3PHASE Gas Separator - V2105_4.7x16_for_ Original

PETROFAC JOB NO: JI - 182

HARWEEL CLUSTER PHASE 2 FACILITIES

Calculation S!!t Ra"a" #a$ S!%a&ato& '-2()1

O

2*1+*2)),

AS

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ATE

PRP B3

CH B3

APP B3

I$$u!. /o& Cli!nt0$ A%%&oal APP B3

ESCRIPTION

fle:///var/www/apps/conversion/tmp/scratch_5/293311022.xls

PROJ4 EN#

SI#N

PO APPRO'AL

fle:///var/www/apps/conversion/tmp/scratch_5/293311022.xls

!$i5n Ba$i$:

1.

!.

The separator shall be designed to contain hydrodynamic slugs expected from the trunklines between the Normal Operating Level and the high level alarm.This shall be taken as 30m3 reuired volume but shall be confirmed by hydraulic calculations. The following should be the minimum performance reuirements" reuirements" a# $aximum Liuid 5arry&Over in the vapour " 0.0-32 m 31$$m3 b# $aximum $aximum %as carry&u carry&unde nderr in the liuid liuid"" !' (vol#. (vol#. c# $aximum pressure pressure drop between inlet )lange )lange and gas outlet outlet flange" *0mbar d# $inimum Liuid +esidence +esidence Time within the settling ,one" ,one" * minutes minutes (both oil and water# water# e# The water water separated separated shall shall contain no droplets droplets greator greator than -00 microns. f# hen the /nlet water cut is less than *'(vol.# then the separator separator shall be operated as two&phase separator. separator.

3.

The separa separator tor desig design n pres pressur sure e shall shall be " ) 1 -!-!-

2.

The separat separator or shall shall be provided provided with with two two manholes manholes providin providing g human human access for for vessel entry entry for for sludge sludge removal removal .

*.

ampling ampling points points shall be provid provided ed on the the feed inlet4 inlet4 gas gas and liuid liuid outlet outlet lines lines as close as as possible possible to enable enable performa performance nce to be measured.amples from each stream are analysed for oil in water concentrations4 water in oil concentrations4 liuid in gas carry over and compositions of each stream.

DOC O. !"#/0/31$/1$/1D/%/0

Calculation sheet

5lient 6ro8ect Location

6etroleum 7evelopment Oman 9arweel 5luster 6hase ! )acilities Oman

5alc No $ade by 5hecked by

: ;<

Ba$i$ 7etermine vessel si,ing in line with hell 7=6 criteria and )unctional pecifications. 7etermine vessel design conditions !$i5n Ca$!$ $aximum si,ing cases are determined from final simulation for 6hase !5 cases.

+abab eparator

$ax %as

$ax Oil

$ax ater

6!5 9igh ater !00>4 ummer

6!5 9igh ater !00>4 ummer

6!5 9igh ater !00>4 inter

-!0 barg ?!@5

Operating 6ressure Operating Temperature

!$i5n Con.ition$ 7esign 6ressure 7esign Temperature

>> barg !0&*0@5

P!&/o&6anc! C&it!&ia The following should be the minimum performance reuirements" a# $aximum Liuid 5arry&Over in the vapour " 0.0-32 m31$$m3 b# $aximum %as carry&under in the liuid" !' (vol#. c# $aximum pressure drop between inlet )lange and gas outlet flange" *0mbar d# $inimum Liuid +esidence Time within the settling ,one" * minutes (both oil and water# between L:L and L:9 e# The water separated shall contain no droplets greator than -00 microns. f# 3 minutes hold up time f or control volume is considered between L:L to L:9. Slu5 'olu6! : slug volume of 30 mA is reuired between NLL B L:9 (refer to =9$1021!0-1)10-03# !$i5n 7a&5in )or 6hase !5 a design margin of !0' will be added4 3 trains )or 6hase !:1!C no design margin will be added4 ! trains P&!li6ina& No99l! Location$ NN! N2 N3 $eshpad eir 6late )low 7ist essel 7ia Tan Length

-3-* ?330 ?*D0 ?0D0 E-E0 ?*D0 -3-*

(reference point is from the inlet tan line) mm mm mm mm mm mm mm

!.E? m >.*D m

DOC O. !"#/0/31$/19/1D/%/0

7ate 7ate

.

->&)eb&0D

DOC O. !"#/0/31$/20/1D/%/0 /N6FT /N)O+$:T/ON )O+ =6:+:TO+ 6+O%+:$ 6+O<=5T No." heatstone 5L/=NT " 6+O<=5T " ==L 7=5+/6T/ON" $ultiuse separator T:;= /NTO :55OFNT 9=:7 OLF$=G

H (H1N#

5:=

-

5:= T/TL=

7esign

! ell clean up

3 Turndown

2 )ree flow

* -0m3 oil slug on case2

:T=+ COOT )/TT=7G (H1N# 5=NT+:L /NL=TG (H1N#

N N

N N

N N

N N

N N

%: $OL=5FL:+ =/%9T

!0.0

->.!

->.-

!0.!

!0.!

?* 0 0 0 ?*

!0 0 0 0 !0

!0 0 0 0 !0

?* 0 0 0 ?*

?* 0 0 0 ?*

barg bara kg1cmI&g kg1cmI&a kpa&g kpa&a psig psia bara

0.0 E!.2 0 0 0 0 0 0 E!.2

0.0 >>.? 0 0 0 0 0 0 >>.E*

0.0 E!.2 0 0 0 0 0 0 E!.2

0.0 -3E.2 0 0 0 0 0 0 -3E.2

0.0 -3E.2 0 0 0 0 0 0 -3E.2

kg1mA lb1ftA .% kg1mA

*3.0 0 0 *3.00

-0-.0 0 -0-.-0

D?.* 0 0 D?.*0

-0*.> 0 0 -0*.>0

-0*.> 0 0 -0*.>0

kg1mA lb1ftA kg1mA

D>>.0 0 D>>

DDD.0 0 DDD

D?D.0 0 D?D

DDD.0 0 DDD

DDD.0 0 DDD

kg1mA lb1ftA kg1mA

-000.0 0 -000

-02E.0 0 -02E

-02*.0 0 -02*

-00E.0 0 -00E

-00E.0 0 -00E

Fsed unit

c6 c 6a.s c6

0.0-*3 0 0 0.0-*3

0.0-*3 0 0 0.0-*3

0.0-3E 0 0 0.0-3E

0.0-E> 0 0 0.0-E>

0.0-E> 0 0 0.0-E>

L/JF/7 /5O/TH

Fnit

c6

(c64c46a.s#

0.*E0.3*2

-.DD0.3*D

-.E?! 0.202

0.D>0.!>D

0.D>0.!>D

T=$6=+:TF+=

Fsed unit

6+=F+=

Fsed unit

%: 7=N/TH

Fsed unit

O/L 7=N/TH Fsed unit

:T=+ 7=N/TH Fsed unit

%: /5O/TH

@5 @) + ; @5

ater Oil

DOC O. !"#/0/31$/21/1D/%/0 5:=

-

5:= T/TL=

%: )LO

7esign

! ell clean up

3 Turndown

2 )ree flow

* -0m3 oil slug on case2

$$5)7 $$5$7 $$N5$7 scf1bbl scm1bbl kg1hr lb1hr mA1hr ftA1hr kg1hr 7=/%N )LO

0 0 0 0 0 !2?E?E 0 0 0 !2?E?E !2?E?E.0

0 0 0 0 0 332D00 0 0 332D0332D0-.0

0 0 0 0 0 2EE** 0 0 0 2EE** 2EE**.0

0 0 0 0 0 3!0000 0 0 0 3!0000 3!0000.0

0 0 0 0 0 3!0000 0 0 0 3!0000 3!0000.0

bbl1d kg1hr lb1hr mA1hr ftA1hr kg1hr 7=/%N )LO

0 3>!-? 0 0 0 3>!-? 3>!-?.0

0 DE-?3 0 0 0 DE-?3 DE-?3.0

0 !!DE 0 0 0 !!DE !!DE.0

0 DE-?3 0 0 0 DE-?3 DE-?3.0

0 E3?23 0 0 0 E3?23 E3?23.0

bbl1d kg1hr lb1hr mA1hr ftA1hr kg1hr 7=/%N )LO

0 2??>! 0 0 0 2??>! 2??>!.0

0 2E0>E 0 0 0 2E0>E 2E0>E.0

0 *>> 0 0 0 *>> *>>.0

0 2??>! 0 0 0 2??>! 2??>!.0

0 2??>! 0 0 0 2??>! 2??>!.0

0.>-*0

0.E?*0

0.?300

0.??00

0.??00

7+O6L=T 7=/%N $:+%/N ('#

0

0

0

0

0

F+%= ):5TO+ ('#

0

0

0

0

0

=LL ):5TO+ ('#

0

0

0

0

0

*3.--*

-00.-0-

D?.*3E

-0D.0-E

0.000

Fsed unit

O/L )LO

Fsed unit

:T=+ )LO

Fsed unit

%: 5O$6+=/C/L/TH ):5TO+

%: 7=N/TH (=T#

kg1mA

DOC O. !"#/0/31$/22/1D/%/0

D -0m3 water slug on case 2 N N !0.!

?* 0 0 0 ?*

0.0 -3E.2 0 0 0 0 0 0 -3E.2

-0*.> 0 0 -0*.>0

DDD.0 0 DDD

-00E.0 0 -00E

0.0-E> 0 0 0.0-E>

0.D>0.!>D

DOC O. !"#/0/31$/23/1D/%/0 D -0m3 water slug on case 2 0 0 0 0 0 3!0000 0 0 0 3!0000 3!0000.0

0 DE-?3 0 0 0 DE-?3 DE-?3.0

0 *?>D! 0 0 0 *?>D! *?>D!.0 0.??00 0 0 0

0.000

DOC O. !"#/0/31$/2%/1D/%/0

3 69:= 9O+/KONT:L =6:+:TO+ 6ro8ect No. " 5lient 5ONT+:5T " ==L +=) "

heet " 7ate " -2&)eb&0D +ev " 0 Cy " :

heatstone 0 0 $ultiuse separator 5:= NO " 5:= T/TL= " 7esign COOT )/TT=7 " N 5=NT+:L /N " N

Operating 6ressure Operating Temperature /nlet ater in Oil %as )raction Liuid 7ensity '!$$!l .ata essel /7 Tan 1 Tan Length 9=$/ O+ !"- =LL/6 9=:7 "

7esign Temperature 7esign 6ressure hell Thickness 5orrosion :llowance hell eight 9ead eight No,,le eight Total '!$$!l W!i5t ater )illed eight

T:N TO =/+ " =))=5T/= =6 L=N%T9 O/L " =))=5T/= =6 L=N%T9 :T=+ " 9=/%9T O) =/+ " TOT:L ==L OLF$= "

E!.20 ?*.00 2D.*D' 0.E3? 0.>E? ?3>.!

bara @5 CB v1v w1w v1v kg1mA

!.E?0 >.*D0 9 -00 -*! --?.!0 3 E?!D! !!>2E -*D*! 11,8,1 D>!?!

m m (91=# deg5 barg mm mm kg kg kg 5 kg

-

P&oc!$$ F!!. St&!a6 Su66a& Total mass flow  33D?>E kg1hr $ean density  E0.!00 kg1mA %: !2?E?E.00 kg1hr *3.00 kg1mA 0.0-* c6

Total flow rate  Total liuid flow  O/L 3>!-?.00 kg1hr D>>.00 kg1mA 0.3*2 c6

:T=+ 2??>!.00 kg1hr -000.00 kg1mA 0.*E- c6

-.333 mA1s 0.0!> mA1s )low 7ensity iscosity

No99l! Si9in5 Sc!.ul! N.C in )LF/7 /N

/.7 m -?

Pipe Sch. %: OFT

!0 Pipe Sch.

O/L OFT

? Pipe Sch.

:T=+ OFT

D Pipe Sch. FLAN#E TO FLAN#E PRESSURE ROP

?.*D0 E.*D0 E.0D0 -.0?0 D>.!?

m m m m mA

0.2-> 60 0.2*D 80 0.->> 60 0.-*2 40

5alculate +esidence time based on Tan LengthG (H1N# Length used for oil phase residence time calculation Length used for water phase residence time calculation

elocity m1s >.DD

rho&vI kg1msI D***

6ressure drop mbar 3!.?

?.00

33>0

-0.!

0.*0

-EE

0.*

0.E3

*30

-.D

Check mom

()4;

3 8.56 m 8.56 m

DOC O. !"#/0/31$/25/1D/%/0

Li
Level m

Oil Oil Oil Oil Oil Oil Oil

99LL(!# 99LL 9LL NLL NLL LLL LLLL W!i& !i5t ater 99/L ater 9/L ater NIL ater N/L ater L/L ater LL/L Fllage

essel fill '

-.*>0 -.*>0 -.2>0 1418) -.-?0 -.0?0 0.D?0 14)8) -.0?0 0.>?0 )4(>) 0.*30 0.200 0.300 0.000

*E.! *E.! *3.D +24+ 2!.2 3?.? !2.*

without coalescing packs

  

:5TF:L O/L 7+O6L=T +=JF/+=7 O/L /N :T=+ T:+%=T O/L 7+O6L=T

 

!.2? mI -.->0 m

ill /nlet 7evice fit adeuatelyG

0.0?D 0.0?> 0.>*E

φwm = elected λ =

0.002 0.0E0

!.?*

)or a meshpad B schoepentoeter (refer to 7=6 3-.!!.0*.--&%en ept !00!#

*.33* mI Less than actual gas space! Consult Prinicipal to see if it is acceptable

$ax. 7roplet to approach vane pack %as space axial velocity

0.03?

D0 microns 0.*!D m1s

m1s between N/L B microns between N/L B percent v1v microns

DD microns between N/L B essel bottom ppm v1v -00 microns

If a vane pack, use 0.1 to allow for slugs. If a bare vessel, use 0.07 +ecommended %as )low :rea

!.*? -0.*3 =4++ !.*3 -.E3.!0.00

)4)1,8

0.00> 2! -00

Hes

λ= φ= f η  f φ 

olume between levels mA 0.00 3.!2 -0.0> 1(4=+ 3.!0 !.0E !.00 MM

+esidence time mins (/ncluding heads# 0.00 3.2E -0.E> 1,48> 3.2! !.!! !.-3

/nterval

99LL199LL(!# 9LL199LL NLL19LL NIL to LLL1NLL LLLL1LLL C1LLLL

3.-E -!.>! ;41> 3.-0 !.-0 3.>3

9/L199/L N/L19/L NIL to L/L1N/L LL/L1L/L L/LL to

!> microns to NLL

:/:L )LF/7 =LO5/TH :5TF:L :T=+ 7+O6L=T +=JF/+=7 :T=+ /N O/L T:+%=T :T=+ 7+O6L=T

#AS CAP ANAL3SIS :ctual %as pace :rea %as 5ap height

)4));(

3?.? 3*.3 1;41 ->.-2.2 -0.?

)+O$ TO;= L: %: CFCCL= =6:+:T=7  %: +=$:/N/N% :T/)/= =JF/L/C+/F$ 5ON7/T/ON


:xial velocity m1s

NLL NLL

0.00D m1s between N/L B 2- microns between N/L B percent v1v

DD microns between N/L B essel botto ppm v1v

DOC O. !"#/0/31$/2)/1D/%/0

of

=rosion vel m1s -2.*D -D.ED 2.D3.?D 6"a&

DOC O. !"#/0/31$/2*/1D/%/0

NLL

B'

C

99LL 99LL

m

DOC O. !"#/0/31$/2$/1D/%/0

3 69:= 9O+/KONT:L =6:+:TO+ heet " 7ate " -2&)eb&0D +ev " 0 Cy " :

6ro8ect No. " heatstone 5lient 0 5ONT+:5T " 0 ==L +=) " $ultiuse separator 5:= NO " ! 5:= T/TL= " ell clean up COOT )/TT=7 " N 5=NT+:L /N " N




>>.E* !0.00 30.?2' 0.E2* 0.>*? E?3.*


!.E?0 >.*D0 9 ?! -!0 --?.!0 3 E?!D! !!>2E -*D*! 11,8,1 D>!?!


P&oc!$$ F!!. St&!a6 Su66a& Total mass flow  22???- kg1hr $ean density  -!>.>0* kg1mA %: 332D0-.00 kg1hr -0-.-0 kg1mA 0.0-* c6

Total flow rate  Total liuid flow  O/L DE-?3.00 kg1hr DDD.00 kg1mA 0.3*D c6

:T=+ 2E0>E.00 kg1hr -02E.00 kg1mA -.DD- c6

0.>D0 mA1s 0.02- mA1s )low 7ensity iscosity


/.7 m -?

Pipe Sch. %: OFT

!0 Pipe Sch.

O/L OFT

? Pipe Sch.

:T=+ OFT


?.*D0 E.*D0 E.0D0 -.0?0 D>.!?

m m m m mA

0.2-> 100 0.2*D 100 0.->> 100 0.-*2 40


elocity m1s D.>D

rho&vI kg1msI D!?>

6ressure drop mbar 3-.2

*.D2

3!-*

>.D

0.>-

*2D

-.D

0.DE

2E0

-.2

Check mom

+;41

3 8.56 m 8.56 m

DOC O. !"#/0/31$/29/1D/%/0

Li
Level m

essel fill '


-.*>0 -.*>0 -.2>0 1418) -.-?0 -.0?0 0.D?0 14)8) -.0?0 0.>?0 )4(>) 0.*30 0.200 0.300 0.000

*E.! *E.! *3.D +24+ 2!.2 3?.? !2.*



  


 

!.2? mI -.->0 m


0.02? 0.-!3 0.*D3?E?0?30.>2!


0.00D 0.0E0

!.?*


*.**D mI Less than actual gas space! Consult Prinicipal to see if it is acceptable


0.03*



>D microns between N/L B essel bottom ppm v1v -00 microns


!.*? -0.*3 =4++ !.*3 -.E3.!0.00

)4)1((

0.0-E *0 0.* -00

Hes

λ= φ= f η  f φ 


+esidence time mins (/ncluding heads# 0.00 -.>3 D.00 ;4>, -.>0 -.!3 -.->

/nterval


3.22 -2.02 ;4;> 3.3E !.!? 2.!?


2- microns to NLL



)4)1=)

3?.? 3*.3 1;41 ->.-2.2 -0.?



:xial velocity m1s

NLL NLL

0.0-0 m1s between N/L B 2> microns between N/L B percent v1v

>D microns between N/L B essel botto ppm v1v

DOC O. !"#/0/31$/30/1D/%/0

of

=rosion vel m1s -0.E0 -!.-3 2.E3 3.EE 6"a&

DOC O. !"#/0/31$/31/1D/%/0

NLL

B'

C

99LL 99LL

m

DOC O. !"#/0/31$/32/1D/%/0


6ro8ect No. " heatstone 5lient 0 5ONT+:5T " 0 ==L +=) " $ultiuse separator 5:= NO " 3 5:= T/TL= " Turndown COOT )/TT=7 " N 5=NT+:L /N " N




E!.20 !0.00 -2.E?' 0.>23 0.>>2 E3>.-


!.E?0 >.*D0 9 -00 -*! --?.!0 3 E?!D! !!>2E -*D*! 11,8,1 D>!?!


P&oc!$$ F!!. St&!a6 Su66a& Total mass flow  *0D!- kg1hr $ean density  E!.!0> kg1mA %: 2EE**.00 kg1hr D?.*0 kg1mA 0.0-2 c6

Total flow rate  Total liuid flow  O/L !!DE.00 kg1hr D?D.00 kg1mA 0.202 c6

:T=+ *>>.00 kg1hr -02*.00 kg1mA -.E?! c6

0.->* mA1s 0.00- mA1s )low 7ensity iscosity


/.7 m -?

Pipe Sch. %: OFT

!0 Pipe Sch.

O/L OFT

? Pipe Sch.

:T=+ OFT


?.*D0 E.*D0 E.0D0 -.0?0 D>.!?

m m m m mA

0.2-> 100 0.2*D 100 0.->> 100 0.-*2 40


elocity m1s -.2-

rho&vI kg1msI -22

6ressure drop mbar 0.E

-.->

>E

0.3

0.03

-

0.0

0.0-

0

0.0 ;4)

3 8.56 m 8.56 m

DOC O. !"#/0/31$/33/1D/%/0

Li
Level m

essel fill '


-.*>0 -.*>0 -.2>0 1418) -.-?0 -.0?0 0.D?0 14)8) -.0?0 0.>?0 )4(>) 0.*30 0.200 0.300 0.000

*E.! *E.! *3.D +24+ 2!.2 3?.? !2.*



  


 

!.2? mI -.->0 m



0.0*0 0.0-? 0.*D!!>23-2!


0.>>0.000.0E0

0.>!- mI


0.000



-! microns between N/L B essel bottom ppm v1v -00 microns

!.?*


!.*? -0.*3 =4++ !.*3 -.E3.!0.00

)4)))2

0.00-0 -00

Hes

λ= φ= f η  f φ 


+esidence time mins (/ncluding heads# 0.00 *?.?* -?3.-3 28(4=+ *?.0! 3E.D! 3D.!3

/nterval


!E0.-D --0-.>* ==;4)+ !D2.20 -E>.0* 33*.*>


? microns to NLL



)4))),

3?.? 3*.3 1;41 ->.-2.2 -0.?



:xial velocity m1s

NLL NLL

0.000 m1s between N/L B -0 microns between N/L B percent v1v

-! microns between N/L B essel botto ppm v1v

DOC O. !"#/0/31$/3%/1D/%/0

of

=rosion vel m1s -2.3D -2.E2 2.DD 3.EE 6"a&

DOC O. !"#/0/31$/35/1D/%/0

NLL

B'

C

99LL 99LL

m

DOC O. !"#/0/31$/3)/1D/%/0


6ro8ect No. " heatstone 5lient 0 5ONT+:5T " 0 ==L +=) " $ultiuse separator 5:= NO " 5:= T/TL= " )ree flow COOT )/TT=7 " N 5=NT+:L /N " N




-3E.20 ?*.00 3!.2>' 0.E32 0.>*3 EED.?


!.E?0 >.*D0 9 -00 -*! --?.!0 3 E?!D! !!>2E -*D*! 11,8,1 D>!?!


2

P&oc!$$ F!!. St&!a6 Su66a& Total mass flow  23D0E* kg1hr $ean density  -3E.*-3 kg1mA %: 3!0000.00 kg1hr -0*.>0 kg1mA 0.0-? c6

Total flow rate  Total liuid flow  O/L DE-?3.00 kg1hr DDD.00 kg1mA 0.!>D c6

:T=+ 2??>!.00 kg1hr -00E.00 kg1mA 0.D>- c6

0.??- mA1s 0.02! mA1s )low 7ensity iscosity


/.7 m -?

Pipe Sch. %: OFT

!0 Pipe Sch.

O/L OFT

? Pipe Sch.

:T=+ OFT


?.*D0 E.*D0 E.0D0 -.0?0 D>.!?

m m m m mA

0.2-> 100 0.2*D 100 0.->> 100 0.-*2 40


elocity m1s D.3>

rho&vI kg1msI *D0E

6ressure drop mbar !?.0

*.-*

!?0E

?.2

0.>-

*2D

-.D

0.E!

*!E

-.D ++4+

3 8.56 m 8.56 m

DOC O. !"#/0/31$/3*/1D/%/0

Li
Level m



essel fill '

-.*>0 -.*>0 -.2>0 1418) -.-?0 -.0?0 0.D?0 14)8) -.0?0 0.>?0 )4(>) 0.*30 0.200 0.300 0.000

*E.! *E.! *3.D +24+ 2!.2 3?.? !2.*


  


 

!.2? mI -.->0 m


0.0?2 0.-32 0.>3E


0.00E 0.0E0

!.?*


*.!-2 mI Less than actual gas space! Consult Prinicipal to see if it is acceptable


0.03?



D? microns between N/L B essel bottom ppm v1v -00 microns


!.*? -0.*3 =4++ !.*3 -.E3.!0.00

)4)1,=

0.0-E 2? 0.* -00

Hes

λ= φ= f η  f φ 



/nterval


3.-> -3.0;42) 3.-! !.-3.>D


3? microns to NLL



)4)1=)

3?.? 3*.3 1;41 ->.-2.2 -0.?



:xial velocity m1s

NLL NLL

0.0-0 m1s between N/L B 2E microns between N/L B percent v1v

D? microns between N/L B essel botto ppm v1v

DOC O. !"#/0/31$/3$/1D/%/0

of

=rosion vel m1s -0.20 --.?D 2.E3 3.?2 6"a&

DOC O. !"#/0/31$/39/1D/%/0

NLL

B'

C

99LL 99LL

m

DOC O. !"#/0/31$/%0/1D/%/0


6ro8ect No. " heatstone 5lient 0 5ONT+:5T " 0 ==L +=) " $ultiuse separator 5:= NO " * 5:= T/TL= " -0m3 oil slug on case2 COOT )/TT=7 " N 5=NT+:L /N " N




-3E.20 ?*.00 30.2*' 0.E!3 0.>*0 ED>.?


!.E?0 >.*D0 9 -00 -*! --?.!0 3 E?!D! !!>2E -*D*! 11,8,1 D>!?!


P&oc!$$ F!!. St&!a6 Su66a& Total mass flow  22!E3* kg1hr $ean density  -3>.-E* kg1mA %: 3!0000.00 kg1hr -0*.>0 kg1mA 0.0-? c6

Total flow rate  Total liuid flow  O/L E3?23.00 kg1hr DDD.00 kg1mA 0.!>D c6

:T=+ 2??>!.00 kg1hr -00E.00 kg1mA 0.D>- c6

0.??2 mA1s 0.022 mA1s )low 7ensity iscosity


/.7 m -?

Pipe Sch. %: OFT

!0 Pipe Sch.

O/L OFT

? Pipe Sch.

:T=+ OFT


?.*D0 E.*D0 E.0D0 -.0?0 D>.!?

m m m m mA

0.2-> 100 0.2*D 100 0.->> 100 0.-*2 40


elocity m1s D.2-

rho&vI kg1msI *E-0

6ressure drop mbar !?.D

*.-*

!?0E

?.2

-.00

DD0

!.0

0.E!

*!E

-.D +(4)

3 8.56 m 8.56 m

DOC O. !"#/0/31$/%1/1D/%/0

Li
Level m

essel fill '


-.*>0 -.*>0 -.2>0 1418) -.-?0 -.0?0 0.D?0 14)8) -.0?0 0.>?0 )4(>) 0.*30 0.200 0.300 0.000

*E.! *E.! *3.D +24+ 2!.2 3?.? !2.*



  


 

!.2? mI -.->0 m


0.0?2 0.-2! 0.>32


0.00E 0.0E0

!.?*




0.03?



0 microns between N/L B essel bottom ppm v1v -00 microns


!.*? -0.*3 =4++ !.*3 -.E3.!0.00

)4)1,=

0.0-> 0 0.* -00

Hes

λ= φ= f η  f φ 


+esidence time mins (/ncluding heads# 0.00 -.E* *.2D 84(2 -.E3 -.-! -.0?

/nterval


3.-> -3.0;42) 3.-! !.-3.>D


3> microns to NLL



)4)18=

3?.? 3*.3 1;41 ->.-2.2 -0.?



:xial velocity m1s

NLL NLL

0.0-- m1s between N/L B 0 microns between N/L B percent v1v

P:LF=M

0 microns between N/L B essel botto ppm v1v

DOC O. !"#/0/31$/%2/1D/%/0

of

=rosion vel m1s -0.32 --.?D 2.E3 3.?2 6"a&

DOC O. !"#/0/31$/%3/1D/%/0

NLL

B'

C

99LL 99LL

m

DOC O. !"#/0/31$/%%/1D/%/0


6ro8ect No. " heatstone 5lient 0 5ONT+:5T " 0 ==L +=) " $ultiuse separator 5:= NO " D 5:= T/TL= " -0m3 water slug on case 2 COOT )/TT=7 " N 5=NT+:L /N " N




-3E.20 ?*.00 3D.E3' 0.E-E 0.>*0 E>-.!


!.E?0 >.*D0 9 ?! -!0 --?.!0 3 E?!D! !!>2E -*D*! 11,8,1 D>!?!


P&oc!$$ F!!. St&!a6 Su66a& Total mass flow  22D-2* kg1hr $ean density  -20.!2E kg1mA %: 3!0000.00 kg1hr -0*.>0 kg1mA 0.0-? c6

Total flow rate  Total liuid flow  O/L DE-?3.00 kg1hr DDD.00 kg1mA 0.!>D c6

:T=+ *?>D!.00 kg1hr -00E.00 kg1mA 0.D>- c6

0.??2 mA1s 0.022 mA1s )low 7ensity iscosity


/.7 m -?

Pipe Sch. %: OFT

!0 Pipe Sch.

O/L OFT

? Pipe Sch.

:T=+ OFT


?.*D0 E.*D0 E.0D0 -.0?0 D>.!?

m m m m mA

0.2-> 100 0.2*D 100 0.->> 100 0.-*2 40


elocity m1s D.2-

rho&vI kg1msI *E*2

6ressure drop mbar !?.?

*.-*

!?0E

?.2

0.>-

*2D

-.D

0.?E

EDD

!.3 +(42

3 8.56 m 8.56 m

DOC O. !"#/0/31$/%5/1D/%/0

Li
Level m

essel fill '


-.*>0 -.*>0 -.2>0 1418) -.-?0 -.0?0 0.D?0 14)8) -.0?0 0.>?0 )4(>) 0.*30 0.200 0.300 0.000

*E.! *E.! *3.D +24+ 2!.2 3?.? !2.*



  


 

!.2? mI -.->0 m


0.0?2 0.-22 0.>33


0.00E 0.0E0

!.?*




0.02D



0 microns between N/L B essel bottom ppm v1v -00 microns


!.*? -0.*3 =4++ !.*3 -.E3.!0.00

)4)2)2

0.0-E 0 0.* -00

Hes

λ= φ= f η  f φ 



/nterval


!.D2 -0.E> =4,> !.*> -.E* 3.!>


3? microns to NLL



)4)1=)

3?.? 3*.3 1;41 ->.-2.2 -0.?



:xial velocity m1s

NLL NLL

0.0-0 m1s between N/L B 0 microns between N/L B percent v1v

P:LF=M

0 microns between N/L B essel botto ppm v1v

DOC O. !"#/0/31$/%)/1D/%/0

of

=rosion vel m1s -0.30 --.?D 2.E3 3.?2 6"a&

DOC O. !"#/0/31$/%*/1D/%/0

NLL

B'

C

99LL 99LL

m

+late +ac,

293311022.xls

Cross-low Plate Pack i"ing #$ori"ontal% 5ontract +ef " 7ocument +ef " essel " SI UNITS 5:= " Inl!t con.ition$ 7esign $argin Oil flow (kg1hr# Oil density (kg1mA# Oil iscosity (c6# ater flow (kg1hr# ater density (kg1mA# ater iscosity (c6# ater Loading '(w1w#

-

!

3

2

*

D

14( >;2184) ,;;4) )4>( +88;24) 1)))4) )4(= **.2>0

14( ,=18>4) ,,,4) )4>, +=);=4) 1)+=4) 14,, 2-.!-

14( 22,=4) ,8,4) )4+) (;;4) 1)+(4) 14=8 !0.>0

14( ,=18>4) ,,,4) )4>) +88;24) 1))=4) )4,; 2!.-!

1 =>8+>4) ,,,4) )4>) +88;24) 1))=4) )4,; 3>.?2

1 ,=18>4) ,,,4) )4>) (8;,24) 1))=4) )4,; 2D.E2

$ean inlet density (kg1mA# Total inlet flow (mA1hr# Oil )low (mA1hr# ater )low (mA1hr#

?3>.-D -0*.00 *D.-2?.?>

E?3.*0 -2*.?D -00.?? 22.>?

E3>.0E 3.?? 3.30 0.*E

EED.?0 -2>.23 -00.?? 2?.**

ED>.?* -*>.23 --0.?? 2?.**

E>-.!2 -*>.23 -00.?? *?.**

Plate &eo'etr( Plat! An5l! ?.!5&!!$@ . %% Plat! i$tanc! ?66@

+(

2*

2*

2*

2*

2*

1)

-0

-0

-0

-0

-0

t %% Plat! Ticn!$$ ?66@

1

-

-

-

-

-

L %% L!n5t o/ Plat! ?6@

14)))

-.000

-.000

-.000

-.000

-.000

)4;))

0.>0

0.>0

0.>0

0.>0

0.>0

S!l!ct!. R!nol.$ No

)48)) 8()

0.?0 ?*0

0.?0 ?*0

0.?0 ?*0

0.?0 ?*0

0.?0 ?*0

)in *e+uire'ents for i"ing of ront rea of Plate Pack Oil Plat! Co&&!ction Facto& F

lo$$

Wat!& Plat! Co&&!ction Facto& F

lo$$

d 9 9ydraulic 7iameter (m#

0.0!0

0.0!0

0.0!0

0.0!0

0.0!0

0.0!0

$inimum Oil 6hase 6ack Net )ace :rea (m!#

-.0?D

-.?*0

0.0**

!.!!*

-.D3-

-.2?3

$inimum ater 6hase 6ack Net )ace :rea (m !#

0.?3>

0.!E?

0.003

0.D>2

0.2D!

0.**?

7ini6u6 Total Plat! Pac #&o$$ Fac! A&!a ?6 2@

24+82

24,++

)4)=2

>4,=>

24,2;

24(8)

Oil 6hase 6ack %ross )ace :rea (m !# ater 6hase 6ack %ross )ace :rea (m !#

-.3!E -.-*2

!.!D0.3?!

0.0DE 0.00*

!.E!0 0.>*2

-.>>3 0.D3D

-.?-3 0.EDE

6late 6ack height (m#

-.!00

0.000 0.000

1)) 1)) 0.000 0.000

0.000 0.000

Ta&5!t Oil &o%l!t Si9! ? 6@ Ta&5!t Wat!& &o%l!t Si9! ? 6@ 0.0-0.000 0.000 0.-30.000 0.000

eter'ination of eparation Perfor'ance :xial elocity of Oil (light# section (m1s# :xial elocity of ater (heavy# section (m1s#

0.E?*

Axial velocity shoul not excee 0.015

9==T 7:T= +=//ON

ater phase settling velocity (in light section# (m1s# Oil phase settling velocity (in heavy section# (m1s#

0.000 0.00!0

0.000 0.0000

0.000 0.0000

0.000 0.0000

0.000 0.0000

0.000 0.0000

:ctual ater 7roplet eparation in oil section (µm# :ctual Oil 7roplet eparation in water section (µm#

-> ?2

0 0

0 0

0 0

0 0

0 0

essel etails 9ydrualic 7iameter for Liuid1Liuid eparation (m# $in. /nlet 5ompartment (m# $in. ettling 5ompartment (m# $in. Outlet 5ompartment (m# 7ini6u6 Tan L!n5t ?6@

-.EE? -.3>0 -.D*0 0.D>* (4+)=

-.?3* 0.>-E -.D*0 0.2*> (4+)=

0.30! 0.-*-.D*0 0.0ED (4+)=

!.-D3 -.0?-.D*0 0.*2(4+)=

-.?!> 0.>-* -.D*0 0.2*E (4+)=

-.?-! 0.>0D -.D*0 0.2*3 (4+)=

'!$$!l ia6!t!& ?6@ NIL ?6@

24=8) )42))

%essel Area (m# )

6.0!

&ax Plate Area (m# )

0.1"

0.00

0.00

0.00

0.00

0.00

Actual Plate Area (m# ) NLL ?6@

0.16 142))

0.00

0.00

0.00

0.00

0.00

&ax Plate Area (m# )

#.$1

0.00

0.00

0.00

0.00

0.00

Actual Plate Area (m# )

#.08

0.00

0.00

0.00

0.00

0.00

O) !&Nov&-*

/%N 6+O<=5T +=)

+a-e %$

CONTOURE 'ANE PAC SIIN# 0!&Nov&-* essel ref " $ultiuse separator 5ontract rev " essel i.d Liuid level Q 99LL Top vane overlap hell clearance :d8ust box width ane area ane pitch =ffective diameter ector hgt at d1! ector area

0

!.E?0 -.*>0 0.0!* 0.0*0 0.0?0 -.00D! 0.0-? !.D30 0.000.000

5ontoured 9t.

m m m m m mI m m m mI

5hord 0.-30

5ase $ax rho&vI +e area (mI# :ctual area (mI# ane R;R factor

ector area -.-20

0.0>>?

5ase !

?> -.00D! -.00D! 0.3E-!

Number of anes

Non&cont height 0.?D*

?> 0.>E>? -.00D! 0.3?D*

:ctual 

5ase 3 ?> 0.-D>> -.00D! 0.0D2-

:ctual 9

5ase 2 ?> 0.>-*D -.00D! 0.3D!E

:ctual ector area

5ase * ?> 0.>-*D -.00D! 0.3D!E

5ase D ?> 0.>-*D -.00D! 0.3D!E

:ctual h

D0

-.-!E

0.-!E

0.0>D!

0.?E>

5ase 0.0?* 2.3>2 2.*ED !.2-

5ase ! 0.0?* 2.*ED 2.*ED !.2-

5ase 3 0.0?* 0.E*> 2.*ED !.2-

5ase 2 0.0?* 2.!>2 2.*ED !.2-

5ase * 0.0?* 2.!>2 2.*ED !.2-

-3.000

Fnderside of vanebox to top of vessel (m#

Fnderside of vanebox to high 99LL (m# -.!3-

&0.02-

$=96:7 /K/N% D!E JF:+= /K/N% :ngle idth Length 9eight Top of essel Fnderside of vanebox to top of vessel (m#

D0 -.003 -.003 0.!!0 0.2E2

deg m m m m

; )actor +e area (mI# :ctual area (mI# $espad dia (m#

Fnderside of vanebox to high high li level (m# 0.D>2 0.2>D

Fnderside of ane 6ack from Top of essel 0.D>2 m Fnderside of ane 6ack to 99LL 0.2>D m $ax 99LL available -.?3* m heet " 7ate " 0!&Nov&-* +evision " ignature " Phyp 6ro8ect No."

of P+=)M P+=)M

5ase D 0.0?* 2.!>3> 2.*E*D !.2-

heet " 7ate " +evision " ignature " +eference "

+evision date " -?1031>2 +evision level " 0

of 0!&Nov&-*

59O=6=NTO=T=+ (:N= TH6=# /NL=T 7=/5= 5:L5FL:T/ON 7ocument reference " 6ro8ect reference " 5ustomer " essel reference "

0 heatstone 0 $ultiuse separator

In%ut .ata

Out%ut &!$ult$

essel internal diameter No,,le internal diameter essel orientation ane angle & alpha $aterial of construction

!E?0 2-> 9 = >1,

mm mm (19#  (-D-430243-D# (?!*422D!# > mm >4( ,)) mm N (H1N# 7 ($1N#

ane thickness /nlet 1 Length ratio $anway internal diameter acuum operation =xit manway or no,,le

Inl!t .!ic! t%! 1A 'an! an5l! - al%a 'an! &a.iu$ ?R@ 'an! L!n5t ?L@ E.5! an5l! - "!ta Nu6"!& o/ an!$ %!& $i.! Wo A%%&oDi6at! !i5t S%lit an! la..!&$  No

= 1)) 1)) 1)4)> 12 2,4=+ 1+1

 Nv +ounded Nv =dge angle & beta vo $aximum vane height pace available +euired vane height $aximum ladder height

66 5

%!& $i.! 66 1>1( 66 =>+ 66

A%%&oDi6at! l!n5t A%%&oDi6at! 6aDi6u6 i.t

Int!&6!.iat! calculation$

 66 66

Ta"l! to .!t!&6in! E         

eight of vane ladder  eight of top 1 btm plates  Total overall weight 

3.0ED -!.>D> -! -0.03 !D.E2 *D2.>? -2DE 23> 23>

@ mm mm mm mm mm

7 0 !000 2000

= !0>*.* !0>*.* !0>*.*

Ta"l! to .!t!&6in! L an. R  0 3 D !0

*> kg each !! kg -2- kg

Lv -00 -00 -*0 !00

+v *0 -00 -00 -00

: -D* !-* E-*

C -!0 -E0 23*

Ta"l! to .!t!&6in! A an. B +v *0 -00 300

Not!$ : -.

The value of  is not a physical dimension on the vane type inlet device. /t is purely a ratio used to determine the reuired values of Lv and +v.

!.

The above spreadsheet assists in determining the preliminary layout of the vane type inlet device. )or final dimensions of the vane type inlet device please refer to the fabrication drawings.

C$ +ef " heatstone 5lient16ro8ect +ef " 0 essel " $ultiuse separator 5ase %as density (kg1mA# %as iscosity (c6# %as /nlet flow (mA1hr# Culk Liuid density (kg1mA# :ctual vane area (mI# ane 6ack ; )actor (m1s# ane elocity (m1s#

ane elocity (m1s# -.!>D -.!3-.-DD -.-0-.03E 0.>E! 0.>0E 0.?2! 0.EE? 0.E-3 0.D2? 0.*?3 0.*-? 0.2*2 0.3?> 0.3!2 0.!*> 0.->2 0.-30 0.0D*

=ffective eparator Length (m# %as pace 9eight (m# %as pace :xial velocity (m1s# 7aD4 &o%l!t to a%%&oac an! %ac

*3.0 0.0-* 2D>2.D>>.0 -.00.3E-.!>D

7-00 (microns# E.? ?.0 ?.! ?.* ?.E >.0 >.3 >.E -0.-0.* --.0 --.D -!.3 -3.! -2.! -*.D -E.2 !0.!2.D 32.>

1)) !%!n.in5 on G Flo&at! -00

)lowrate ('# -00 >* >0 ?* ?0 E* E0 D* D0 ** *0 2* 20 3* 30 !* !0 -* -0 *

E.*D0 -.->0 0.*!*D ,) 6ic&on$

! t a & E o l F G

-0

*.0

-0.0

-*.0

!0.0

!*.0

30.0

1)) ?6ic&on$@

heet " 7ate " +evision " ignature " +eference "

of 0!&Nov&-*

3*.0

20.0

6/6= /7 )O+ 59=7FL= ( O7

NC 1 ! 3 2 D ? -0 -! -2 -D -? !0 !2 30 3! 32 3D 3? 20 2! 22 2D 2? *! *D D0 D2 D? E! ED ?0

D0.3 ??.> --2.3 -D?.3 !->.!E3 3!3.> 3**.D 20D.2 2*E.! *0? D0>.D ED! ?-3 ?D2 >-2 >D* -0-D -0DE ---E --D? -!-> -3!-2!! -*!2 -D!D -E!E -?!> ->30 303! /NL=T 6ipe i,e (NC#

-0 2

32!.> 3>3.E 222.* 2>*.3 *>D.> E2D.! E>E.-D ?2?.-D ?>?.-D >2>.-D

ch No -?

!0 >

30 +

!0D.2 !D0.3 3--.! 33>.? 3>0.D 22-.2 2?> *>0.D E3D.D E?E.D ?3?.D ???.D

!0* !*E.2 30E.33D.D 3?E.2 232.> 2?!.D *?-.E30.! E?-.2 ?3!.2 ??!.2

hell Thickness (mm#

11$.20

D0 ,

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3PHASE Gas Separator - V2105_4.7x16_for_ Original

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