3 rotarapes

. ropav/diuqil/diuqil 3

.

3

.

. rotarapes .

2 3 .

.

.

L

BlueHighlight

BlueHighlight

BlueHighlight

BlueHighlight

% 02-51

. toob

riew

.

riew-dna-tekcub

.

3

. .

riew toob 3 rotarapes .1 toob diuqil yvaeH 3 rotarapes .2 riew 3 rotarapes .3 riew tekcuB 3 rotarapes .4 eHtoob diuqil yva 3 rotarapes .5

riew toob 3 rotarapes

:

-1

-2

L

-1

. K k

. ( s/tf K )

()0.5V

LV UK T

=

K retsimeD kroY

)p( nl 0640.0 + P 9200.0 + 1281.0 = K 51 p

TV UU 75.0= 2- holdup surge

holdup surge holdup. surge . holdup :LHH QTV =

surge : LSS QTV = Holdup Surge

Surge time, min (NLL-LLL)

Holdup time, min (NLL-LLL)

Service

5 10 A. Unit feed drum

B. Separators 3 5 1. feed to column

2. feed to other drum or tankage 2 5 a. with pump or through exchanger 1 2 b. without pump 3 10 3. feed to fired heater

C. Reflux or product accumulator 2 3 1. Reflux only

2 + 3 + 2. Reflux and product (Base on reflux (3 min) plus appropriate holdup time of overhead product (as per B1-3)

D. Column bottoms 2 5 1. Feed to another column

2. Feed to other drum or tankage 2 5 a. with pump or through exchanger 1 2 b. without pump

2 - 4 5 - 8 1. Feed to fired reboiler (Base on reboiler vapor expressed as liquid (3 min) plus appropriate holdup time of overhead product (as per D1,2)

D. Compressor suction / interstage scrubber 3 min between HLL (high liquid alarm) and high level shutdown 10 min for bottom tangent line to high liquid alarm

F. Fuel gas knock-out dram 20 ft. slug in the incoming fuel gas line between NLL and high level shutdown

G. Flare Knock-out drum 20 to 30 min to HLL

Multiply by the following factor (optional) factor Instrumentation factor Personnel

1.0 Well Instrumented 1.0 Experienced 1.2 Standard Instrumented 1.2 Trained 1.5 Poorly Instrumented 1.5 Inexperienced

-3 D/L

.

D/L

)gisp( D/L 0.3-5.1 052 P 0

0.4-0.3 005 P 052

0.6-0.4 P 005

3

1

0.5()4()

+ =

DLVV

HS Dpi

4

TAD2pi

=

egrus pudloh .1 TA/VA .a

tf 1 rotanimile tsim ) tf 2 D 2.0 ( VH) . TA/VA D/VH . (

TA/A D/H

234

234

xbxdxfxh 1.0yaxcxexgxi

++++

++++=

// HDotAAT

=/ yAAr

=/ xHD

5-01039557.4-=a 190429.3=b 578471.0=c 508853.6-=d 379866.5=e 844810.4=f 114619.4-=g 507108.1-=h 843541.0-=i

// T AAotHD

=/ yHD

=/ xAAr

65735100.0=a 101787.62=b 102992.3=c 239329.22-=d 815353.42=e 428448.41-=f 673999.63-=g 2755925.01=h 158298.9=i

( LHA+ LLA) .b

) ( LHH LLH) D/)LLH+LHH( (

. TA/)LLA+LHA(

egruspudloh nim .c

TVLHLL ()HS

AAAAVV

L+

+=

(LNIM) .2 ()

V

V

UH

=

(AVU)

V

VA AV

= UQ

LU NIMAV = LNIM L .3 ) NIML=L , NIML

. , NIML>L L VH ( pudloh diuqil) , NIML>>L

VH. NIML 1 VA VH . 1

. .4

.

.

:

81cpHL 2 1,884()

T

gDU

=

. Pc s.tf/bl 884,1 :

pHL 52 2.1516001()

T

DU

=

: 2.151600152 = Dk Ps

sHL ()

T = Uk

: sk - sk

(m) sk

F 06 GS < 58.0 citsuac 721 333.0

F 06 GS > 58.0 citsuac 98 361.0

larufruF 98 361.0

98 361.0

lohocla lytuB-ceS 98 361.0

98 361.0

lohocla lynoN 98 361.0

TU: . nim/.ni 01

. :

Ukni ()(./)nimL

sHL LH

=

:

Ukni ()(./)nimH

sHL HL

=

. .5

:

LH

VLHU LH

DHHt

21()=

:

HL

LHU HL

Ht

21 =

.6

.

:

LL

TVLHQ LL

() AAAL =

: LH

LHQ LH

AL =

(tHL tLH) LH LL .7 t LLLH

t LHHL

. .

) (

=

TVLH

LHLL

LH

HLLH

AAAtQ

AtQ

.xam, L

D/L .8 . D/L D/L >> 6 D D D/L

toob diuqil yvaeH 3 rotarapes

:

-1

-2

-1

. K k

. ( s/tf K )

()0.5V

LV UK T

=

K retsimeD kroY

)p( nl 0640.0 + P 9200.0 + 1281.0 = K 51 p

TV UU 75.0=

2- holdup surge .

holdup :LHH QTV =

surge :LSS QTV = Holdup Surge

Surge time, min

(NLL-LLL)

Holdup time, min (NLL-LLL)

Service

5 10 A. Unit feed drum

B. Separators 3 5 1. feed to column

2. feed to other drum or tankage 2 5 a. with pump or through exchanger 1 2 b. without pump 3 10 3. feed to fired heater

C. Reflux or product accumulator 2 3 1. Reflux only

2 + 3 + 2. Reflux and product (Base on reflux (3 min) plus appropriate holdup time of overhead product (as per B1-3)

D. Column bottoms 2 5 1. Feed to another column

2. Feed to other drum or tankage 2 5 a. with pump or through exchanger 1 2 b. without pump

2 - 4 5 - 8 1. Feed to fired reboiler (Base on reboiler vapor expressed as liquid (3 min) plus appropriate holdup time of overhead product (as per D1,2)

D. Compressor suction / interstage scrubber 3 min between HLL (high liquid alarm) and high level shutdown 10 min for bottom tangent line to high liquid alarm

F. Fuel gas knock-out dram 20 ft. slug in the incoming fuel gas line between NLL and high level shutdown

G. Flare Knock-out drum 20 to 30 min to HLL

Multiply by the following factor (optional) factor Instrumentation factor Personnel

1.0 Well Instrumented 1.0 Experienced 1.2 Standard Instrumented 1.2 Trained 1.5 Poorly Instrumented 1.5 Inexperienced

-3 D/L

.

D/L

)gisp( D/L 0.3-5.1 052 P 0

0.4-0.3 005 P 052

0.6-0.4 P 005

3

1

0.6()4()

+ =

DL

VVHS D

pi

4

TAD2pi

=

egrus pudloh -1 TA/VA .a

( tf 1 rotanimile tsim ) tf 2 D 2.0 ( VH) . TA/VA D/VH .

TA/A D/H

234

234

xbxdxfxh 1.0yaxcxexgxi

++++

++++=

// HDotAAT

=/ yAAr

=/ xHD

5-01039557.4-=a 190429.3=b 578471.0=c 508853.6-=d 379866.5=e 844810.4=f 114619.4-=g 507108.1-=h 843541.0-=i

// T AAotHD

=/ yHD

=/ xAAr

65735100.0=a 101787.62=b 102992.3=c 239329.22-=d 815353.42=e 428448.41-=f 673999.63-=g 2755925.01=h 158298.9=i

( VLLA) lessev .b ) ( VLLH) lessev

D/VLLH ( . VLLA TA/)VLLA(

egruspudloh nim .c

TVVLL

HS

AAAVV

L

+ =

(LNIM) -2 ()

V

V

UH

=

(AVU)

V

VA AV

= UQ

LU NIMAV = LNIM L -3 ) NIML=L NIML

L VH ( pudloh diuqil) NIML>>L VH . NIML

1 VA VH . 1 .

-4

. .

.

:

Ukni ()(./)nimL

sHL LH

=

:

Ukni ()(./)nimH

sHL HL

=

. : sk

- sk

(m) sk

F 06 GS < 58.0 citsuac 721 333.0

F 06 GS > 58.0 citsuac 98 361.0

larufruF 98 361.0

98 361.0

lohocla lytuB-ceS 98 361.0

98 361.0

lohocla lynoN 98 361.0

-5 :

LH

BLLVU LH

HDHt

+ 21() =

:

LL

TVQ LL

() AAL =

. toob

(tLH) LL -6 t LLLH

. .

D/L -7 . D/L D/L >> 6 D D D/L

t LHHL . toob .

riew 3 rotarapes

:

-1

-2

-1

. K

k .

( s/tf K )

()0.5V

LV UK T

=

K retsimeD kroY

)p( nl 0640.0 + P 9200.0 + 1281.0 = K 51 p

max 0.75 :

TV UU 75.0= 2- holdup surge

. holdup :LHH QTV =

surge :LSS QTV = Holdup Surge

Surge time, min (NLL-LLL)

Holdup time, min (NLL-LLL)

Service

5 10 A. Unit feed drum

B. Separators 3 5 1. feed to column

2. feed to other drum or tankage 2 5 a. with pump or through exchanger 1 2 b. without pump 3 10 3. feed to fired heater

C. Reflux or product accumulator 2 3 1. Reflux only

2 + 3 + 2. Reflux and product (Base on reflux (3 min) plus appropriate holdup time of overhead product (as per B1-3)

D. Column bottoms 2 5 1. Feed to another column

2. Feed to other drum or tankage 2 5 a. with pump or through exchanger 1 2 b. without pump

2 - 4 5 - 8 1. Feed to fired reboiler (Base on reboiler vapor expressed as liquid (3 min) plus appropriate holdup time of overhead product (as per D1,2)

D. Compressor suction / interstage scrubber 3 min between HLL (high liquid alarm) and high level shutdown 10 min for bottom tangent line to high liquid alarm

F. Fuel gas knock-out dram 20 ft. slug in the incoming fuel gas line between NLL and high level shutdown

G. Flare Knock-out drum 20 to 30 min to HLL

Multiply by the following factor (optional) factor Instrumentation factor Personnel

1.0 Well Instrumented 1.0 Experienced 1.2 Standard Instrumented 1.2 Trained 1.5 Poorly Instrumented 1.5 Inexperienced

-3 D/L

.

D/L

)gisp( D/L 0.3-5.1 052 P 0

0.4-0.3 005 P 052

0.6-0.4 P 005

3

1

0.6()4()

+ =

DL

VVHS D

pi

4

TAD2pi

=

egrus pudloh -1 TA/VA .a

tf 1 rotanimile tsim ) tf 2 D 2.0 ( VH) . TA/VA D/VH . (

TA/A D/H

234

234

xbxdxfxh 1.0yaxcxexgxi

++++

++++=

// HDotAAT

=/ yAAr

=/ xHD

5-01039557.4-=a 190429.3=b 578471.0=c 508853.6-=d 379866.5=e 844810.4=f 114619.4-=g 507108.1-=h 843541.0-=i

// T AAotHD

=/ yHD

=/ xAAr

65735100.0=a 101787.62=b 102992.3=c 239329.22-=d 815353.42=e 428448.41-=f 673999.63-=g 2755925.01=h 158298.9=i

( LLLA) level diuqil woL .b : LLLH

LLL HD =+ 0.57 D/LLLH . .ni 9 LLLH tf4 D . LLLA (WH) riew .c

.

= HDH WV . a tf 2 < WH

. 2L .d

TVLLL

HS

AAAVV

L

+ 2=

. .ni 6

=+ N Ldni 221.

2L

(ALL) -2 ) LLH LHH 2/WH

D/LHH (. . LLA LHA

= AAAA LLTVLH

-3

. .

. :

Ukni ()(./)nimL

sHL LH

=

:

Ukni ()(./)nimH

sHL HL

=

. : sk

- sk

(m) sk

F 06 GS < 58.0 citsuac 721 333.0

F 06 GS > 58.0 citsuac 98 361.0

larufruF 98 361.0

98 361.0

lohocla lytuB-ceS 98 361.0

98 361.0

lohocla lynoN 98 361.0

-4 :

LH

LLU LH

Ht

21=

:

HL

LHU HL

Ht

21 =

-5 1L .a

: - 1L

=

LL

LHLL

LH

HLLH

AtQ

AtQ

1xam, L

. .ni 6

.b

=+ LLL 12 (LNIM) -6

() .a

V

V

UH

=

(AVU) .b

V

VA AV

= UQ

.c

1L

LU NIMAV = LNIM L -7

) NIML=L NIMLL

1 VH . NIML . 1 VA VH .

D/L -9 . D/L D/L >> 6 D D D/L

riew tekcuB 3 rotarapes

:

-1

-2

-1

. K

k .

( s/tf K )

()0.5V

LV UK T

=

K retsimeD kroY

)p( nl 0640.0 + P 9200.0 + 1281.0 = K 51 p

xam : 57.0

=0.57 UU VT (LH LL) emit ecnediser -2

: smurd deef reppirts retaw ruos rof ecivres yrenifer rof .nim 06 = LH ecivres tnalp lacimehc rof .nim 51 01 = LH smurd deef retareneger enima rof .nim 51 01 = LH

-3 D/L

.

D/L

)gisp( D/L 0.3-5.1 052 P 0

0.4-0.3 005 P 052

0.6-0.4 P 005

3

1

0.7()4()

+ =

DLQQ

LLLLLHLH Dpi

4

TAD2pi

=

L1 -1 ( VA ) .a

( tf 1 rotanimile tsim ) tf 2 D 2.0 ( VH) . VA TA/VA D/VH .

TA/A D/H

234

234

xbxdxfxh 1.0yaxcxexgxi

++++

++++=

// HDotAAT

=/ yAAr

=/ xHD

5-01039557.4-=a 190429.3=b 578471.0=c 508853.6-=d 379866.5=e 844810.4=f 114619.4-=g 507108.1-=h 843541.0-=i

// T AAotHD

=/ yHD

=/ xAAr

65735100.0=a 101787.62=b 102992.3=c 239329.22-=d 815353.42=e 428448.41-=f 673999.63-=g 2755925.01=h 158298.9=i

1L .b

) (TV

LLLLLHLH

AAQQ

L

+=

1

(LNIM) -4

() .a

V

V

UH

=

(AVU) .b

V

VA AV

= UQ

1L

.c

LU NIMAV =

LNIM L1 -5 ) NIML=1L NIML

H/D A/AT

432

432

0.1 hxfxdxbxixgxexcxay

++++

++++=

TAAtoDH //

rAAy /=

DHx /=

a=-4.75593010-5 b=3.924091 c=0.174875 d=-6.358805 e=5.668973 f=4.018448 g=-4.916411 h=-1.801705 i=-0.145348

DHtoAA T //

DHy /=

rAAx /=

a=0.00153756 b=26.787101 c=3.299201 d=-22.923932 e=24.353518 f=-14.844824 g=-36.999376 h=10.5295572 i=9.892851

b. L2

( )LLLHLL

LLSH

AAQTT

L

+=2

7- 3L L3 D/12 12 in. .

L3 L4

L4 -8 .a

(1)H

L HHLL

=

.b . H VH D =

.nim 51 5 = )yllacipyt( egrus/pudloh a emussA fo mottob eht evoba .ni 6 tuoba si LLL dna thgieh riew eht woleb .ni 6 tuoba si LLH emussA lessev eht

D/LLLA D/LLHA D/LLLH D/LLHH . LLLA LLHA 4L .c

) (LLHLLL

HSLL

AATTQ

L

+ 4=

L -9

=+++ LLLLL 1234 D/L -01

. D/L D/L >> 6 D D D/L

: Heavy Liquid Boot

:

20 Operating Pressure (bar a) 715.09 (kg/m3)Liquid Density 112639 Total Mass Flow (kg/h)

2.60 Vapor Density (kg/m3) 45 Temperature(C)

1-

PsiabarPsiabarP 3741.1

7.1401.120 ==

s

m

s

ftPPkPsiaPPsia 0612.02007.0ln046.00029.01821.0151 ==++=

s

mKUV

VLT 0131.16.2

6.209.7150612.0)( 5.0 ===

s

mUU TV 76.075.0 ==

2- holdup surge Separator with pump or through exchanger - TH , TS

33

96.120432.0min160

min5 ms

msQTV LHH ===

3-

m

DL

VVD SH 5769.2

)(6.0)(4 3

1

=

+=

pi

22

2154.54

mDAT ==

pi

1- holdup surge a. AV/AT

33

184.50432.0min160

min2 ms

msQTV LSS ===

= 0.20.4515 Dm : ( m 9403.0) tf 1 D2.0 VH

=0.4515 VHm Am 0.20.1142410.72472

AA

DH

VT

VV ===

( VLLA) lessev .b . m 572.1 VLLH

Am 1.5720.940.47842.2452A

AD

HVLL Hm

T

VLLVLL ==== VLL

egruspudloh nim .c

(LNIM) -2 () .a

sUH

V

==0.876 V

(AVU) .b

==0.3691V

VA AV

UQ

.c

==0.331 NIMAV LUm LNIM L -3 . NIML>L -4

nim0.960.580.333.

4101 === GS SrGcificepSytivakni ()007.5

tf 16.793 bl

= H

tf 34.373 bl

= L

= HPc 0.9395() = LPc 0.8663()

mAAA

LVVTVVLL

=9.6793 HS

+=

sUkninim

L

sHLLH

7.8110013nim

)61.2955.nim

=== ()(.

sUkninim

H

sHLHL

4.6033013nim

)01.2722.nim

=== ()(.

-5

(BLLH tooB ) toob .

Qs ()279.191()

AAL

LL

TV= LL

=

(tLH) LL -6

LLLH telbatpecca D/L -7

elbatpecca

DL

3.9346 =

-8

toob diuqil yvaeH :

s

PHL UUm== 0.573.9742013

: toob

mU

QD

P

LH0.88 B

421=

=

pi:

sUH

tHL

LH4.603301792.25 HL

22.9675

= 3==

:

) ( ) (Qs

DH

LH

BLH40.200193 LH

20.882.9675

4

22

=

==

pipi

t LHHL

.

s 21()492.4400()U

HDHt

LH

BLLV= LH

+=