PETROFAC JOB NO: JI - 182
HARWEEL CLUSTER PHASE 2 FACILITIES
Calculation S!!t Ra"a" #a$ S!%a&ato& '-2()1
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ATE
PRP B3
CH B3
APP B3
I$$u!. /o& Cli!nt0$ A%%&oal APP B3
ESCRIPTION
fle:///var/www/apps/conversion/tmp/scratch_5/293311022.xls
PROJ4 EN#
SI#N
PO APPRO'AL
fle:///var/www/apps/conversion/tmp/scratch_5/293311022.xls
!$i5n Ba$i$:
1.
!.
The separator shall be designed to contain hydrodynamic slugs expected from the trunklines between the Normal Operating Level and the high level alarm.This shall be taken as 30m3 reuired volume but shall be confirmed by hydraulic calculations. The following should be the minimum performance reuirements" reuirements" a# $aximum Liuid 5arry&Over in the vapour " 0.0-32 m 31$$m3 b# $aximum $aximum %as carry&u carry&unde nderr in the liuid liuid"" !' (vol#. (vol#. c# $aximum pressure pressure drop between inlet )lange )lange and gas outlet outlet flange" *0mbar d# $inimum Liuid +esidence +esidence Time within the settling ,one" ,one" * minutes minutes (both oil and water# water# e# The water water separated separated shall shall contain no droplets droplets greator greator than -00 microns. f# hen the /nlet water cut is less than *'(vol.# then the separator separator shall be operated as two&phase separator. separator.
3.
The separa separator tor desig design n pres pressur sure e shall shall be " ) 1 -!-!-
2.
The separat separator or shall shall be provided provided with with two two manholes manholes providin providing g human human access for for vessel entry entry for for sludge sludge removal removal .
*.
ampling ampling points points shall be provid provided ed on the the feed inlet4 inlet4 gas gas and liuid liuid outlet outlet lines lines as close as as possible possible to enable enable performa performance nce to be measured.amples from each stream are analysed for oil in water concentrations4 water in oil concentrations4 liuid in gas carry over and compositions of each stream.
DOC O. !"#/0/31$/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 reuirements" a# $aximum Liuid 5arry&Over in the vapour " 0.0-32 m31$$m3 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# 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 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$ 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
(c64c46a.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 Liuid 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!i5t 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 CB 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 liuid 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& !i5t 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 adeuatelyG
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 C1LLLL
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
without coalescing packs
: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
Operating 6ressure Operating Temperature /nlet ater in Oil %as )raction Liuid 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 '!$$!l W!i5t ater )illed eight
T:N TO =/+ " =))=5T/= =6 L=N%T9 O/L " =))=5T/= =6 L=N%T9 :T=+ " 9=/%9T O) =/+ " TOT:L ==L OLF$= "
>>.E* !0.00 30.?2' 0.E2* 0.>*? E?3.*
bara @5 CB v1v w1w v1v kg1mA
!.E?0 >.*D0 9 ?! -!0 --?.!0 3 E?!D! !!>2E -*D*! 11,8,1 D>!?!
m m (91=# deg5 barg mm mm kg kg kg 5 kg
P&oc!$$ F!!. St&!a6 Su66a& Total mass flow 22???- kg1hr $ean density -!>.>0* kg1mA %: 332D0-.00 kg1hr -0-.-0 kg1mA 0.0-* c6
Total flow rate Total liuid flow O/L DE-?3.00 kg1hr DDD.00 kg1mA 0.3*D c6
:T=+ 2E0>E.00 kg1hr -02E.00 kg1mA -.DD- c6
0.>D0 mA1s 0.02- mA1s )low 7ensity iscosity
No99l! Si9in5 Sc!.ul! N.C in )LF/7 /N
/.7 m -?
Pipe Sch. %: OFT
!0 Pipe Sch.
O/L OFT
? Pipe Sch.
:T=+ OFT
D Pipe Sch. FLAN#E TO FLAN#E PRESSURE ROP
?.*D0 E.*D0 E.0D0 -.0?0 D>.!?
m m m m mA
0.2-> 100 0.2*D 100 0.->> 100 0.-*2 40
5alculate +esidence time based on Tan LengthG (H1N# Length used for oil phase residence time calculation Length used for water phase residence time calculation
elocity m1s D.>D
rho&vI kg1msI D!?>
6ressure drop mbar 3-.2
*.D2
3!-*
>.D
0.>-
*2D
-.D
0.DE
2E0
-.2
Check mom
+;41
3 8.56 m 8.56 m
DOC O. !"#/0/31$/29/1D/%/0
Li
Level m
essel fill '
Oil Oil Oil Oil Oil Oil Oil
-.*>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.*
99LL(!# 99LL 9LL NLL NLL LLL LLLL W!i& !i5t ater 99/L ater 9/L ater NIL ater N/L ater L/L ater LL/L Fllage
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 adeuatelyG
0.02? 0.-!3 0.*D3?E?0?30.>2!
φwm = elected λ =
0.00D 0.0E0
!.?*
)or a meshpad B schoepentoeter (refer to 7=6 3-.!!.0*.--&%en ept !00!#
*.**D mI Less than actual gas space! Consult Prinicipal to see if it is acceptable
$ax. 7roplet to approach vane pack %as space axial velocity
0.03*
D0 microns 0.*!D m1s
m1s between N/L B microns between N/L B percent v1v microns
>D microns between N/L B essel bottom ppm v1v -00 microns
If a vane pack, use 0.1 to allow for slugs. If a bare vessel, use 0.07 +ecommended %as )low :rea
!.*? -0.*3 =4++ !.*3 -.E3.!0.00
)4)1((
0.0-E *0 0.* -00
Hes
λ= φ= f η f φ
olume between levels mA 0.00 3.!2 -0.0> 1(4=+ 3.!0 !.0E !.00 MM
+esidence time mins (/ncluding heads# 0.00 -.>3 D.00 ;4>, -.>0 -.!3 -.->
/nterval
99LL199LL(!# 9LL199LL NLL19LL NIL to LLL1NLL LLLL1LLL C1LLLL
3.22 -2.02 ;4;> 3.3E !.!? 2.!?
9/L199/L N/L19/L NIL to L/L1N/L LL/L1L/L L/LL to
2- microns to NLL
:/:L )LF/7 =LO5/TH :5TF:L :T=+ 7+O6L=T +=JF/+=7 :T=+ /N O/L T:+%=T :T=+ 7+O6L=T
#AS CAP ANAL3SIS :ctual %as pace :rea %as 5ap height
)4)1=)
3?.? 3*.3 1;41 ->.-2.2 -0.?
)+O$ TO;= L: %: CFCCL= =6:+:T=7 %: +=$:/N/N% :T/)/= =JF/L/C+/F$ 5ON7/T/ON
without coalescing packs
: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
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 " 3 5:= T/TL= " Turndown COOT )/TT=7 " N 5=NT+:L /N " N
Operating 6ressure Operating Temperature /nlet ater in Oil %as )raction Liuid 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!i5t 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 !0.00 -2.E?' 0.>23 0.>>2 E3>.-
bara @5 CB 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 *0D!- kg1hr $ean density E!.!0> kg1mA %: 2EE**.00 kg1hr D?.*0 kg1mA 0.0-2 c6
Total flow rate Total liuid 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
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-> 100 0.2*D 100 0.->> 100 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 -.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 '
Oil Oil Oil Oil Oil Oil Oil
-.*>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.*
99LL(!# 99LL 9LL NLL NLL LLL LLLL W!i& !i5t ater 99/L ater 9/L ater NIL ater N/L ater L/L ater LL/L Fllage
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 adeuatelyG
φwm = elected λ =
0.0*0 0.0-? 0.*D!!>23-2!
)or a meshpad B schoepentoeter (refer to 7=6 3-.!!.0*.--&%en ept !00!#
0.>>0.000.0E0
0.>!- mI
$ax. 7roplet to approach vane pack %as space axial velocity
0.000
D0 microns 0.*!D m1s
m1s between N/L B microns between N/L B percent v1v microns
-! 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)))2
0.00-0 -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.-3 28(4=+ *?.0! 3E.D! 3D.!3
/nterval
99LL199LL(!# 9LL199LL NLL19LL NIL to LLL1NLL LLLL1LLL C1LLLL
!E0.-D --0-.>* ==;4)+ !D2.20 -E>.0* 33*.*>
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
without coalescing packs
: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
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= " )ree flow COOT )/TT=7 " N 5=NT+:L /N " N
Operating 6ressure Operating Temperature /nlet ater in Oil %as )raction Liuid 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 '!$$!l W!i5t ater )illed eight
T:N TO =/+ " =))=5T/= =6 L=N%T9 O/L " =))=5T/= =6 L=N%T9 :T=+ " 9=/%9T O) =/+ " TOT:L ==L OLF$= "
-3E.20 ?*.00 3!.2>' 0.E32 0.>*3 EED.?
bara @5 CB v1v w1w v1v kg1mA
!.E?0 >.*D0 9 -00 -*! --?.!0 3 E?!D! !!>2E -*D*! 11,8,1 D>!?!
m m (91=# deg5 barg mm mm kg kg kg 5 kg
2
P&oc!$$ F!!. St&!a6 Su66a& Total mass flow 23D0E* kg1hr $ean density -3E.*-3 kg1mA %: 3!0000.00 kg1hr -0*.>0 kg1mA 0.0-? c6
Total flow rate Total liuid flow O/L DE-?3.00 kg1hr DDD.00 kg1mA 0.!>D c6
:T=+ 2??>!.00 kg1hr -00E.00 kg1mA 0.D>- c6
0.??- mA1s 0.02! mA1s )low 7ensity iscosity
No99l! Si9in5 Sc!.ul! N.C in )LF/7 /N
/.7 m -?
Pipe Sch. %: OFT
!0 Pipe Sch.
O/L OFT
? Pipe Sch.
:T=+ OFT
D Pipe Sch. FLAN#E TO FLAN#E PRESSURE ROP
?.*D0 E.*D0 E.0D0 -.0?0 D>.!?
m m m m mA
0.2-> 100 0.2*D 100 0.->> 100 0.-*2 40
5alculate +esidence time based on Tan LengthG (H1N# Length used for oil phase residence time calculation Length used for water phase residence time calculation
elocity m1s D.3>
rho&vI kg1msI *D0E
6ressure drop mbar !?.0
*.-*
!?0E
?.2
0.>-
*2D
-.D
0.E!
*!E
-.D ++4+
3 8.56 m 8.56 m
DOC O. !"#/0/31$/3*/1D/%/0
Li
Level m
Oil Oil Oil Oil Oil Oil Oil
99LL(!# 99LL 9LL NLL NLL LLL LLLL W!i& !i5t 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 adeuatelyG
0.0?2 0.-32 0.>3E
φwm = elected λ =
0.00E 0.0E0
!.?*
)or a meshpad B schoepentoeter (refer to 7=6 3-.!!.0*.--&%en ept !00!#
*.!-2 mI Less than actual gas space! Consult Prinicipal to see if it is acceptable
$ax. 7roplet to approach vane pack %as space axial velocity
0.03?
D0 microns 0.*!D m1s
m1s between N/L B microns between N/L B percent v1v microns
D? microns between N/L B essel bottom ppm v1v -00 microns
If a vane pack, use 0.1 to allow for slugs. If a bare vessel, use 0.07 +ecommended %as )low :rea
!.*? -0.*3 =4++ !.*3 -.E3.!0.00
)4)1,=
0.0-E 2? 0.* -00
Hes
λ= φ= f η f φ
olume between levels mA 0.00 3.!2 -0.0> 1(4=+ 3.!0 !.0E !.00 MM
+esidence time mins (/ncluding heads# 0.00 -.>3 D.00 ;4>, -.>0 -.!3 -.->
/nterval
99LL199LL(!# 9LL199LL NLL19LL NIL to LLL1NLL LLLL1LLL C1LLLL
3.-> -3.0;42) 3.-! !.-3.>D
9/L199/L N/L19/L NIL to L/L1N/L LL/L1L/L L/LL to
3? microns to NLL
:/:L )LF/7 =LO5/TH :5TF:L :T=+ 7+O6L=T +=JF/+=7 :T=+ /N O/L T:+%=T :T=+ 7+O6L=T
#AS CAP ANAL3SIS :ctual %as pace :rea %as 5ap height
)4)1=)
3?.? 3*.3 1;41 ->.-2.2 -0.?
)+O$ TO;= L: %: CFCCL= =6:+:T=7 %: +=$:/N/N% :T/)/= =JF/L/C+/F$ 5ON7/T/ON
without coalescing packs
: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
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= " -0m3 oil slug on case2 COOT )/TT=7 " N 5=NT+:L /N " N
Operating 6ressure Operating Temperature /nlet ater in Oil %as )raction Liuid 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!i5t 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$= "
-3E.20 ?*.00 30.2*' 0.E!3 0.>*0 ED>.?
bara @5 CB 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 22!E3* kg1hr $ean density -3>.-E* kg1mA %: 3!0000.00 kg1hr -0*.>0 kg1mA 0.0-? c6
Total flow rate Total liuid 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
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-> 100 0.2*D 100 0.->> 100 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 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 '
Oil Oil Oil Oil Oil Oil Oil
-.*>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.*
99LL(!# 99LL 9LL NLL NLL LLL LLLL W!i& !i5t ater 99/L ater 9/L ater NIL ater N/L ater L/L ater LL/L Fllage
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 adeuatelyG
0.0?2 0.-2! 0.>32
φwm = elected λ =
0.00E 0.0E0
!.?*
)or a meshpad B schoepentoeter (refer to 7=6 3-.!!.0*.--&%en ept !00!#
*.!-2 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
0 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,=
0.0-> 0 0.* -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 -.E* *.2D 84(2 -.E3 -.-! -.0?
/nterval
99LL199LL(!# 9LL199LL NLL19LL NIL to LLL1NLL LLLL1LLL C1LLLL
3.-> -3.0;42) 3.-! !.-3.>D
9/L199/L N/L19/L NIL to L/L1N/L LL/L1L/L L/LL to
3> 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)18=
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
without coalescing packs
: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
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 " D 5:= T/TL= " -0m3 water slug on case 2 COOT )/TT=7 " N 5=NT+:L /N " N
Operating 6ressure Operating Temperature /nlet ater in Oil %as )raction Liuid 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 '!$$!l W!i5t ater )illed eight
T:N TO =/+ " =))=5T/= =6 L=N%T9 O/L " =))=5T/= =6 L=N%T9 :T=+ " 9=/%9T O) =/+ " TOT:L ==L OLF$= "
-3E.20 ?*.00 3D.E3' 0.E-E 0.>*0 E>-.!
bara @5 CB v1v w1w v1v kg1mA
!.E?0 >.*D0 9 ?! -!0 --?.!0 3 E?!D! !!>2E -*D*! 11,8,1 D>!?!
m m (91=# deg5 barg mm mm kg kg kg 5 kg
P&oc!$$ F!!. St&!a6 Su66a& Total mass flow 22D-2* kg1hr $ean density -20.!2E kg1mA %: 3!0000.00 kg1hr -0*.>0 kg1mA 0.0-? c6
Total flow rate Total liuid flow O/L DE-?3.00 kg1hr DDD.00 kg1mA 0.!>D c6
:T=+ *?>D!.00 kg1hr -00E.00 kg1mA 0.D>- c6
0.??2 mA1s 0.022 mA1s )low 7ensity iscosity
No99l! Si9in5 Sc!.ul! N.C in )LF/7 /N
/.7 m -?
Pipe Sch. %: OFT
!0 Pipe Sch.
O/L OFT
? Pipe Sch.
:T=+ OFT
D Pipe Sch. FLAN#E TO FLAN#E PRESSURE ROP
?.*D0 E.*D0 E.0D0 -.0?0 D>.!?
m m m m mA
0.2-> 100 0.2*D 100 0.->> 100 0.-*2 40
5alculate +esidence time based on Tan LengthG (H1N# Length used for oil phase residence time calculation Length used for water phase residence time calculation
elocity m1s D.2-
rho&vI kg1msI *E*2
6ressure drop mbar !?.?
*.-*
!?0E
?.2
0.>-
*2D
-.D
0.?E
EDD
!.3 +(42
3 8.56 m 8.56 m
DOC O. !"#/0/31$/%5/1D/%/0
Li
Level m
essel fill '
Oil Oil Oil Oil Oil Oil Oil
-.*>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.*
99LL(!# 99LL 9LL NLL NLL LLL LLLL W!i& !i5t ater 99/L ater 9/L ater NIL ater N/L ater L/L ater LL/L Fllage
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 adeuatelyG
0.0?2 0.-22 0.>33
φwm = elected λ =
0.00E 0.0E0
!.?*
)or a meshpad B schoepentoeter (refer to 7=6 3-.!!.0*.--&%en ept !00!#
*.!-2 mI Less than actual gas space! Consult Prinicipal to see if it is acceptable
$ax. 7roplet to approach vane pack %as space axial velocity
0.02D
D0 microns 0.*!D m1s
m1s between N/L B microns between N/L B percent v1v microns
0 microns between N/L B essel bottom ppm v1v -00 microns
If a vane pack, use 0.1 to allow for slugs. If a bare vessel, use 0.07 +ecommended %as )low :rea
!.*? -0.*3 =4++ !.*3 -.E3.!0.00
)4)2)2
0.0-E 0 0.* -00
Hes
λ= φ= f η f φ
olume between levels mA 0.00 3.!2 -0.0> 1(4=+ 3.!0 !.0E !.00 MM
+esidence time mins (/ncluding heads# 0.00 -.>3 D.00 ;4>, -.>0 -.!3 -.->
/nterval
99LL199LL(!# 9LL199LL NLL19LL NIL to LLL1NLL LLLL1LLL C1LLLL
!.D2 -0.E> =4,> !.*> -.E* 3.!>
9/L199/L N/L19/L NIL to L/L1N/L LL/L1L/L L/LL to
3? microns to NLL
:/:L )LF/7 =LO5/TH :5TF:L :T=+ 7+O6L=T +=JF/+=7 :T=+ /N O/L T:+%=T :T=+ 7+O6L=T
#AS CAP ANAL3SIS :ctual %as pace :rea %as 5ap height
)4)1=)
3?.? 3*.3 1;41 ->.-2.2 -0.?
)+O$ TO;= L: %: CFCCL= =6:+:T=7 %: +=$:/N/N% :T/)/= =JF/L/C+/F$ 5ON7/T/ON
without coalescing packs
: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! Ticn!$$ ?66@
1
-
-
-
-
-
L %% L!n5t o/ Plat! ?6@
14)))
-.000
-.000
-.000
-.000
-.000
)4;))
0.>0
0.>0
0.>0
0.>0
0.>0
S!l!ct!. R!nol.$ No
)48)) 8()
0.?0 ?*0
0.?0 ?*0
0.?0 ?*0
0.?0 ?*0
0.?0 ?*0
)in *e+uire'ents for i"ing of ront rea of Plate Pack Oil Plat! Co&&!ction Facto& F
lo$$
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 Liuid1Liuid 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 SIIN# 0!&Nov&-* essel ref " $ultiuse separator 5ontract rev " essel i.d Liuid 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.! Wo A%%&oDi6at! !i5t 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 +euired 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 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.
C$ +ef " heatstone 5lient16ro8ect +ef " 0 essel " $ultiuse separator 5ase %as density (kg1mA# %as iscosity (c6# %as /nlet flow (mA1hr# Culk Liuid 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 ,
->?.* !2E.D !>*.2 3!*.2 3E3.2->.2DD.? *D0.2
?0 = 2>.! E3.E >E.! -2D.2 ->3.E !2!.? !?> 3-E.* 3D3.* 20>.D 2**.D *2E.E
EE?.02 ?!>.02 ?E>.02
O/L OFTL=T 6ipe i,e ch No (NC# ?
6ipe 7ia (mm# D0 2->.D
5:+CON T==L 7=/%N T+= (N1mm!# deg 5 ) (bar1-0# !* !03 *0 !03 -00 ->- elected -*0 -E* !00 -*>
20 ( *!.* EE.> -0!.3 -*2.!0!.E !*2.* 303.3 333.3 3?2!?.E 2EE.? *E2.D
->-
D0 D
m# -00 8
-!0 ;
-20 1)
-??.> !3D.* !?30? 3*2 3>?.* 22!.> *3-.?
>! -3>.? -?!.D !30.!E3.300 322.* 3?E.2 23-.? *-E.D
-EE.> !!!.! !DD.E !>!.333.2 3EE.? 2->.*02.?
>33.!2 >?2.!2 -03*.!2 -0?*.!2 --3D.!2 --?E.!2 -!?>.!2 -3>0.!2 -2>!.!2 -*>2.!2 -D>*.!2 -E>E.!2 -?>?.!2 3000.!2
>!D.> >EE.> -0!?.> -0E?.> --!>.> --?0.> -!?!.> -3?3.> -2?*.> -*?E.> -D??.> -E>0.> -?>-.> !>>3.>
>!0.*2 >E-.*2 -0!!.*2 -0E!.*2 --!3.*2 --E2.*2 -!ED.*2 -3EE.*2 -2E>.*2 -*?-.*2 -D?!.*2 -E?2.*2 -??*.*2 !>?E.*2
6ipe 7ia (mm# ->?.*
-D0 N 11 2!.? DD.D ?E.3 -3-.? -E3.!-*.? !*E.! !?2.! 3!*.2 3DD.E 20? 2>0.*
>-2.! >D*.! -0-D.! -0DD.! ---E.! --D?.! -!E0.! -3E-.! -2E3.! -*E*.! -DED.! -EE?.! -?E>.! !>?-.!
:T=+ OFTL=T 6ipe i,e ch No (NC# D
12 *0.? ED.! -0-.D -*!.2 !03.! !*2 302.? 3**.D 20D.2 2*E.! *0? D0>.D ED! ?-!.? ?D3.D >-2.2 >D*.! -0-D -0DD.? ---E.D --D?.2 -!->.! -3!0.? -2!!.2 -*!2 -D!*.D -E!E.! -?!?.? ->30.2 !03!
6ipe 7ia (mm# 20 -*2.*
%: OFTL=T 6ipe i,e ch No (NC# !0
?0 E
6ipe 7ia (mm# 2**.D
S!!t Calculation No: Cli!nt: P&o!ct: Location: Cont&act No:
>*-D (check# 67O 9arweel 6hase ! Oman L3??*
RE' 66! ! 3
B3 69yp 69yp
1)
o/
11
CH $;
APP
ATE 31!D1!002 *1!D1!002
HORIONTAL > PHASE SEPARATOR SIIN# 1*2 Si9in5 7esign !$c&i%tion: -st tage eparator
Ta5 No: !-0#a$ Flo Oil Flo Wat!& Flo Flui. P&o%!&ti!$ 7ensity (actual# (kg1mA# iscosity (c6# $olecular t )low (kg1hr# )low (actual mA1min# Alloa"l! 'a%ou& '!locit g ;((6l&6v#16v#UV %as eparation 5onstant egmental area reuired for gas flow W!i& H!i5t ?inclu.in5 li
E.0?02 $$td mA 1 day (-*54 -atm# -32E actual mA1day --E3 actual mA1day #a$ *3.00 n1a ->.>? !.2>3=S0* E?.3>
P*Pl*P
'5 *,)K'5 F5 c&!$tl A AKF5 L
' '1
!*0.*D $$5)7 (D0)4 -atm# ?2D> C67 (actual# E3?0 C67 (actual#
Oil D>> 0.3* n1a 3.>!!=S02 0.>2
Wat!& -000 0.*E n1a 2.??>=S02 0.?-
0.!> 0.0?3 2.*0> *> 0.3?>!
m1s m1s (hell 7=6 3-.!! .0*.--# mI ' of 7iameter
32 !.E?0 D.0E0 !.3D! &2? >.*D 3.22 -.000 *?.03
mm (hell 7=6 3-.!!.0*.-!# m mI mI ' m
"
m from Oil outlet end Tan Line mA
*-.>D mA 3-.E2 mA
/T=+:T= FNT/L O/L :N7 :T=+ +=/7=N5= T/$= =5==7 =TTL/N% T/$=. ($:H N==7 TO :7
-*.!> ' of 7iameter >.E ' of Overall 5: *-.2 ' of Overall 5:
A$ A$
"
Li
Oil -!0?
Wat!& 2!*
A$K'1 *
min
-*.3
D.!
T KT
min mA bbl
*.00 ?.E* *2.>
9eight of phase
+esidence time Si9in5 "a$!. on API 12J ?C!c 7!to.@ +etention Time & T Total Liuid olume +euired & oilSwater
*.00 min 2.0E mA !*.D bbl