3PHASE Gas Separator - V2105_4.7x16_for_ Original

7/24/2019 3PHASE Gas Separator - V2105_4.7x16_for_ Original

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

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 J L' I$$u!. /o& Cli!nt0$ A%%&oal

RE' ATE PRP B3 CH B3 APP B3 APP B3 ESCRIPTION


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

PROJ4 EN#SI#N

PO APPRO'AL


3/44

!$i5n Ba$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 reuired volume but shall be confirmed by hydraulic calculations.

!. The following should be the minimum performance reuirements"

a#

b# $aximum %as carry&under in the liuid" !' (vol#.

c# $aximum pressure drop between inlet )lange and gas outlet flange" *0mbar

d# $inimum Liuid +esidence Time within the settling ,one" * minutes (both oil and water#

e# The water separated shall contain no droplets greator than -00 microns.

f# hen the /nlet water cut is less than *'(vol.# then the separator shall be operated as two&phase separator.

3. The separator design pressure shall be " ) 1 -!-

2. The separator shall be provided with two manholes providing human access for vessel entry for sludge removal .

*. ampling points shall be provided on the feed inlet4 gas and liuid outlet lines as close as possible to enable performance

to be measured.amples from each stream are analysed for oil in water concentrations4 water in oil concentrations4

liuid in gas carry over and compositions of each stream.

$aximum Liuid 5arry&Over in the vapour " 0.0-32 m31$$m3


4/44


5/44

DOC O. !"#/0/31$/1$/1D/%/0

Calculation sheet

5lient 6etroleum 7evelopment Oman 5alc No

6ro8ect 9arweel 5luster 6hase ! )acilities $ade by :

Location Oman 5hecked by ;> barg

7esign Temperature ?!@5 Operating Temperature !0&*0@5

P!&/o&6anc! C&it!&ia

The following should be the minimum performance reuirements"

a# $aximum Liuid 5arry&Over in the vapour " 0.0-32 m31$$m3b# $aximum %as carry&under in the liuid" !' (vol#.

c# $aximum pressure drop between inlet )lange and gas outlet flange" *0mbar

d# $inimum Liuid +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 for control volume is considered between L:L to L:9.

Slu5 'olu6!

: slug volume of 30 mA is reuired 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$ (reference point is from the inlet tan line)

N- -3-* mm

N! ?330 mm

N2 ?*D0 mm

N3 ?0D0 mm

$eshpad E-E0 mm

eir 6late ?*D0 mm

)low 7ist -3-* mm

essel 7ia !.E? m

Tan Length >.*D m

6!5 9ighater !00>4ummer

6!5 9ighater !00>4ummer

6!5 9ighater !00>4inter


6/44

DOC O. !"#/0/31$/19/1D/%/0

7ate ->&)eb&0D

7ate

.


7/44

DOC O. !"#/0/31$/20/1D/%/0

/N6FT /N)O+$:T/ON )O+ =6:+:TO+ 6+O%+:$

6+O.! ->.- !0.! !0.!

T=$6=+:TF+= @5 ?* !0 !0 ?* ?*

@) 0 0 0 0 0

+ 0 0 0 0 0

; 0 0 0 0 0

Fsed unit @5 ?* !0 !0 ?* ?*

6+=F+= barg 0.0 0.0 0.0 0.0 0.0

bara E!.2 >>.? E!.2 -3E.2 -3E.2

kg1cmI&g 0 0 0 0 0

kg1cmI&a 0 0 0 0 0

kpa&g 0 0 0 0 0

kpa&a 0 0 0 0 0

psig 0 0 0 0 0

psia 0 0 0 0 0

Fsed unit bara E!.2 >>.E* E!.2 -3E.2 -3E.2

%: 7=N/TH kg1mA *3.0 -0-.- D?.* -0*.> -0*.>lb1ftA 0 0 0 0 0

.% 0 0 0 0 0

Fsed unit kg1mA *3.00 -0-.-0 D?.*0 -0*.>0 -0*.>0

O/L 7=N/TH kg1mA D>>.0 DDD.0 D?D.0 DDD.0 DDD.0

lb1ftA 0 0 0 0 0

Fsed unit kg1mA D>> DDD D?D DDD DDD

:T=+ 7=N/TH kg1mA -000.0 -02E.0 -02*.0 -00E.0 -00E.0

lb1ftA 0 0 0 0 0

Fsed unit kg1mA -000 -02E -02* -00E -00E

%: /5O/TH c6 0.0-*3 0.0-*3 0.0-3E 0.0-E> 0.0-E>

c 0 0 0 0 0

6a.s 0 0 0 0 0

Fsed unit c6 0.0-*3 0.0-*3 0.0-3E 0.0-E> 0.0-E>

L/JF/7 /5O/TH Fnit c6 (c64c46a.s#

ater 0.*E- -.DD- -.E?! 0.D>- 0.D>-

Oil 0.3*2 0.3*D 0.202 0.!>D 0.!>D

-0m3 oil slug oncase2


8/44

DOC O. !"#/0/31$/21/1D/%/0

5:= - ! 3 2 *

5:= T/TL= 7esign ell clean up Turndown )ree flow-0m3 oil slug oncase2

%: )LO $$5)7 0 0 0 0 0

$$5$7 0 0 0 0 0

$$N5$7 0 0 0 0 0

scf1bbl 0 0 0 0 0

scm1bbl 0 0 0 0 0kg1hr !2?E?E 332D0- 2EE** 3!0000 3!0000

lb1hr 0 0 0 0 0

mA1hr 0 0 0 0 0

ftA1hr 0 0 0 0 0

Fsed unit kg1hr !2?E?E 332D0- 2EE** 3!0000 3!0000

7=/%N )LO !2?E?E.0 332D0-.0 2EE**.0 3!0000.0 3!0000.0

O/L )LO bbl1d 0 0 0 0 0

kg1hr 3>!-? DE-?3 !!DE DE-?3 E3?23

lb1hr 0 0 0 0 0

mA1hr 0 0 0 0 0

ftA1hr 0 0 0 0 0

Fsed unit kg1hr 3>!-? DE-?3 !!DE DE-?3 E3?23

7=/%N )LO 3>!-?.0 DE-?3.0 !!DE.0 DE-?3.0 E3?23.0

:T=+ )LO bbl1d 0 0 0 0 0

kg1hr 2??>! 2E0>E *>> 2??>! 2??>!

lb1hr 0 0 0 0 0

mA1hr 0 0 0 0 0

ftA1hr 0 0 0 0 0

Fsed unit kg1hr 2??>! 2E0>E *>> 2??>! 2??>!

7=/%N )LO 2??>!.0 2E0>E.0 *>>.0 2??>!.0 2??>!.0

%: 5O$6+=/C/L/TH ):5TO+ 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

%: 7=N/TH (=T# kg1mA *3.--* -00.-0- D?.*3E -0D.0-E 0.000


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DOC O. !"#/0/31$/22/1D/%/0

D

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

-0m3 water slugon case 2


10/44

DOC O. !"#/0/31$/23/1D/%/0

D

-0m3 water slugon case 2

0

0

0

0

03!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


11/44

DOC O. !"#/0/31$/2%/1D/%/0

3 69:= 9O+/KONT:L =6:+:TO+

heet "

6ro8ect No. " heatstone 7ate " -2&)eb&0D

5lient 0 +ev " 0

5ONT+:5T " 0 Cy " :

==L +=) " $ultiuse separator

5:= NO " -

5:= T/TL= " 7esign

COOT )/TT=7 " N

5=NT+:L /N " N

P&oc!$$ F!!. St&!a6 Su66a&

Operating 6ressure E!.20 bara Total mass flow 33D?>E kg1hr Total flow rate -.333 mA1s

Operating Temperature ?*.00 @5 $ean density E0.!00 kg1mA Total liuid flow 0.0!> mA1s

/nlet ater in Oil 2D.*D' CB v1v %: :T=+ O/L

%as )raction 0.E3? w1w !2?E?E.00 kg1hr 2??>!.00 kg1hr 3>!-?.00 kg1hr )low

0.>E? v1v *3.00 kg1mA -000.00 kg1mA D>>.00 kg1mA 7ensity

Liuid 7ensity ?3>.! kg1mA 0.0-* c6 0.*E- c6 0.3*2 c6 iscosity

'!$$!l .ata No99l! Si9in5 Sc!.ul!

essel /7 !.E?0 m

Tan 1 Tan Length >.*D0 m N.C /.7 elocity rho&vI 6ressure drop

9=$/ O+ !"- =LL/6 9=:7 " 9 (91=# in m m1s kg1msI mbar

7esign Temperature -00 deg5 )LF/7 /N -? 0.2-> >.DD D*** 3!.?

7esign 6ressure -*! barg Pipe Sch. 60 Check mom

hell Thickness --?.!0 mm %: OFT !0 0.2*D ?.00 33>0 -0.!

5orrosion :llowance 3 mm Pipe Sch. 80

hell eight E?!D! kg O/L OFT ? 0.->> 0.*0 -EE 0.*

9ead eight !!>2E kg Pipe Sch. 60

No,,le eight -*D*! kg :T=+ OFT D 0.-*2 0.E3 *30 -.D

Total '!$$!l W!i5t 11,8,1 5 Pipe Sch. 40

ater )illed eight D>!?! kg FLAN#E TO FLAN#E PRESSURE ROP ()4;

T:N TO =/+ " ?.*D0 m 5alculate +esidence time based on Tan LengthG (H1N# 3

=))=5T/= =6 L=N%T9 O/L " E.*D0 m Length used for oil phase residence time calculation 8.56m

=))=5T/= =6 L=N%T9 :T=+ " E.0D0 m Length used for water phase residence time calculation 8.56m

9=/%9T O) =/+ " -.0?0 m

TOT:L ==L OLF$= " D>.!? mA


12/44

DOC O. !"#/0/31$/25/1D/%/0

Li


13/44

DOC O. !"#/0/31$/2)/1D/%/0

of

=rosion vel

m1s

-2.*D

-D.ED

2.D-

3.?D

6"a&


14/44

DOC O. !"#/0/31$/2*/1D/%/0

NLL

B'

C

99LL

99LL

m


15/44

DOC O. !"#/0/31$/2$/1D/%/0

3 69:= 9O+/KONT:L =6:+:TO+

heet "


5lient 0 +ev " 0

5ONT+:5T " 0 Cy " :


5:= NO " !

5:= T/TL= " ell clean up

COOT )/TT=7 " N

5=NT+:L /N " N

P&oc!$$ F!!. St&!a6 Su66a&

Operating 6ressure >>.E* bara Total mass flow 22???- kg1hr Total flow rate 0.>D0 mA1s

Operating Temperature !0.00 @5 $ean density -!>.>0* kg1mA Total liuid flow 0.02- mA1s

/nlet ater in Oil 30.?2' CB v1v %: :T=+ O/L

%as )raction 0.E2* w1w 332D0-.00 kg1hr 2E0>E.00 kg1hr DE-?3.00 kg1hr )low

0.>*? v1v -0-.-0 kg1mA -02E.00 kg1mA DDD.00 kg1mA 7ensity

Liuid 7ensity E?3.* kg1mA 0.0-* c6 -.DD- c6 0.3*D c6 iscosity


essel /7 !.E?0 m



7esign Temperature ?! deg5 )LF/7 /N -? 0.2-> D.>D D!?> 3-.2

7esign 6ressure -!0 barg Pipe Sch. 100 Check mom

hell Thickness --?.!0 mm %: OFT !0 0.2*D *.D2 3!-* >.D


hell eight E?!D! kg O/L OFT ? 0.->> 0.>- *2D -.D


No,,le eight -*D*! kg :T=+ OFT D 0.-*2 0.DE 2E0 -.2


ater )illed eight D>!?! kg FLAN#E TO FLAN#E PRESSURE ROP +;41




9=/%9T O) =/+ " -.0?0 m



16/44

DOC O. !"#/0/31$/29/1D/%/0

Li


17/44

DOC O. !"#/0/31$/30/1D/%/0

of

=rosion vel

m1s

-0.E0

-!.-3

2.E3

3.EE

6"a&


18/44

DOC O. !"#/0/31$/31/1D/%/0

NLL

B'

C

99LL

99LL

m


19/44

DOC O. !"#/0/31$/32/1D/%/0

3 69:= 9O+/KONT:L =6:+:TO+

heet "


5lient 0 +ev " 0

5ONT+:5T " 0 Cy " :


5:= NO " 3

5:= T/TL= " Turndown

COOT )/TT=7 " N

5=NT+:L /N " N

P&oc!$$ F!!. St&!a6 Su66a&

Operating 6ressure E!.20 bara Total mass flow *0D!- kg1hr Total flow rate 0.->* mA1s

Operating Temperature !0.00 @5 $ean density E!.!0> kg1mA Total liuid flow 0.00- mA1s

/nlet ater in Oil -2.E?' CB v1v %: :T=+ O/L

%as )raction 0.>23 w1w 2EE**.00 kg1hr *>>.00 kg1hr !!DE.00 kg1hr )low

0.>>2 v1v D?.*0 kg1mA -02*.00 kg1mA D?D.00 kg1mA 7ensity

Liuid 7ensity E3>.- kg1mA 0.0-2 c6 -.E?! c6 0.202 c6 iscosity


essel /7 !.E?0 m



7esign Temperature -00 deg5 )LF/7 /N -? 0.2-> -.2- -22 0.E

7esign 6ressure -*! barg Pipe Sch. 100

hell Thickness --?.!0 mm %: OFT !0 0.2*D -.-> >E 0.3


hell eight E?!D! kg O/L OFT ? 0.->> 0.03 - 0.0


No,,le eight -*D*! kg :T=+ OFT D 0.-*2 0.0- 0 0.0


ater )illed eight D>!?! kg FLAN#E TO FLAN#E PRESSURE ROP ;4)




9=/%9T O) =/+ " -.0?0 m



20/44

DOC O. !"#/0/31$/33/1D/%/0

Li


21/44

DOC O. !"#/0/31$/3%/1D/%/0

of

=rosion vel

m1s

-2.3D

-2.E2

2.DD

3.EE

6"a&


22/44

DOC O. !"#/0/31$/35/1D/%/0

NLL

B'

C

99LL

99LL

m


23/44

DOC O. !"#/0/31$/3)/1D/%/0

3 69:= 9O+/KONT:L =6:+:TO+

heet "


5lient 0 +ev " 0

5ONT+:5T " 0 Cy " :


5:= NO " 2

5:= T/TL= " )ree flow

COOT )/TT=7 " N

5=NT+:L /N " N

P&oc!$$ F!!. St&!a6 Su66a&

Operating 6ressure -3E.20 bara Total mass flow 23D0E* kg1hr Total flow rate 0.??- mA1s

Operating Temperature ?*.00 @5 $ean density -3E.*-3 kg1mA Total liuid flow 0.02! mA1s

/nlet ater in Oil 3!.2>' CB v1v %: :T=+ O/L

%as )raction 0.E32 w1w 3!0000.00 kg1hr 2??>!.00 kg1hr DE-?3.00 kg1hr )low

0.>*3 v1v -0*.>0 kg1mA -00E.00 kg1mA DDD.00 kg1mA 7ensity

Liuid 7ensity EED.? kg1mA 0.0-? c6 0.D>- c6 0.!>D c6 iscosity


essel /7 !.E?0 m



7esign Temperature -00 deg5 )LF/7 /N -? 0.2-> D.3> *D0E !?.0


hell Thickness --?.!0 mm %: OFT !0 0.2*D *.-* !?0E ?.2




No,,le eight -*D*! kg :T=+ OFT D 0.-*2 0.E! *!E -.D


ater )illed eight D>!?! kg FLAN#E TO FLAN#E PRESSURE ROP ++4+


=))=5T/= =6 L=N%T9 O/L " E.*D0 m Length used for oil phase residence time calculation 8.56 m

=))=5T/= =6 L=N%T9 :T=+ " E.0D0 m Length used for water phase residence time calculation 8.56 m

9=/%9T O) =/+ " -.0?0 m



24/44

DOC O. !"#/0/31$/3*/1D/%/0

Li


25/44

DOC O. !"#/0/31$/3$/1D/%/0

of

=rosion vel

m1s

-0.20

--.?D

2.E3

3.?2

6"a&


26/44

DOC O. !"#/0/31$/39/1D/%/0

NLL

B'

C

99LL

99LL

m


27/44

DOC O. !"#/0/31$/%0/1D/%/0

3 69:= 9O+/KONT:L =6:+:TO+

heet "


5lient 0 +ev " 0

5ONT+:5T " 0 Cy " :


5:= NO " *

5:= T/TL= " -0m3 oil slug on case2

COOT )/TT=7 " N

5=NT+:L /N " N

P&oc!$$ F!!. St&!a6 Su66a&

Operating 6ressure -3E.20 bara Total mass flow 22!E3* kg1hr Total flow rate 0.??2 mA1s

Operating Temperature ?*.00 @5 $ean density -3>.-E* kg1mA Total liuid flow 0.022 mA1s

/nlet ater in Oil 30.2*' CB v1v %: :T=+ O/L

%as )raction 0.E!3 w1w 3!0000.00 kg1hr 2??>!.00 kg1hr E3?23.00 kg1hr )low


Liuid 7ensity ED>.? kg1mA 0.0-? c6 0.D>- c6 0.!>D c6 iscosity


essel /7 !.E?0 m



7esign Temperature -00 deg5 )LF/7 /N -? 0.2-> D.2- *E-0 !?.D




hell eight E?!D! kg O/L OFT ? 0.->> -.00 DD0 !.0


No,,le eight -*D*! kg :T=+ OFT D 0.-*2 0.E! *!E -.D


ater )illed eight D>!?! kg FLAN#E TO FLAN#E PRESSURE ROP +(4)




9=/%9T O) =/+ " -.0?0 m



28/44

DOC O. !"#/0/31$/%1/1D/%/0

Li


29/44

DOC O. !"#/0/31$/%2/1D/%/0

of

=rosion vel

m1s

-0.32

--.?D

2.E3

3.?2

6"a&


30/44

DOC O. !"#/0/31$/%3/1D/%/0

NLL

B'

C

99LL

99LL

m


31/44

DOC O. !"#/0/31$/%%/1D/%/0

3 69:= 9O+/KONT:L =6:+:TO+

heet "


5lient 0 +ev " 0

5ONT+:5T " 0 Cy " :


5:= NO " D

5:= T/TL= " -0m3 water slug on case 2

COOT )/TT=7 " N

5=NT+:L /N " N

P&oc!$$ F!!. St&!a6 Su66a&

Operating 6ressure -3E.20 bara Total mass flow 22D-2* kg1hr Total flow rate 0.??2 mA1s

Operating Temperature ?*.00 @5 $ean density -20.!2E kg1mA Total liuid flow 0.022 mA1s

/nlet ater in Oil 3D.E3' CB v1v %: :T=+ O/L

%as )raction 0.E-E w1w 3!0000.00 kg1hr *?>D!.00 kg1hr DE-?3.00 kg1hr )low


Liuid 7ensity E>-.! kg1mA 0.0-? c6 0.D>- c6 0.!>D c6 iscosity


essel /7 !.E?0 m



7esign Temperature ?! deg5 )LF/7 /N -? 0.2-> D.2- *E*2 !?.?

7esign 6ressure -!0 barg Pipe Sch. 100





No,,le eight -*D*! kg :T=+ OFT D 0.-*2 0.?E EDD !.3


ater )illed eight D>!?! kg FLAN#E TO FLAN#E PRESSURE ROP +(42




9=/%9T O) =/+ " -.0?0 m



32/44

DOC O. !"#/0/31$/%5/1D/%/0

Li


33/44

DOC O. !"#/0/31$/%)/1D/%/0

of

=rosion vel

m1s

-0.30

--.?D

2.E3

3.?2

6"a&


34/44

DOC O. !"#/0/31$/%*/1D/%/0

NLL

B'

C

99LL

99LL

m


35/44

+late +ac, 293311022.xls

+a-e %$

Cross-low Plate Pack i"ing #$ori"ontal%5ontract +ef "

7ocument +ef "

essel "

SI UNITS5:= " - ! 3 2 * D

Inl!t con.ition$

7esign $argin 14( 14( 14( 14( 1 1

Oil flow (kg1hr# >;2184) ,=18>4) 22,=4) ,=18>4) =>8+>4) ,=18>4)

Oil density (kg1mA# ,;;4) ,,,4) ,8,4) ,,,4) ,,,4) ,,,4)

Oil iscosity (c6# )4>( )4>, )4+) )4>) )4>) )4>)

ater flow (kg1hr# +88;24) +=);=4) (;;4) +88;24) +88;24) (8;,24)

ater density (kg1mA# 1)))4) 1)+=4) 1)+(4) 1))=4) 1))=4) 1))=4)

ater iscosity (c6# )4(= 14,, 14=8 )4,; )4,; )4,;

ater Loading '(w1w# **.2>0 2-.!- !0.>0 2!.-! 3>.?2 2D.E2

$ean inlet density (kg1mA# ?3>.-D E?3.*0 E3>.0E EED.?0 ED>.?* E>-.!2

Total inlet flow (mA1hr# -0*.00 -2*.?D 3.?? -2>.23 -*>.23 -*>.23

Oil )low (mA1hr# *D.-- -00.?? 3.30 -00.?? --0.?? -00.??ater )low (mA1hr# 2?.?> 22.>? 0.*E 2?.** 2?.** *?.**

Plate &eo'etr(

Plat! An5l! ?.!5&!!$@ +( 2* 2* 2* 2* 2* 0.E?*

1) -0 -0 -0 -0 -0

1 - - - - -

14))) -.000 -.000 -.000 -.000 -.000

)in *e+uire'ents for i"ing of ront rea of Plate Pack

)4;)) 0.>0 0.>0 0.>0 0.>0 0.>0

)48)) 0.?0 0.?0 0.?0 0.?0 0.?0

S!l!ct!. R!nol.$ No 8() ?*0 ?*0 ?*0 ?*0 ?*0

0.0!0 0.0!0 0.0!0 0.0!0 0.0!0 0.0!0

-.0?D -.?*0 0.0** !.!!* -.D3- -.2?3

0.?3> 0.!E? 0.003 0.D>2 0.2D! 0.**?

24+82 24,++ )4)=2 >4,=> 24,2; 24(8)

-.3!E !.!D- 0.0DE !.E!0 -.>>3 -.?-3

-.-*2 0.3?! 0.00* 0.>*2 0.D3D 0.EDE

6late 6ack height (m# -.!00

eter'ination of eparation Perfor'ance 1))

1))

:xial elocity of Oil (light# section (m1s# 0.0-- 0.000 0.000 0.000 0.000 0.000

:xial elocity of ater (heavy# section (m1s# 0.-3- 0.000 0.000 0.000 0.000 0.000

Axial velocity shoul not excee 0.015

ater phase settling velocity (in light section# (m1s# 0.000 0.000 0.000 0.000 0.000 0.000Oil phase settling velocity (in heavy section# (m1s# 0.00!0 0.0000 0.0000 0.0000 0.0000 0.0000

-> 0 0 0 0 0

?2 0 0 0 0 0

essel etails

9ydrualic 7iameter for Liuid1Liuid eparation (m# -.EE? -.?3* 0.30! !.-D3 -.?!> -.?-!

$in. /nlet 5ompartment (m# -.3>0 0.>-E 0.-*- -.0?- 0.>-* 0.>0D

$in. ettling 5ompartment (m# -.D*0 -.D*0 -.D*0 -.D*0 -.D*0 -.D*0

$in. Outlet 5ompartment (m# 0.D>* 0.2*> 0.0ED 0.*2- 0.2*E 0.2*3

7ini6u6 Tan L!n5t ?6@ (4+)= (4+)= (4+)= (4+)= (4+)= (4+)=

'!$$!l ia6!t!& ?6@ 24=8) 6.0!

NIL ?6@ )42))

0.1" 0.00 0.00 0.00 0.00 0.00 0.16 0.00 0.00 0.00 0.00 0.00

NLL ?6@ 142))

#.$1 0.00 0.00 0.00 0.00 0.00

#.08 0.00 0.00 0.00 0.00 0.00

9==T O)

7:T= !&Nov&-*

+=//ON

/%N

6+O


36/44

CONTOURE 'ANE PAC SIIN#

0!&Nov&-*

essel ref " $ultiuse separator

5ontract rev " 0

essel i.d !.E?0 m 5ase - 5ase ! 5ase 3 5ase 2 5ase * 5ase D

Liuid level Q 99LL -.*>0 m $ax rho&vI ?> ?> ?> ?> ?> ?>

Top vane overlap 0.0!* m +e area (mI# -.00D! 0.>E>? 0.-D>> 0.>-*D 0.>-*D 0.>-*D

hell clearance 0.0*0 m :ctual area (mI# -.00D! -.00D! -.00D! -.00D! -.00D! -.00D!

:d8ust box width 0.0?0 m ane R;R factor 0.3E-! 0.3?D* 0.0D2- 0.3D!E 0.3D!E 0.3D!E

ane area -.00D! mI

ane pitch 0.0-? m

=ffective diameter !.D30 m

ector hgt at d1! 0.00- m

ector area 0.000 mI

Number of :ctual :ctual :ctual :ctual

5ontoured 9t. 5hord ector area Non&cont height anes 9 ector area h

0.-30 -.-20 0.0>>? 0.?D* D0 -.-!E 0.-!E 0.0>D! 0.?E>

-3.000

Fnderside of Fnderside of

vanebox to top vanebox to high

of vessel (m# 99LL (m#

-.!3- &0.02-

$=96:7 /K/N%

D!E JF:+= /K/N% 5ase - 5ase ! 5ase 3 5ase 2 5ase * 5ase D

:ngle D0 deg ; )actor 0.0?* 0.0?* 0.0?* 0.0?* 0.0?* 0.0?*

idth -.003 m +e area (mI# 2.3>2 2.*ED 0.E*> 2.!>2 2.!>2 2.!>3>

Length -.003 m :ctual area (mI# 2.*ED 2.*ED 2.*ED 2.*ED 2.*ED 2.*E*D9eight 0.!!0 m $espad dia (m# !.2- !.2- !.2- !.2- !.2- !.2-

Top of essel 0.2E2 m

Fnderside of Fnderside of

vanebox to top vanebox to high

of vessel (m# 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 " of

7ate " 0!&Nov&-*

+evision " P+=)M

ignature " Phyp

6ro8ect No." P+=)M


37/44

+evision date " -?1031>2 heet " of

+evision level " 0 7ate " 0!&Nov&-*

+evision "

ignature "

+eference "

59O=6=NTO=T=+

(:N= TH6=# /NL=T 7=/5= 5:L5FL:T/ON

7ocument reference " 0

6ro8ect reference " heatstone

5ustomer " 0

essel reference " $ultiuse separator

In%ut .ata Out%ut &!$ult$

essel internal diameter !E?0 mm Inl!t .!ic! t%! 1A

No,,le internal diameter 2-> mm 'an! an5l! - al%a =

essel orientation 9 (19# 'an! &a.iu$ ?R@ 1)) 66

ane angle & alpha = 'an! L!n5t ?L@ 1)) 66

$aterial of construction >1, (-D-430243-D# E.5! an5l! - "!ta 1)4)>

(?!*422D!# Nu6"!& o/ an!$ %!& $i.! 12

ane thickness > mm Wo 2,4=+ 66/nlet 1 Length ratio >4( A%%&oDi6at! !i5t 1+1 5

$anway internal diameter ,)) mm S%lit an! la..!&$ No

acuum operation N (H1N# %!& $i.!

=xit manway or no,,le 7 ($1N# 66

A%%&oDi6at! l!n5t 1>1( 66

A%%&oDi6at! 6aDi6u6 i.t =>+ 66

Int!&6!.iat! calculation$ Ta"l! to .!t!&6in! E

3.0ED 7 =

Nv -!.>D> 0 !0>*.*

+ounded Nv -! !000 !0>*.*=dge angle & beta -0.03 @ 2000 !0>*.*

vo !D.E2 mm

$aximum vane height *D2.>? m m Ta"l! to .!t!&6in! L an. R

pace available -2DE mm

+euired vane height 23> mm Lv +v

$aximum ladder height 23> mm 0 -00 *0

3 -00 -00

eight of vane ladder *> kg each D -*0 -00

eight of top 1 btm plates !! kg !0 !00 -00

Total overall weight -2- kg

Ta"l! to .!t!&6in! A an. B

+v : C

*0 -D* -!0

-00 !-* -E0300 E-* 23*

Not!$ :

-. The value of is not a physical dimension on the vane type inlet device.

/t is purely a ratio used to determine the reuired 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.


38/44


39/44

C$ +ef " heatstone

5lient16ro8ect +ef " 0

essel " $ultiuse separator

5ase -

%as density (kg1mA# *3.0

%as iscosity (c6# 0.0-*

%as /nlet flow (mA1hr# 2D>2.-

Culk Liuid density (kg1mA# D>>.0

:ctual vane area (mI# -.0-

ane 6ack ; )actor (m1s# 0.3E-ane elocity (m1s# -.!>D

ane elocity 7-00 )lowrate

(m1s# (microns# ('#

-.!>D E.? -00

-.!3- ?.0 >*

-.-DD ?.! >0

-.-0- ?.* ?*

-.03E ?.E ?0

0.>E! >.0 E*

0.>0E >.3 E00.?2! >.E D*

0.EE? -0.- D0

0.E-3 -0.* **

0.D2? --.0 *0

0.*?3 --.D 2*

0.*-? -!.3 20

0.2*2 -3.! 3*

0.3?> -2.! 30

0.3!2 -*.D !*

0.!*> -E.2 !0

0.->2 !0.- -*

0.-30 !2.D -0

0.0D* 32.> *

heet " of

=ffective eparator Length (m# E.*D0 7ate " 0!&Nov&-*

%as pace 9eight (m# -.->0 +evision "

%as pace :xial velocity (m1s# 0.*!*D ignature "

7aD4 &o%l!t to a%%&oac an! %ac ,) 6ic&on$ +eference "

*.0 -0.0 -*.0 !0.0 !*.0 30.0 3*.0 20.0

-

-0

-00

1)) !%!n.in5 on G Flo&at!

1)) ?6ic&on$@

GFloE&at!


40/44

6/6= /7 )O+ 59=7FL= (

O7 NC -0 !0 30 20 D0 ?0

1 2 > + ( , =

D0.3 ! *!.* 2>.!

??.> 3 EE.> E3.E

--2.3 2 -0!.3 >E.!

-D?.3 D -*2.- -2D.2

!->.- ? !0D.2 !0* !0!.E ->?.* ->3.E

!E3 -0 !D0.3 !*E.2 !*2.* !2E.D !2!.?

3!3.> -! 3--.! 30E.- 303.3 !>*.2 !?>

3**.D -2 32!.> 33>.? 33D.D 333.3 3!*.2 3-E.*

20D.2 -D 3>3.E 3>0.D 3?E.2 3?- 3E3.- 3D3.*

2*E.! -? 222.* 22-.2 232.> 2!?.E 2->.- 20>.D

*0? !0 2>*.3 2?> 2?!.D 2EE.? 2DD.? 2**.D

D0>.D !2 *>D.> *>0.D *?-.- *E2.D *D0.2 *2E.EED! 30 E2D.! E3D.D E30.!

?-3 3! E>E.-D E?E.D E?-.2 EE?.02

?D2 32 ?2?.-D ?3?.D ?3!.2 ?!>.02

>-2 3D ?>?.-D ???.D ??!.2 ?E>.02

>D* 3? >2>.-D

-0-D 20

-0DE 2!

---E 22

--D? 2D

-!-> 2?

-3!- *!

-2!! *D-*!2 D0

-D!D D2

-E!E D?

-?!> E!

->30 ED

303! ?0

/NL=T O/L OFTL=T

6ipe i,e ch No 6ipe 7ia 6ipe i,e ch No

(NC# (mm# (NC#

-? D0 2->.- ? D0

D D

5:+CON T==L 7=/%N T+= (N1mm!#

deg 5 ) (bar1-0#

!* !03

*0 !03

-00 ->- elected ->-

-*0 -E*

!00 -*>

hell Thickness (mm# 11$.20


41/44

m#

-00 -!0 -20 -D0 N

8 ; 1) 11 12

2!.? *0.?

DD.D ED.!

>! ?E.3 -0-.D

-3>.? -3-.? -*!.2

-??.> -?!.D -EE.> -E3.- !03.!

!3D.* !30.- !!!.! !-*.? !*2

!?- !E3.- !DD.E !*E.! 302.?

30? 300 !>!.- !?2.! 3**.D

3*2 322.* 333.2 3!*.2 20D.2

3>?.* 3?E.2 3EE.? 3DD.E 2*E.!

22!.> 23-.? 2->.- 20? *0?

*3-.? *-E.D *02.? 2>0.* D0>.DED!

?-!.?

?D3.D

>-2.2

>33.!2 >!D.> >!0.*2 >-2.! >D*.!

>?2.!2 >EE.> >E-.*2 >D*.! -0-D

-03*.!2 -0!?.> -0!!.*2 -0-D.! -0DD.?

-0?*.!2 -0E?.> -0E!.*2 -0DD.! ---E.D

--3D.!2 --!>.> --!3.*2 ---E.! --D?.2

--?E.!2 --?0.> --E2.*2 --D?.! -!->.!

-!?>.!2 -!?!.> -!ED.*2 -!E0.! -3!0.?

-3>0.!2 -3?3.> -3EE.*2 -3E-.! -2!!.2-2>!.!2 -2?*.> -2E>.*2 -2E3.! -*!2

-*>2.!2 -*?E.> -*?-.*2 -*E*.! -D!*.D

-D>*.!2 -D??.> -D?!.*2 -DED.! -E!E.!

-E>E.!2 -E>0.> -E?2.*2 -EE?.! -?!?.?

-?>?.!2 -?>-.> -??*.*2 -?E>.! ->30.2

3000.!2 !>>3.> !>?E.*2 !>?-.! !03!

:T=+ OFTL=T %: OFTL=T

6ipe 7ia 6ipe i,e ch No 6ipe 7ia 6ipe i,e ch No

(mm# (NC# (mm# (NC#

->?.* D 20 -*2.- !0 ?0

* E


42/44

6ipe 7ia

(mm#

2**.D


43/44

S!!t 1) o/ 11

Calculation No: >*-D (check# RE' B3 CH APP ATE

Cli!nt: 67O 6- 69yp $; 31!D1!002

P&o!ct: 9arweel 6hase ! 6! 69yp *1!D1!002

Location: Oman !

Cont&act No: L3??* 3

HORIONTAL > PHASE SEPARATOR SIIN# 1*2

Si9in5

7esign

Ta5 No: !-0- !$c&i%tion: -st tage eparator

#a$ Flo E.0?02 $$td mA 1 day (-*54 -atm# !*0.*D $$5)7 (D0)4 -atm#

Oil Flo -32E actual mA1day ?2D> C67 (actual#Wat!& Flo --E3 actual mA1day E3?0 C67 (actual#

Flui. P&o%!&ti!$ #a$ Oil Wat!&

7ensity (actual# (kg1mA# P*Pl*P *3.00 D>> -000

iscosity (c6# n1a 0.3* 0.*E

$olecular t ->.>? n1a n1a

)low (kg1hr# !.2>3=S0* 3.>!!=S02 2.??>=S02

)low (actual mA1min# E?.3> 0.>2 0.?- "

Alloa"l! 'a%ou& '!locit

g ;((6l&6v#16v#UV '5 0.!> m1s

%as eparation 5onstant 0.0?3 m1s (hell 7=6 3-.!!.0*.--#

egmental area reuired for gas flow *,)K'5 2.*0> mI

W!i& H!i5t ?inclu.in5 li ' of 7iameter

)raction of total 5: for gas flow F5 0.3?>! "9eight of liuid crest over weir 32 mm (hell 7=6 3-.!!.0*.-!#

'!$$!l Int!&nal ia6!t!& !.E?0 m

Total 5ross ectional :rea A D.0E0 mI

Normal :rea available or %as )low AKF5 !.3D! mI

=xcess area for %as 7isentrainment &2? '

essel length (/N5LF7/N% =/+ =5T/ON# L >.*D m

L17 ratio 3.22

eir 6osition -.000 m from Oil outlet end Tan Line

Total essel olume ' *?.03 mA

essel olume upstream of weir *-.>D mA /T=+:T= FNT/L O/L :N7

Liuid olume upstream of weir 3-.E2 mA :T=+ +=/7=N5= T/$=

=5==7 =TTL/N% T/$=.

H!i5t to Wat!& * Oil Int!&/ac! -*.!> ' of 7iameter ($:H N==7 TO :7.E ' of Overall 5: ==L /7 O+ =/+ 9=/%9T#

egmental :rea for Oil flow A$ *-.2 ' of Overall 5:

Li


44/44

S!!t 11 o/ 11

Calculation No: >*-D (check# RE' B3 CH APP ATE

Cli!nt: 67O 6- 69yp $; 031!D102

P&o!ct: 9arweel 6hase ! 6! 69yp 0*1!D102

Location: Oman ! -!1301>>Cont&act No: L3??* 3 -!1301>>

HORIONTAL > PHASE SEPARATOR SIIN# 2*2

L!!l Cont&ol H!i5t$

Ta5 No: !-0- !$c&i%tion: -st tage eparator

essel 7iameter !.E? m !E?0 mm

essel Length >.*D m

eir 6osition - m from Oil outlet end Tan Line

W!i& !i5t ?inclu.in5 li> 66 0.D-- of &sect area of &sect area

7esign Oil )low 0.>2 actual mA1min -32E actual mA1day7esign ater )low 0.?- actual mA1min --E3 actual mA1day

essel &ectional :rea D.0E0 mI

7epth of %as pace at 99LL -->0 mm 0.20> of &sect area of &sect area

%as )low :rea at 99LL !.* mI

$inimum :rea +euired 2.*0> mI ee i,ing

=xcess area for %as 7isentrainment &2* '

Wat!& Si.! o/ W!i&

W!i& H!i5t ?inclu.in5 c&!$t@ -D33 mm 0.D-- of &sect area of &sect area

olume between top of weir and 99/L -3.0E mA E.2E $inutes of oil S water flow

$inutes of oil

HHIL -0?0 mm 0.3*> of &sect area

olume between 99/L B 9/L !.30 mA !.?! $inutes of water flow $inutes of wa

HIL >?0 mm 0.3-* of &sect area

olume between 9/L B N/L --.32 mA -3.>! $inutes of water flow $inutes of wa

NOR7AL INTERFACE LE'EL ?NIL@ 2!* mm 0.0>E of &sect area

olume between N/L B L/L 0.2! mA 0.*! $inutes of water flow $inutes of wa

LIL 200 mm 0.0?> of &sect area

olume between LL/L and L/L -.*? mA -.>2 $inutes of water flow

$inutes of wa

LLIL 300 mm 0.0*? of &sect area

olume to vessel empty 3.0! mA 3.E- $inutes of water flow

Oil Si.! o/ W!i&Oil ide of ei

HHLL -*>0 mm 0.*>- of &sect area

olume between 99LL and 9LL (sum of both !.D2 mA -.*- $inutes of oil and water flow $inutes of oil

water and oil sides# ERROR: HHLL B!lo W!i& H!i5t it C&!$t

HLL -2>0 mm 0.*2D of &sect area

Total Su&5! 'olu6! "!t!!n HLL an. -24(2 6M -14++ 7inut!$ o/ oil an. at!& /lo $inutes of oil

!i& !i5t inclu.in5 c&!$t ?at!& $i.!@

an. NLL ?oil $i.!@4 ERROR: HLL B!lo W!i& H!i5t it C&!$t

NOR7AL LIUI LE'EL ?NLL@ --?0 mm 0.202 of &sect area of &sect area

olume between NLL B LLL 0.!E mA 0.!> $inutes of oil flow

LLL -0?0 mm 0.3*> of &sect area

olume between LLL and LLLL -.03 mA -.-0 $inutes of oil flow

$inutes of oil f

LLLL D?0 mm 0.->0 of &sect area

olume to vessel empty -.-* mA -.!3 $inutes of oil flow

Date post:	22-Feb-2018
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3PHASE Gas Separator - V2105_4.7x16_for_ Original

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