00 = 1,407.2 kg/cm2
ScVC = min(B, S) = 1,092.5 kg/cm2
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BRIDA CUERPO -- BONETE
ASME VIII-1, 2010 Edition, A11 Addenda Metric, Appendix 2 Flange Calculations
Flange is attached to: ENVOLVENTE 2 (Right)Flange type: Weld neck integralFlange material specification: SA-105 (II-D Metric p. 18, ln. 5)
Bolt material specification:SA-193 B7 Bolt
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17 C MDMT reduction per UCS-68(c) applies.Fig UCS-66.1M MDMT reduction = 12.4 C, (coincident ratio = 0.779)Rated MDMT of -58.4C is limited to -48C by UCS-66(b)(2)UCS-66 governing thickness = 9.5 mmBolts rated MDMT per Fig UCS-66 note (c) = -48 C
The rated flange MDMT is -48 C
Flange calculations for Internal Pressure + Weight Only
Gasket details from facing sketch 1(a) or (b), Column II
Gasket width N = 13 mm
b0= N/2 = 6.5 mm
Effective gasket seating width, b = 2.5*b01/2= 6.37 mm
G = gasket OD - 2*b = 743 - 2*6.37 = 730.25 mm
hG= (C - G)/2 = (799 - 730.25)/2 = 34.37 mm
hD= R + g1/2 = 63 + 15.83/2 = 70.92 mm
hT= (R + g1+ hG)/2 = (63 + 15.83 + 34.37)/2 = 56.6 mm
Hp= 2*b*3.14*G*m*P= 0.01*2*6.37*3.14*730.25*3.75*11.5638= 12,673.56 kgf
H = 0.785*G2*P= 0.01*0.785*730.252*11.5638= 48,407.99 kgf
HD= 0.785*B2
*P= 0.01*0.785*641.342*11.5638= 37,337.5 kgf
HT= H - HD= 48,407.99 - 37,337.5= 11,070.49 kgf
Wm1= H + Hp= 48,407.99 + 12,673.56= 61,081.54 kgf
Per VIII-1 Appendix 2-5(a)(2): Wm1from the mating flange governs so Wm1= 61,101.6 kgf
Wm2= 3.14*b*G*y= 0.01*3.14*6.37*730.25*534.3324= 78,081.84 kgf
Required bolt area, Am= greater of Am1, Am2= 44.5187 cm2
Am1= Wm1/Sb= 61,101.6/1,753.911 = 34.8373 cm2
Am2= Wm2/Sa= 78,081.84/1,753.911 = 44.5187 cm2
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Total area for 26- 0.875 in dia bolts, corroded, Ab= 48.1251 cm2
W = (Am+ Ab)*Sa/2= (44.5187 + 70.2837)*1,753.911/2= 100,676.66 kgf
MD= HD*hD= 37,337.5*0.0709 = 2,647.8 kgf-mMT= HT*hT= 11,070.49*0.0566 = 626.6 kgf-m
HG= Wm1- H = 61,101.6 - 48,407.99 = 12,693.61 kgf
MG= HG*hG= 12,693.61*0.0344 = 436.3 kgf-m
Mo= MD+ MT+ MG= 2,647.8 + 626.6 + 436.3 = 3,710.7 kgf-m
Mg= W*hG= 100,676.66*0.0344 = 3,460.5 kgf-m
The bolts are adequately spaced so the TEMA RCB-11.23 load concentration factor does not apply.
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Hub and Flange Factors
g0= min(g0, tn) = min(6.33, 6.3) = 6.3
h0= (B*g0)1/2= (641.34*6.3)1/2= 63.56 mm
From FIG. 2-7.1, where K = A/B = 854/641.34 = 1.3316
T = 1.7838 Z = 3.5869 Y = 6.9337 U = 7.6194
h/h0= 0.5034 g1/g0= 2.5129
F = 0.8161 V = 0.1837 e = F/h0= 0.1284
d = (U/V)*h0*g02= (7.6194/0.1837)*6.3562*0.632
= 104.6257 cm3
Stresses at operating conditions - VIII-1 Appendix 2-7
f = 1.9795
L = (t*e + 1)/T + t3/d
= (5.3*0.1284 + 1)/1.7838 + 5.33
/104.6257= 2.365
SH= f*Mo/(L*g12*B)
= 1e5*1.9795*3,710.7/(2.365*15.832*641.34)= 1,932.593 kgf/cm
2
SR= (1.33*t*e + 1)*Mo/(L*t2*B)
= (1.33*53*0.0128 + 1)*1e5*3,710.7/(2.365*532*641.34)= 165.914 kgf/cm
2
ST= Y*Mo/(t2*B) - Z*SR
= 1e5*6.9337*3,710.7/(532*641.34) - 3.5869*165.914
= 833.051 kgf/cm2
Allowable stress Sfo= 1,407.207 kgf/cm2
Allowable stress Sno= 1,407.207 kgf/cm2
STdoes not exceed SfoSHdoes not exceed Min[ 1.5*Sfo, 2.5*Sno] = 2,110.811 kgf/cm
2
SRdoes not exceed Sfo0.5(SH+ SR) = 1,049.254 kgf/cm
2does not exceed Sfo0.5(SH+ ST) = 1,382.822 kgf/cm
2does not exceed Sfo
Stresses at gasket seating - VIII-1 Appendix 2-7
SH= f*Mg/(L*g12*B)= 1e5*1.9795*3,460.5/(2.365*15.832*641.34)= 1,802.302 kgf/cm
2
SR= (1.33*t*e + 1)*Mg/(L*t2*B)
= (1.33*53*0.0128 + 1)*1e5*3,460.5/(2.365*532*641.34)= 154.729 kgf/cm
2
ST= Y*Mg/(t2*B) - Z*SR
= 6.9337*1e5*3,460.5/(532*641.34) - 3.5869*154.729
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= 776.889 kgf/cm2
Allowable stress Sfa= 1,407.207 kgf/cm2
Allowable stress Sna= 1,407.207 kgf/cm2
STdoes not exceed SfaSHdoes not exceed Min[ 1.5*Sfa, 2.5*Sna] = 2,110.811 kgf/cm
2
SRdoes not exceed Sfa0.5(SH+ SR) = 978.515 kgf/cm
2does not exceed Sfa
0.5(SH+ ST) = 1,289.596 kgf/cm2
does not exceed Sfa
Flange rigidity per VIII-1 Appendix 2-14
J = 52.14*V*Mo/(L*E*g02*KI*h0)
= 1e5*52.14*0.1837*3,710.7/(2.365*20.14E+05*6.32*0.3*63.56)= 0.9859
The flange rigidity index J does not exceed 1; satisfactory.
BRIDA CUERPO -- BONETE - Flange hub
ASME Section VIII Division 1, 2010 Edition, A11 Addenda Metric
Component: Flange hubMaterial specification: SA-105 (II-D Metric p. 18, ln. 5)Material impact test exemption temperature from Fig UCS-66M Curve B = -29 C17 C MDMT reduction per UCS-68(c) applies.Fig UCS-66.1M MDMT reduction = 45.9 C, (coincident ratio = 0.4186)Rated MDMT of -91.9C is limited to -48C by UCS-66(b)(2)UCS-66 governing thickness = 9.5 mm
Internal design pressure: P = 11.5 kg/cm2@ 90 C
Static liquid head:
Ps = 0.06 kg/cm2 (SG = 1, Hs= 638.17 mm,Operating head)
Pth = 0.09 kg/cm2 (SG = 1, Hs= 907.5 mm, Horizontal test
head)
Corrosion allowance Inner C = 3.17 mm Outer C = 0 mm
Design MDMT = -17.78 C No impact test performedRated MDMT = -48 C Material is normalized
Material is not produced to Fine Grain PracticePWHT is performed
Radiography: Longitudinal joint - Seamless No RT
Left circumferential joint - Full UW-11(a) Type 1Right circumferential joint - N/A
Estimated weight New = 4.8 kg corr = 3.2 kg
Capacity New = 10.13 liters corr = 10.34 liters
ID = 635 mmLengthLc
= 32 mm
t = 9.5 mm
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Design thickness, (at 90 C) UG-27(c)(1)
t = P*R / (S*E - 0.60*P) + Corrosion= 11.56*320.67 / (1,407.21*1.00 - 0.60*11.56) + 3.17= 5.82 mm
Maximum allowable working pressure, (at 90 C) UG-27(c)(1)
P = S*E*t / (R + 0.60*t) - Ps
= 1,407.21*1.00*6.33 / (320.67 + 0.60*6.33) - 0.06= 27.39 kg/cm2
Maximum allowable pressure, (at 21.11 C) UG-27(c)(1)
P = S*E*t / (R + 0.60*t)= 1,407.21*1.00*9.5 / (317.5 + 0.60*9.5)= 41.36 kg/cm2
Allowable Compressive Stress, Hot and Corroded- ScHC, (table CS-2Metric)
A = 0.125 / (Ro/ t)= 0.125 / (327 / 6.33)
= 0.002420B = 1,092.5 kg/cm2
S = 1,407.2 / 1.00 = 1,407.2 kg/cm2
ScHC = min(B, S) = 1,092.5 kg/cm2
Allowable Compressive Stress, Hot and New- ScHN, (table CS-2 Metric)
A = 0.125 / (Ro/ t)
= 0.125 / (327 / 9.5)
= 0.003631B = 1,169 kg/cm2
S = 1,407.2 / 1.00 = 1,407.2 kg/cm2
ScHN = min(B, S) = 1,169 kg/cm2
Allowable Compressive Stress, Cold and New- ScCN, (table CS-2 Metric)
A = 0.125 / (Ro/ t)
= 0.125 / (327 / 9.5)= 0.003631
B = 1,169 kg/cm2
S = 1,407.2 / 1.00 = 1,407.2 kg/cm2
ScCN = min(B, S) = 1,169 kg/cm2
Allowable Compressive Stress, Cold and Corroded- ScCC, (table CS-2Metric)
A = 0.125 / (Ro/ t)
= 0.125 / (327 / 6.33)
= 0.002420B = 1,092.5 kg/cm2
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S = 1,407.2 / 1.00 = 1,407.2 kg/cm2