CPF-010 Utility Line Sizing Attachment_0.xls

7/24/2019 CPF-010 Utility Line Sizing Attachment_0.xls

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293701913.xls Cover 11/05/2015 Cover

Calculation Cover Sheet

Calc no CPF)-CA-PRO-010

Project title Melut Bas! Ol "evelo#$e!t Pa%&a'e A Proj no 211095

Client Petroar O#erat!' Co$#a!* +$te Phase/CTR "etale

Calculation title ,tlt* +!e !' Page 1 of 2

Calculation objective

o eter$!e utlt* l!e ses or Al-aala*! CPF #la!t.

Calculation method

Assumptions

References

Conclusions

Reer to t4e atta%4e su$$ar* o sele%te l!e ses.

A -e#-0 ssue or Reve6 M8

R: "A "CRPO; B C?005>9-PR-"-003) 6t4 res#e%t to velo%t* a! #ressure ro# t4rou'4 t4e l!e.

4e lu velo%t* a! #ressure ro# 6ere %al%ulate or a 've! l!e se a%%or!' to t4e ta!ar +!e!' #reas4eets (Reere!%es 1@2).

Reer to Reere!%e 3 or s!' %rtera.

1. ta!ar Cal%ulato! PR-CA-002 - !'le P4ase Pressure "ro#2. ta!ar Cal%ulato! PR-CA-001 - 6o P4ase Pressure "ro#3. Ra!4ll =orle* "es'! ta!ar - +!e !' (0>?005>9-PR-"-003)


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293701913.xls C4e%&lst 11/05/2015 C4e%&lst

Calculation Checklist

Calc no PF)-CA-PRO-0


Client Petroar O#erat!' Co$#a!* +$te Phase/CTR "etaleCalculation title ,tlt* +!e !' Page 2 of 2

Please check boxes for all applicable items checked or delete if not appropriate:

Calculations:

Project title shown.

Calculation title shown.

Revision history box complete and signed.

Index.

Appropriate stamp for preliminary issues.Calculation objectives (aims stated.

Calculation method defined or described (including formulae if relevant.

Reference made to text! standard or code. Chec" version#edition with that re$uired for project.

%ource of input data stated (with revision number and date if relevant.

Assumptions stated.

%ummary of results or conclusions if appropriate.

&or software based calculations! reference to software verification if available.

'ethod clear and easy to follow.

Input data correct.

Calculation result within expected limits.

Calculation tolerances stated if significant.

nits used as re$uired by client.

Abbreviations correct.

Appropriate cross)references.

%"etches included and clearly labelled! where re$uired.

Attachments included and referenced! as re$uired.

Checking records:

Chec"ed and annotated copy of calculation filed (use *Chec" Print* stamp.

Corrections made as re$uired and calculation dated and signed on cover sheet by chec"er.

Revisions:

Changes clouded.

Revision history bloc" updated.

Calculation re)chec"ed if re$uired.

A -e#-0 ssue or Reve6 M8

REV DATE DESCRIPTION BY CHECKED

Calculation number assigned and registered (usual format is Proj +o)CA,)-iscipline code)%e$ +o eg)CA,)/)001! but format may be varied by Project 'anager.

Calculation arithmetically correct 2R software previously verified and reference to verificationchec"ed.


3/31

Calculation Sheet

Calc n

Project title 'elut 3asin 2il -evelopment Pac"age A Proj n

Client Petrodar 2perating Company ,imited Phase

Calculation title tility ,ine %i8ing Page

Activity ,ine %i8ing %ummary ile

!ine "o# $escription Phase P%& 'C& Rating

lo# Ol (1) -CO-AC-1109 to 1117-252.0

lo# Ol (1) 10-CO-AC-112-25@>70 2) Co$$o! 4eaer or !tera%e ra6-o +u 100 20 150 3.0 3.1

lo# Ol (2) -CO-AC-11>2-25@7 +u 100 0 150 0.3 1.9

lo# Ol (2) -CO-AC-11>3-25 +u 100 0 150 0.3 1.0

lo# Ol (3) 3-CO-AC-11>5-25@7 +u >0 0 150 0. 5.7

lo# Ol (3) 3-CO-AC-100-25 +u >0 0 150 0. .1

Fuel Ol 1 -CO-AC-1239@ 120-25-25.9

Fuel Ol 2 3-CO-AC-121>-250 0 150 0.7 22.>

Fuel Ol 2 2-CO-AC-122-25 2) Crue ol ro$ P:s o! !let $a!ol +u >0 0 150 0.2 1.

Fuel Ol 3 2-CO-AC-123-25

Blo6o6! 1 1-PR-AC-001-3>9 2) Crue ol ro$ P:s o! !let $a!ol +u 0 20 150 5.1

Blo6o6! 2 10-CO-AC-12-250 +u 0 20 150 0.3 10.1

Blo6o6! 2 -CO-AC-1253@ 125-250 0 150 0.> 9.>

P$

'tream"o#

$esign lo(

Rate )kg/h*Velocity

[m/s

Pressure!rop

["Pa/#$$m

1) lo# ol #u$#s (P-503A/B) su%to!l!es

1) lo# ol #u$#s (P-503A/B) su%to!

l!es

1) lo# ol #u$#s (P-503A/B) s%4ar'el!es

1) lo# ol #u$#s (P-503A/B) s%4ar'el!es

1) Fuel ol #u$#s (P-505A/B) su%to! l!es

2) Fuel ol #u$#s (P-505A/B) s%4ar'el!es

1) Blo6o6! ta!& #u$#s (P-50A/B)su%to! l!es

2) Blo6o6! ta!& #u$#s (P-50A/B)s%4ar'e l!es

1) Blo6o6! ta!& #u$#s (P-50A/B)s%4ar'e l!es

2) o o o#erato! #u$# (P-507) su%to!l!es

1) o o o#erato! #u$# (P-507)s%4ar'e l!e

2) Blo6o6! ta!& #u$#s (P-50A/B)su%to! l!es

1)"esel u!loa!' #u$# (P-55) su%to!l!e

1)"esel u!loa!' #u$# (P-55)s%4ar'e l!e

1) "esel tra!ser #u$#s (P-5A/B)su%to! l!e

2) "esel tra!ser #u$#s (P-5A/B)s%4ar'e l!e


4/31

"esel 2-FO-A-025 >@92> 1) "esel to 4eat $eu$ 4eaters +u 50 0 150 1. .9

"esel 2-FO-A-05 11@20 2) "esel to P2 +u 50 0 150 1.> 7.9

O#e! "ra!1 3-P=-AC-2033/3/35/3 @500 O#e! "ra! u$# Pu$# "s%4ar'e +u >0 0 150 0.3 1.3

O#e! "ra!1 3-P=-AC-2020/37 @500 O#e! "ra! u$# Pu$# "s%4ar'e +u >0 0 150 0.3 1.3

O#e! "ra!2 3-P=-AC-2021/3> 9@000 +u >0 0 150 0. .5

O#e! "ra!2 3-CO-AC-1233/3/35/3 13@500 Close "ra! Pu$# "s%4ar'e +u >0 0 150 0.9 9.5

O#e! "ra!3 -CO-AC-123>/>-25A/B s%4ar'e l!e.


5/31

293701913.xls lo# Ol (1) 11/05/2015 lo# Ol (1)

CALCULATION SHEET

Calc no (CPF)-CA-PRO-010



Calculation title ,tlt* +!e !' Page of 2

Activity ileR+,-'-." $AT+ 0 C&+C1+$ APPR.,+$ R+,-'-." $AT+ 0 C&+C1+$ APPR.,+$

A 6-Sep-04 0 11-Feb-05 PWH

S%&'() P*AS) PR)SS+R) !R,P -(%.+%! ,R 'AS

ACCORDING TO CRANE AND CHURCHILL (SI UNITS)

ta!ar Cal%ulato! 0>/005>9-PR-CA-002@ Rev. 0@ ssue or ,se@ 1>-Fe-99

(1) (2)

INPUT

+!e ;u$er -CO-AC-1109 to 1117-257.0 >7.0 fro t!e "#ec. De!drator to '#o an*

A%tual :s%ost* %PH 1>.000 1>.000 F#owrate :

(%&) SP)C%0%CAT%,&

;o$!al "a$eter $$H 100 250 Proert%e$:

P#!' #e%%ato! AC AC

A; Rat!' 150 150

P#e %4eule 40 20

P#e !ter!al "a$eter $$H 102.3 20.

,ser !#ut P#e " $$H

Materal o Co!stru%to! C C

P#e Rou'4!ess $$H 0.0 0.0

OUTPUT

P#e Cross-se%to!al Area $KH 0.00>21 0.0532

Flu :elo%t* $/sH 1234 52$$

Re*!ols ;u$er 12@500 37@0

"ar%* Fr%to! Fa%tor 0.030 0.023

Pressure "ro# &Pa/100$H 612$# 542#5

:elo%t* "es'! Ra!'e $/sH 2 to 3 2 to 3

"P "es'! Ra!'e &Pa/100$H 90.0 90.0

C,&C(+S%,&S

Therefore the recommended line si7e for 489C,9AC9##$: to ###;913*9)T is #$$ mm &/005>9-PR-CA-002@ Rev. 0@ ssue or ,se@ 1>-Fe-99

INPUT

+!e ;u$er -CO-AC-11>2-253-25@7 9@3> Proert%e$: Fro $#o o%# +$ data$!eet

"es'! Mar'! 0I 0I

"es'! Flo6 &'/4H >@7 9@3>

A%tual "e!st* &'/$JH >7.0 93.>0

A%tual :s%ost* %PH 1>.000 0.25

(%&) SP)C%0%CAT%,&

;o$!al "a$eter $$H 100 100

P#!' #e%%ato! AC AC

A; Rat!' 150 150

P#e %4eule 40 40

P#e !ter!al "a$eter $$H 102.3 102.3

,ser !#ut P#e " $$H


P#e Rou'4!ess $$H 0.0 0.0

OUTPUT

P#e Cross-se%to!al Area $KH 0.00>21 0.00>21

Flu :elo%t* $/sH $254 $254

Re*!ols ;u$er 1@70 123@1>0

"ar%* Fr%to! Fa%tor 0.03> 0.020

Pressure "ro# &Pa/100$H #26> #2$4

:elo%t* "es'! Ra!'e $/sH 1.5 3.0

"P "es'! Ra!'e &Pa/100$H 5 - 1 23 - 35

C,&C(+S%,&S

Therefore the recommended line si7e for 489C,9AC9##61913*9)T is #$$ mm &/005>9-PR-CA-002@ Rev. 0@ ssue or ,se@ 1>-Fe-99

INPUT

+!e ;u$er 3-CO-AC-11>5-25@7 9@3> Proert%e$: Fro $#o o%# +$ data$!eet

"es'! Mar'! 0I 0I

"es'! Flo6 &'/4H >@7 9@3>

A%tual "e!st* &'/$JH >7.0 93.>0

A%tual :s%ost* %PH 1>.000 0.25

(%&) SP)C%0%CAT%,&

;o$!al "a$eter $$H >0 >0

P#!' #e%%ato! AC AC

A; Rat!' 150 150

P#e %4eule 40 40

P#e !ter!al "a$eter $$H 77.9 77.9

,ser !#ut P#e " $$H


P#e Rou'4!ess $$H 0.0 0.0

OUTPUT

P#e Cross-se%to!al Area $KH 0.0077 0.0077

Flu :elo%t* $/sH $236 $236

Re*!ols ;u$er 2@190 11@0

"ar%* Fr%to! Fa%tor 0.030 0.020

Pressure "ro# &Pa/100$H 32>: 42$>

:elo%t* "es'! Ra!'e $/sH 1.5 3.0

"P "es'! Ra!'e &Pa/100$H 5 - 1 23 - 35

C,&C(+S%,&S

Therefore the recommended line si7e for 589C,9AC9##63913*9)T is 6$ mm &$913*9)T is 6$ mm &/005>9-PR-CA-002@ Rev. 0@ ssue or ,se@ 1>-Fe-99

(1) (2)

INPUT

+!e ;u$er -CO-AC-1239@ 120-25-25


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293701913.xls Fuel Ol 2 11/05/2015 Fuel Ol 2

CALCULATION SHEET




Calculation title ,tlt* +!e !' Page > of 2


A 6-Sep-04 0 11-Feb-05 PWH

S%&'() P*AS) PR)SS+R) !R,P -(%.+%! ,R 'AS



(1) (2)

INPUT

+!e ;u$er 3-CO-AC-121>-25

"es'! Mar'! 0I 0I

"es'! Flo6 &'/4H 11@122 1@> 2) F+e# o%# to ower #ant

A%tual "e!st* &'/$JH >>9.7 >>9.7 F#owrate : Info fro 4P

A%tual :s%ost* %PH 59.75 59.75

(%&) SP)C%0%CAT%,& Proert%e$: Fro f+e# o%# +$ data$!eet

;o$!al "a$eter $$H >0 50

P#!' #e%%ato! AC A

A; Rat!' 150 150

P#e %4eule 40 40

P#e !ter!al "a$eter $$H 77.9 52.5

,ser !#ut P#e " $$H


P#e Rou'4!ess $$H 0.0 0.0

OUTPUT


Flu :elo%t* $/sH $2;5 $214

Re*!ols ;u$er >50 190

"ar%* Fr%to! Fa%tor 0.075 0.337

Pressure "ro# &Pa/100$H 112;: #>233

:elo%t* "es'! Ra!'e $/sH 2 - 3 2 - 3

"P "es'! Ra!'e &Pa/100$H 90.0 90.0

C,&C(+S%,&S

Therefore the recommended line si7e for 189C,9AC9#1#6913*9)T is now 6$ mm &< Revised from 2 ro 3" due o !i!er f#ow

Therefore the recommended line si7e for 189C,9AC9#14$913*9)T is 3$ mm &/005>9-PR-CA-002@ Rev. 0@ ssue or ,se@ 1>-Fe-99

INPUT

+!e ;u$er 2-CO-AC-123-25 ":/0

Pressure "ro# &Pa/100$H 442;5 @!%V/$

:elo%t* "es'! Ra!'e $/sH 2 - 3

"P "es'! Ra!'e &Pa/100$H 90.0

C,&C(+S%,&S

Therefore the recommended line si7e for 189C,9AC9#14#913*9)T is 3$ mm &/005>9-PR-CA-002@ Rev. 0@ ssue or ,se@ 1>-Fe-99

(1) (2)

INPUT

+!e ;u$er -CO-CC-1255-259 Proert%e$: Fro cr+de o%# on t!e !eader

"es'! Mar'! 0I 0I

"es'! Flo6 &'/4H 9@225 2@03@9>9 2) Cr+de o%# fro P'8$ on %n#et an%fo#d

A%tual "e!st* &'/$JH 923.00 923.00 F#owrate : Fro P'8$ ca#c+#at%on

A%tual :s%ost* %PH 9.0>> 9.0>>

(%&) SP)C%0%CAT%,& Proert%e$: Fro P'8$ ca#c+#at%on

;o$!al "a$eter $$H 100 00

P#!' #e%%ato! CC AC

A; Rat!' 00 150

P#e %4eule %0 20

P#e !ter!al "a$eter $$H 97.2 390.

,ser !#ut P#e " $$H


P#e Rou'4!ess $$H 0.0 0.0

OUTPUT

P#e Cross-se%to!al Area $KH 0.0072 0.119>0

Flu :elo%t* $/sH 126# 32##

Re*!ols ;u$er 3>0 2@750

"ar%* Fr%to! Fa%tor 0.1> 0.01

Pressure "ro# &Pa/100$H >5$2:: #1321;

:elo%t* "es'! Ra!'e $/sH 2 - 3 2 - 3

"P "es'! Ra!'e &Pa/100$H 90.0 90.0

C,&C(+S%,&S

Though the pressure drop for 489C,9CC9#133913*9)T is high? the selected line si7e is #$$ mm &< because the line is used

intermittently2 Similarly? selected line si7e for #>89PR9AC9>$$#956*9)T is 4$$ mm &< even though velocity and pressure drop

are higher than design range due to intermittent service2

R)0)R)&C)S

1) Cra!e@ Flo6 o Flus t4rou'4 :alves@ Ftt!'s@ a! P#e@ 1992@ Metr% to! - ,!ts

2) C4ur%4ll .=.@ Fr%to!-a%tor euato! s#a!s all lu-lo6 re'$es@ C4e$. !'.@ 7-;ov-77

Vapour Criteria

(i=uid Criteria

P%P) %!

Liquid Liquid

CC AC

80 20

CS CS


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CALCULATION SHEET






A 6-Sep-04 0 11-Feb-05 PWH

S%&'() P*AS) PR)SS+R) !R,P -(%.+%! ,R 'AS



(1) (2)

INPUT

+!e ;u$er 10-CO-AC-12-250 27@90

"es'! Mar'! 0I 0I

"es'! Flo6 &'/4H 55@3>0 27@90 2) B#owdown tan* +$ (P-,6A/B) d%$c!ar0e #%

A%tual "e!st* &'/$JH 923.00 923.00 F#owrate : B#owdown tan* +$ (P-,6A/B) ca.

A%tual :s%ost* %PH 9.0>> 9.0>>

(%&) SP)C%0%CAT%,& Proert%e$: Fro B#owdown tan* +$ (P-,6A/

;o$!al "a$eter $$H 250 150

P#!' #e%%ato! AC AC

A; Rat!' 150 150

P#e %4eule 20 40

P#e !ter!al "a$eter $$H 20. 15.1

,ser !#ut P#e " $$H


P#e Rou'4!ess $$H 0.0 0.0OUTPUT


Flu :elo%t* $/sH $25# $243

Re*!ols ;u$er 110 90

"ar%* Fr%to! Fa%tor 0.5>2 0.711

Pressure "ro# &Pa/100$H #$2#$ 41234

:elo%t* "es'! Ra!'e $/sH 1.> 3.0

"P "es'! Ra!'e &Pa/100$H 11 - 23 23 to 35

C,&C(+S%,&S

13$ mm &< from 1$$

#3$ mm &913*9)T is high? the selected line si7e is Bas changed to

The selected line si7e for 489C,9AC9#135? #134913*9)T is Bas changed from #$$ to

Vapour Criteria

(i=uid Criteria

P%P) %!

Liquid Liquid

AC AC

20 40

CS CS


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CALCULATION SHEET






A 6-Sep-04 0 11-Feb-05 PWH

S%&'() P*AS) PR)SS+R) !R,P -(%.+%! ,R 'AS



(1) (2)

INPUT

+!e ;u$er -CO-AC-1252-25


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CALCULATION SHEET






A 6-Sep-04 0 11-Feb-05 PWH

S%&'() P*AS) PR)SS+R) !R,P -(%.+%! ,R 'AS



(1) (2)

INPUT

+!e ;u$er -CO-CC-1257-25


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CALCULATION SHEET






A 6-Sep-04 0 11-Feb-05 PWH

S%&'() P*AS) PR)SS+R) !R,P -(%.+%! ,R 'AS



INPUT

+!e ;u$er 3-FO-A-010 3-FO-A-010 (P&ID: JAB-CPF1-PID-2166-1 Rev. 1)

Mass D !er'* Bala!%e trea$ ;o. 0

PR,C)SS !ATA 1)D%e$e# +n#oad%n0 + (P-,,) $+ct%on #%ne

P4ase Liquid Liquid F#owrate : D%e$e# +n#oad%n0 + (P-,,) ca.

e$#erature@ GCH 39.0 39.0

Pressure@ P &PaaH 101.30 101.30 Proert%e$: D%e$e# +n#oad%n0 + (P-,,) data$!e

Mass Flo6rate &'/4H 2@900 2@900

"es'! Mar'! 0I 0I

"es'! Flo6 &'/4H 2@900 2@900

A%tual "e!st* &'/$JH >30.00 >30.00

A%tual :s%ost* %PH 5.000 5.000

(%&) SP)C%0%CAT%,&

;o$!al "a$eter $$H >0 100

P#!' #e%%ato! A A

A; Rat!' 150 150

P#e %4eule 40 40

P#e !ter!al "a$eter $$H 77.9 102.3

,ser !#ut P#e " $$H


P#e Rou'4!ess $$H 0.0 0.0

OUTPUT


Flu :elo%t* $/sH #2;3 #2$#

Re*!ols ;u$er 22@00 17@220

"ar%* Fr%to! Fa%tor 0.027 0.02>

Pressure "ro# &Pa/100$H 452#6 ##2>5

:elo%t* "es'! Ra!'e $/sH 1.0 1.0

"P "es'! Ra!'e &Pa/100$H 5 - 1 5 - 1

C,&C(+S%,&S

Therefore the recommended line si7e is #$$ mm &30.00 >30.00

A%tual :s%ost* %PH 5.000 5.000

(%&) SP)C%0%CAT%,&

;o$!al "a$eter $$H >0 100

P#!' #e%%ato! A A

A; Rat!' 150 150

P#e %4eule 40 40

P#e !ter!al "a$eter $$H 77.9 102.3

,ser !#ut P#e " $$H


P#e Rou'4!ess $$H 0.0 0.0

OUTPUT


Flu :elo%t* $/sH #2;3 #2$#

Re*!ols ;u$er 22@00 17@220

"ar%* Fr%to! Fa%tor 0.027 0.02>

Pressure "ro# &Pa/100$H 452#6 ##2>5

:elo%t* "es'! Ra!'e $/sH 1.> 1.>

"P "es'! Ra!'e &Pa/100$H 23 - 35 23 - 35

C,&C(+S%,&S

Since the calculated !P is higher than alloBable !P?the line si7e Bas increased from 5 to 48

not used for continuous service2 Therefore the recommended line si7e is #$$ mm &30.00 >30.00

A%tual :s%ost* %PH 5.000 5.000 Proert%e$: D%e$e# tran$fer +$ (P-,6A/B) data

(%&) SP)C%0%CAT%,&

;o$!al "a$eter $$H >0 >0

P#!' #e%%ato! A A

A; Rat!' 150 150

P#e %4eule 40 40

P#e !ter!al "a$eter $$H 77.9 77.9

,ser !#ut P#e " $$H


P#e Rou'4!ess $$H 0.0 0.0

OUTPUT


Flu :elo%t* $/sH $2;> $2;>

Re*!ols ;u$er 9@>00 9@>00

"ar%* Fr%to! Fa%tor 0.032 0.032

Pressure "ro# &Pa/100$H :265 :265

:elo%t* "es'! Ra!'e $/sH 1.0 1.>

"P "es'! Ra!'e &Pa/100$H 5 - 1 23 - 35

C,&C(+S%,&S

Therefore the recommended line si7e for 5890,9A94$#4 and 4$#3 is 6$ mm &? 4$#; and 4$11 is 6$ mm &30.00 >30.00 F#owrate : D%e$e# tran$fer +$ (P-,6A/B) ca.

A%tual :s%ost* %PH 5.000 5.000

(%&) SP)C%0%CAT%,& Proert%e$: D%e$e# tran$fer +$ (P-,6A/B) data

;o$!al "a$eter $$H >0 25

P#!' #e%%ato! A A

A; Rat!' 150 150

P#e %4eule 40 40

P#e !ter!al "a$eter $$H 77.9 2.

,ser !#ut P#e " $$H


P#e Rou'4!ess $$H 0.0 0.0

OUTPUT


Flu :elo%t* $/sH $2;> $23$

Re*!ols ;u$er 9@>00 2@200

"ar%* Fr%to! Fa%tor 0.032 0.030

Pressure "ro# &Pa/100$H :265 ##2>4

:elo%t* "es'! Ra!'e $/sH 2 - 3 2 - 3

"P "es'! Ra!'e &Pa/100$H 90.0 90.0

C,&C(+S%,&S

Therefore the recommended line si7e for 5890,9A94$11 is 6$ mm &? 4$15 is 13 mm &30.00 >30.00

A%tual :s%ost* %PH 5.000 5.000 Proert%e$: D%e$e# tran$fer +$ (P-,6A/B) data

(%&) SP)C%0%CAT%,&

;o$!al "a$eter $$H 50 50

P#!' #e%%ato! A A

A; Rat!' 150 150

P#e %4eule 40 40

P#e !ter!al "a$eter $$H 52.5 52.5

,ser !#ut P#e " $$H


P#e Rou'4!ess $$H 0.0 0.0

OUTPUT


Flu :elo%t* $/sH #2>; $2#5

Re*!ols ;u$er 1@50 1@120

"ar%* Fr%to! Fa%tor 0.030 0.057

Pressure "ro# &Pa/100$H >32>; $2;3

:elo%t* "es'! Ra!'e $/sH 2 - 3 2 - 3

"P "es'! Ra!'e &Pa/100$H 90.0 90.0

C,&C(+S%,&S

Therefore the recommended line si7e for 5890,9A94$1# is 3$ mm &2:1 ;42:3

:elo%t* "es'! Ra!'e $/sH 2 - 3 2 - 3

"P "es'! Ra!'e &Pa/100$H 90.0 90.0

C,&C(+S%,&S

Therefore the recommended line si7e for 5890,9A9 is 3$ mm & - 9.22 - - - 2.

>0 >>.9 77.92 73. 5>.2 - - - 77.92 - 73. - - - .100 11.3 102.2 97.1> >0.0 - - - 102.2 - 97.1> - 92.0 - >7.

150 1>.3 15.0> 1.3 12. - - - 15.0> - 1.3 - 139.7 - 131

200 219.1 202.7 193.7 17. - 20. 205.02 202.7 19>.> 193.7 1>>.92 1>2.5> 177.> 173

250 273.1 25.5 27.7 222.3 - 20. 257.5 25.5 27.7 22.92 23.5> 230.22 222.3 215

300 323.9 30.> 29>.5 273.1 - 311.2 307.1 303.2> 295.3 2>>.9 2>1.02 273.1 2.7 257

350 355. 33.5 330.2 - 32.9 339.7 33.5 333.3 325.2 317.5 307.9 300.02 292.1 2>

00 0. 3>7.3 3>1 - 393.7 390.5 3>7.3 3>1 373.0> 33.52 35.02 3.> 333.3 325

50 57 37.9 31. - .3 1.1 3.7 2>. 1>.9 09.3 39>.2> 3>7.1 377. 3

500 50> >>.9 >2. - 95.3 >>.9 >2. 77.>2 .7 55.2 2.92 31.> 19.1 07

550 559 539.9 533. - 5.3 539.9 533. - 51.5 501.> >9.1 7. 3.7 51

00 10 590.9 5>. - 597.3 590.9 5>1. 575.0 50.7> 5>.0> 532.22 517.9 505.2 90

50 0 0.9 3. - .1 3. - - - - - - - -

700 711 91.9 >5. - 95.1 >5. 79.2 - - - - - - -

750 72 72.9 73. - 7.1 73. 730.2 - - - - - - -

>00 >13 793.9 7>7. - 797.1 7>7. 7>1.2 77>.0 - - - - - ->50 > >.9 >3>. - >>.1 >3>. >32.2 >29.0 - - - - - -

900 91 >9.9 >>>. - >9>.1 >>>. >>2.2 >75.9 - - - - - -

1050 107 107.9 101. - - - - - - - - - - -


22/31

leE///var/666/a##s/%o!verso!/t$#/s%rat%4L2/293701913.xls 293701913.xls O#e! "ra!1

CALCULATION SHEET






A 6-Sep-04 0 11-Feb-05 PWH

S%&'() P*AS) PR)SS+R) !R,P -(%.+%! ,R 'AS



(1) (2)

INPUT

+!e ;u$er 3-P=-AC-2033/3/35/3 3-P=-AC-2020/37 (P&ID: JAB-CPF1-PID-2169-1 Rev. 1)

Mass D !er'* Bala!%e trea$ ;o. -25


23/31

leE///var/666/a##s/%o!verso!/t$#/s%rat%4L2/293701913.xls 293701913.xls O#e! "ra!2

CALCULATION SHEET






A 6-Sep-04 0 11-Feb-05 PWH

S%&'() P*AS) PR)SS+R) !R,P -(%.+%! ,R 'AS



INPUT

+!e ;u$er 3-P=-AC-2021/3> 3-CO-AC-1233/3/35/3

Mass D !er'* Bala!%e trea$ ;o. -2500 0.>00

(%&) SP)C%0%CAT%,&

;o$!al "a$eter $$H >0 >0

P#!' #e%%ato! AC AC

A; Rat!' 150 150

P#e %4eule 40 40

P#e !ter!al "a$eter $$H 77.9 77.9

,ser !#ut P#e " $$H


P#e Rou'4!ess $$H 0.0 0.0

OUTPUT


Flu :elo%t* $/sH $236 $26;

Re*!ols ;u$er 51@00 7@00

"ar%* Fr%to! Fa%tor 0.023 0.022

Pressure "ro# &Pa/100$H 4246 :24:

:elo%t* "es'! Ra!'e $/sH 1.> 1.0

"P "es'! Ra!'e &Pa/100$H 23 - 35 5 - 1

C,&C(+S%,&S

Therefore the recommended line si7e for 589PD9AC91$1#/56913*9)T is 6$ mm &913*9)T is 6$ mm &21 :A+,

Flu :elo%t* $/sH #241 @!%V/$

Re*!ols ;u$er 15@20 ":/0

"ar%* Fr%to! Fa%tor 0.019 ":/0

Pressure "ro# &Pa/100$H #:2$4 @!%V/$

:elo%t* "es'! Ra!'e $/sH 1.5 - 2.1 .3

"P "es'! Ra!'e &Pa/100$H - 5 35 - 5

C,&C(+S%,&S

Therefore the recommended line si7e for 689SD9A943$5 is #$$ mm &/005>9-PR-CA-002@ Rev. 0@ ssue or ,se@ 1>-Fe-99

INPUT

+!e ;u$er >-,=-A-15/55/5 -,=-A-157/5>

Mass D !er'* Bala!%e trea$ ;o.

PR,C)SS !ATA 1. ;ater fro reatent ac*a0e to 'tora0e an*$

P4ase Liquid Liquid

e$#erature@ GCH 35.0 35.0 2. ;ater fro an*$ to f+rt!er treatent

Pressure@ P &PaaH 101.33 201.33

Mass Flo6rate &'/4H 2@000 2@000

"es'! Mar'! 0I 0I

"es'! Flo6 &'/4H 2@000 2@000

A%tual "e!st* &'/$JH 1000.00 1000.00

A%tual :s%ost* %PH 0.>00 0.>00

(%&) SP)C%0%CAT%,&

;o$!al "a$eter $$H 200 150

P#!' #e%%ato! A AC

A; Rat!' 150 150

P#e %4eule 20 40

P#e !ter!al "a$eter $$H 20. 15.1

,ser !#ut P#e " $$H


P#e Rou'4!ess $$H 0.0 0.0

OUTPUT


Flu :elo%t* $/sH $253 $2>5

Re*!ols ;u$er >9@90 120@510

"ar%* Fr%to! Fa%tor 0.019 0.019

Pressure "ro# &Pa/100$H $23; 124#

:elo%t* "es'! Ra!'e $/sH 2.5 1.5

"P "es'! Ra!'e &Pa/100$H 23 - 35 5 - 1

C,&C(+S%,&S

1$$ mm &< =%ne no c!an0e$

Therefore the recommended line si7e for >89+D9A94#3;/36 is #3$ mm & is

Vapour Criteria

(i=uid Criteria

P%P) %!

Liquid Liquid

A AC

20 40

CS CS


27/31

leE///var/666/a##s/%o!verso!/t$#/s%rat%4L2/293701913.xls 293701913.xls reate =ater3

CALCULATION SHEET






A 6-Sep-04 0 11-Feb-05 PWH

S%&'() P*AS) PR)SS+R) !R,P -(%.+%! ,R 'AS



INPUT

+!e ;u$er 3-,=-A-029/30 2-,=-A-1/>

Mass D !er'* Bala!%e trea$ ;o. 1. reated ;ater to >$er$

PR,C)SS !ATA

P4ase Liquid Liquid 2. Pota7#e ;ater to +$er$

e$#erature@ GCH 35.0 35.0

Pressure@ P &PaaH 501.33 501.33

Mass Flo6rate &'/4H 21@000 >@00

"es'! Mar'! 0I 0I

"es'! Flo6 &'/4H 21@000 >@00

A%tual "e!st* &'/$JH 1000.00 1000.00

A%tual :s%ost* %PH 0.>00 0.>00

(%&) SP)C%0%CAT%,&

;o$!al "a$eter $$H >0 50

P#!' #e%%ato! A A

A; Rat!' 150 150

P#e %4eule 40 40

P#e !ter!al "a$eter $$H 77.9 52.5

,ser !#ut P#e " $$H


P#e Rou'4!ess $$H 0.0 0.0

OUTPUT


Flu :elo%t* $/sH #211 #2$6

Re*!ols ;u$er 119@150 70@70

"ar%* Fr%to! Fa%tor 0.020 0.023

Pressure "ro# &Pa/100$H #:23; 13215

:elo%t* "es'! Ra!'e $/sH 1.> 1.>

"P "es'! Ra!'e &Pa/100$H 23 - 35 23 - 35

C,&C(+S%,&S

Therefore the recommended line si7e for 589+D9A94$1:/5$ is 6$ mm &>/>6 is 3$ mm &/005>9-PR-CA-002@ Rev. 0@ ssue or ,se@ 1>-Fe-99

INPUT

+!e ;u$er 3-,=-A-029/30

Mass D !er'* Bala!%e trea$ ;o. reated ;ater to >$er$

PR,C)SS !ATA

P4ase Liquid Liquid

e$#erature@ GCH 35.0

Pressure@ P &PaaH 501.33

Mass Flo6rate &'/4H 37@>00

"es'! Mar'! 0I

"es'! Flo6 &'/4H 37@>00

A%tual "e!st* &'/$JH 1000.00

A%tual :s%ost* %PH 0.>00

(%&) SP)C%0%CAT%,&

;o$!al "a$eter $$H >0

P#!' #e%%ato! A A

A; Rat!' 150 150

P#e %4eule %0 40

P#e !ter!al "a$eter $$H 73.7

,ser !#ut P#e " $$H


P#e Rou'4!ess $$H 0.0 0.0

OUTPUT

P#e Cross-se%to!al Area $KH 0.002 :A+,

Flu :elo%t* $/sH 124> @!%V/$

Re*!ols ;u$er 22@>70 ":/0

"ar%* Fr%to! Fa%tor 0.019 ":/0

Pressure "ro# &Pa/100$H ;:265 @!%V/$

:elo%t* "es'! Ra!'e $/sH 0. to .> 1.>

"P "es'! Ra!'e &Pa/100$H to 5 23 - 35

C,&C(+S%,&S

The velocity is in the middle of the range? and Bhile the pressure drop is higher than recommended this is only an intermittent

stream floB at this high rate2 6$ mm &/005>9-PR-CA-002@ Rev. 0@ ssue or ,se@ 1>-Fe-99

INPUT 1 2 JAB-CPF1-PID-2199-1

+!e ;u$er >-=-A-501

Mass D !er'* Bala!%e trea$ ;o. Pu$# P-5>A/B 1. ;!%te ?%#e R%ver ;ater =%ft P+$< P-,6A/B

PR,C)SS !ATA d%$c!ar0e #%ne.

P4ase Liquid Liquid Rated caac%t 91. 3/!r. (D+r%n0 ra%n%n0 $ea$on)

e$#erature@ GCH 7.5 0.0 Proert%e$ ta*en fro ;!%te ?%#e R%ver ;ater =%ft

Pressure@ P &PaaH 301.33 0.00 P+$< P-,6A/B data$!eet.

Mass Flo6rate &'/4H >5@200 0

"es'! Mar'! 0I 0I

"es'! Flo6 &'/4H >5@200 0

A%tual "e!st* &'/$JH 1200 0

A%tual :s%ost* %PH 1.1 1.1

(%&) SP)C%0%CAT%,&

;o$!al "a$eter $$H 150 150

P#!' #e%%ato! A A

A; Rat!' 150 150

P#e %4eule 40 40

P#e !ter!al "a$eter $$H 15.1 15.1

,ser !#ut P#e " $$H


P#e Rou'4!ess $$H 0.0 0.0

OUTPUT


Flu :elo%t* $/sH #2$> @!%V/$

Re*!ols ;u$er 177@790 ":/0

"ar%* Fr%to! Fa%tor 0.01> ":/0

Pressure "ro# &Pa/100$H ;26> @!%V/$

:elo%t* "es'! Ra!'e $/sH 1.> to .3 2.1 - 2.7

"P "es'! Ra!'e &Pa/100$H 35 to 5 - 5

C,&C(+S%,&S

Therefore the recommended line si7e for Pump? P934>6A/< dischrge is #3$ mm &/005>9-PR-CA-002@ Rev. 0@ ssue or ,se@ 1>-Fe-99

INPUT 1 2 JAB-CPF1-PID-2199-1

+!e ;u$er -=-A-502 -=-A-503

Mass D !er'* Bala!%e trea$ ;o. P-5 u%to! P-5 "s%4ar'e 1. Raw ;ater Pre-treatent Pac*a0e A-,63

PR,C)SS !ATA d%$c!ar0e #%ne.

P4ase Liquid Liquid Rated caac%t 91. 3/!r

e$#erature@ GCH 7.5 7.5 .

Pressure@ P &PaaH 301.33 301.33 2. '+ct%on #%ne of Pre-reatent ;ater ran$fer

Mass Flo6rate &'/4H 3@000 3@000 P+< P-,6A/B

"es'! Mar'! 0I 0I Rated Caac%t 2. 3/!r

"es'! Flo6 &'/4H 3@000 3@000

A%tual "e!st* &'/$JH 1000 1000 Proert%e$ ta*en fro Pre-reatent ;ater

A%tual :s%ost* %PH 1.000 1.000 ran$fer P+< P-,6A/B data$!eet.

(%&) SP)C%0%CAT%,&

;o$!al "a$eter $$H 150 100

P#!' #e%%ato! A A

A; Rat!' 150 150

P#e %4eule 40 40

P#e !ter!al "a$eter $$H 15.1 102.3

,ser !#ut P#e " $$H


P#e Rou'4!ess $$H 0.0 0.0

OUTPUT


Flu :elo%t* $/sH $2>4 #243

Re*!ols ;u$er 9>@700 1>@720

"ar%* Fr%to! Fa%tor 0.020 0.019

Pressure "ro# &Pa/100$H 12>$ #:2:$

:elo%t* "es'! Ra!'e $/sH 1.5 2.5

"P "es'! Ra!'e &Pa/100$H 1 to 5 23 - 35

C,&C(+S%,&S

Therefore the recommended line si7e for A934>5 discharge line? RaB Dater is #3$ mm &>A/< discharge line? RaB Dater is #$$ mm &/005>9-PR-CA-002@ Rev. 0@ ssue or ,se@ 1>-Fe-99

INPUT (P&ID: JAB-CPF1-PID-2199-1)

+!e ;u$er 3-=-A-50 -=-A-50

Mass D !er'* Bala!%e trea$ ;o. e$e!t "s#osal +!e e$e!t "s#osal +!e 'ed%ent d%$o$a# #%ne

PR,C)SS !ATA Rated caac%t 39. 3/!r

P4ase Liquid Liquid Den$t%t and v%$co$%t a$$+ed a$ 13 *0/3

e$#erature@ GCH 50 50 and 1.3 cP con$%der%n0 t!e water %@ w%t! t!e

Pressure@ P &PaaH 200 200 $#+d0e.

Mass Flo6rate &'/4H 3@00 3@00

"es'! Mar'! 0I 0I

"es'! Flo6 &'/4H 3@00 3@00

A%tual "e!st* &'/$JH 1300.00 1300.00

A%tual :s%ost* %PH 1.3 1.3

(%&) SP)C%0%CAT%,&

;o$!al "a$eter $$H >0 150

P#!' #e%%ato! A A

A; Rat!' 150 150

P#e %4eule 40 40

P#e !ter!al "a$eter $$H 77.9 102.3

,ser !#ut P#e " $$H


P#e Rou'4!ess $$H 0.0 0.0

OUTPUT


Flu :elo%t* $/sH #2>5 $2:3

Re*!ols ;u$er 127@090 9@>0

"ar%* Fr%to! Fa%tor 0.020 0.020

Pressure "ro# &Pa/100$H 442:1 ##23>

:elo%t* "es'! Ra!'e $/sH 1.5 - 2. 1.5 - 2.

"P "es'! Ra!'e &Pa/100$H 110.0 110.0

C,&C(+S%,&S

Therefore the recommended line si7e for sediment disposal line is 6$ mm &

Documents

CPF-010 Utility Line Sizing Attachment_0.xls