Objectives and Indicators for MCH Programs MCH in Developing Countries.
ECUMED Sizing Report for the First Phase Rev_0 MCH (Réparé) (2)
Transcript of ECUMED Sizing Report for the First Phase Rev_0 MCH (Réparé) (2)
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Project: ECUMED -El BibaneFeasibility Study for EBB Plant Upgrade For Gas
Commerciali ationProject NO Contract NO EPPM document NO
Clientdocument NO
Rev
!"##$#% &'(
))))) ))))) ))))) *
Date XX/XX/XXXX Page # of +(
"EP'",
E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",
ECUMED PE,"'2EUM
1 21/0 /201! "##ued $ora%%roval
&'N'-MC( MC( M)"
0 1*/0 /201! "##ued $orRevie+ &'N' MC( M)"
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P"'CESS "E3.E& "E-U."ED M'D.F.C!,.'/ "EP'",
/'4 "###%5"P,5P"5**5**#"E34!P!GE: % $ 6(
"E3 D!,E Designation/!ME 3.S! /!ME 3.S! /!ME 3.S!
Prepared by 3eri7ed by !ppro8ed by
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S,P!",
/'4"E34 *P!GE: ( $ 6(
"e8isions report:
"e8ision /o "e8ision Description0 "##ued $or Revie+1 "##ued $or '%%roval
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: 9 $ 6(
, !B2E 'F C '/,E/,S
1. INTRODUCTION................................................................... ............ ......... 6
1.1 G ENERAL.................................................................................................................6
1.2 P ROJECT DETAILED S COPE ...........................................................................................6
1.3 D OCUMENT S COPE .....................................................................................................7
1.4 D EFINITIONS & ABBREVIATIONS ....................................................................................7
1.4.1 DEF IN IT ION S................................. ................................. .................................. ....... ...... ....... ..... 7
1.4.2 ABB REV IAT IO NS.............................................................................................................................8
1.5 U NITS O F MEASUREMENT ............................................................................................8
2. DESIGN DATA..........................................................................................10
2.1 E NVIRONMENTAL DATA..............................................................................................10
2.1.1 CL IMAT IC AN DM ETE ORO LOG ICALC OND IT IO NS...........................................................................................................................10
2.1.2 GR OUN DAN DS OIL CO ND IT IONS...........................................................................................................................11
2.2 ELLS! LOCATION ...................................................................................................11
2.3 P ROCESS DESIGN D ATA............................................................................................11
2.3.1 EL L"E AD PA RAMET ER S...........................................................................................................................11
2.3.2 CO MPO SIT IO NS...........................................................................................................................12
2.4 CPFDES IGN PARAME TER S...........................................................................................................................122.5 GAS RE #U IR ED SPE CIF IC AT IO N $STEGSPE CIF IC ATIONS%...........................................................................................................................12
3. CALCULATION METHODS.......................................................... ............ ...13
3.1 P ROCESS DESIGN TOOLS ..........................................................................................13
3.2 T "ERMOD NAMICS ...................................................................................................13
3.3 M ODEL D ESCRIPTION ' B ATTER LIMITS AND ASSUMPTIONS ...............................................13
3.3.1 FLU ID R ESE RVOIR...........................................................................................................................13
3.3.2 EL L"E ADS...........................................................................................................................14
3.3.3 PIPE L IN E...........................................................................................................................14
3.3.4 FIRS TS EPA RATION...........................................................................................................................14
3.3.5 AMIN E UN IT...........................................................................................................................14
3.3.6 GL&C OL DE "&DRAT ION UN IT...........................................................................................................................14
3.3.7 CO NDE NS AT ER EMOVA L UN IT...........................................................................................................................15
3.3.8 INJEC TION G ASC OMP RES SO R...........................................................................................................................16
3.3.( CO NDE NS AT ES TAB IL I) AT ION...........................................................................................................................16
4. DESIGN OF THE NEW AMINE UNIT............................................................ 20
4.1 SELECTION FACTORS FOR T"E T PE OF AMINE................................................................20
4.2 CO 2 SELECTIVIT .................................................................................................20
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: + $ 6(
4.3 * INETICS OF REACTION IT" CO2..............................................................................20
4.4 C ORROSIVIT ..........................................................................................................21
4.5 A MINE CONSUMPTION AND PRICE................................................................................21
4.6 T "ERMOD NAMICS OF REACTION IT" CO2..................................................................214.7 M AIN E#UIPMENTS S I)ING .........................................................................................21
4.7.1 DET ER MIN AT ION OF AM IN EF LO RATE...........................................................................................................................21
4.7.2 SI) IN G OFCO2ABSORB ER...........................................................................................................................22
4.7.3 AMIN E REG ENERATOR...........................................................................................................................23
4.7.4 LEA NA MINE CIRCUL AT ION PUM PS...........................................................................................................................23
4.8 SI) IN G OF" EAT E+C" AN GER...........................................................................................................................24
4.8.1 SI) IN G OFLE AN AMIN EA IR C OOLER...........................................................................................................................24
4.8.2 SI) IN G OFR IC ",LEA NA MINE "EAT E +C"A NG ER...........................................................................................................................244.8.3 SI) IN G OFR EGENE RAT OR C ONDENS ER...........................................................................................................................25
4.8.4 SI) IN G OFR EGENE RAT OR R EBOILER...........................................................................................................................25
4.8.5 SI) IN G OFA MINE FLAS "D RUM...........................................................................................................................26
5. REVISION OF TEG UNIT DESIGN.............................................. ............ .....26
5.1 REVISION OF TEG CONTACTOR DESIGN..................................................................26
5.2 CURRENT TEG REGENERATION UNIT DESIGN......................................................28
5.2.1 GL&C OL FLAS "TAN* OPE RAT IN G DATA AND DIME NS IO NS...........................................................................................................................28
5.2.2 "E AT E +C "A NGERS INP UT DATA...........................................................................................................................2(
5.2.2.1 AIR,G L&CO L"EAT E+C" AN GER E320...........................................................................................................................2(
5.2.2.2 GL&C OL,G L&C OL " EAT E+C" ANGER...........................................................................................................................2(
5.2.2.3 GL&C OL REG EN,DR& GAS ECO NOMI)E R...........................................................................................................................2(
5.3 GL&C OL PUM PS...........................................................................................................................30
5.4 CO NDE NSE RC OIL E+C" AN GER...........................................................................................................................30
5.5 RE GEN ERATO R RE BOILE R...........................................................................................................................30
5.6 LGSTR IP P IN G COLU MN...........................................................................................................................30
5.7 LGST IL LC OLUMN-...........................................................................................................................315.8 REGENERATION PROCESS TROUBLE S"OUTING ................................................................32
5.8.1 STR IP P IN G GAS FLORATE...........................................................................................................................32
5.8.2 STR IP P IN G GAS COLU MN DES IGN $DIAME TER %...........................................................................................................................33
6. NEW CHILLING UNIT................................................................................34
6.1 R EFRIGERANT FLUID SELECTION ..................................................................................34
6.2 P ROPANE RECEIVER .................................................................................................34
6.3 P ROPANE COMPRESSOR ............................................................................................35
6.4 P ROPANE CONDENSER ..............................................................................................35
6.5 P ROPANE ECONOMI)ER VJ 4003-...............................................................................36
6.6 G AS,P ROPANE " EAT E+C"ANGER EJ 4003...................................................................36
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: 6 $ 6(
6.7 G AS,G AS O UTLET COLD S EPARATOR " EAT E+C"ANGER EJ 4001A...................................37
6.8 G AS,LI#UID " EAT E+C"ANGER EJ 4002......................................................................37
6.( C OLD S EPARATOR ....................................................................................................37
7. NITROGEN SKID...................................................................................... 38
8. SIZING OF I ELINE................................................................................ 3!
!. CONCLUSION.......................................................................................... 42
10. A ENDICES........................................................................................... 44
10.1 APPENDI+ 1- RECIRCULATION RATE OF DEA SOLUTION ..................................................44
10.2 APPENDI+ 2- AMINE CONTACTOR DIAMETER CALCULATION ..............................................44
10.3 APPENDI+ 3- AMINE REGENERATOR DIAMETER CALCULATION ..........................................44
10.4 APPENDI+ 4- GPSA STANDARD FOR TEG CONTACTOR SI)ING ........................................45
10.5 APPENDI+ 5- NORSO* STANDARD FOR SI)ING OF GAS LINE.............. ....... ...... ....46
10.6 APPENDI+ 6- AMINE UNIT "EAT E+C"ANGERS TEMA S"EETS........................ ......47
10.7 APPENDI+ 7- GLCOL UNIT "EAT E+C"ANGERS TEMA S"EETS...................... ......4(
10.8 APPENDI+ 8- C"ILLING UNIT "EAT E+C"ANGERS TEMA S"EETS........ ...... ....... ....52
10.( APPENDI+ (- STRIPPING GAS COLUMN DESIGN................................ ...... ....... ...... 56
10.10 TIE IN PROCEDURE TO ADD AMINE FLAS" VAPOR TO STRIPPING GAS PROCESS
58
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: $ 6(
#4 ./,"'DUC,.'/
1 1. ENER')
El- i ane o # ore +ell# are located at a out 1* 3m far from t e CP$ 4t eon# ore central %roce##ing facilit56 #ituated on t e to+n of 7ar8i#
Pre#entl59 El- i ane :eld i# o%erating a# de#cri ed elo+;
- Producing from t e o # ore +ell E > e %roduction i# andled to t e CP$ t roug an *? #ea line and t e treated ga#
i# rerouted from t e CP$ to e re-injected t roug ? #ea line
Figure #: ,;e 'ns;ore ℓeads Con7guration
1 2P RO@EC> DE>'")ED &COPE
> e main engineering ta#3# for t i# %roject can e #ummari8ed into t ree 4!6%art# a# follo+#;
1/ $ea#i ilit5 #tud5 for #elling 1/! of ga# %roduction and injection of t e
remaining Auantit5;
- Pre%are t e reAuired #imulation# to #ell ,-= MM&C$D and inject B-11
MM&C$D of ga# in order to recover conden#ate
- De:ne t e reAuired %roce## modi:cation# for t e :r#t % a#e
- Perform needed calculation# for modi:ed or %otential additional reAuired
eAui%ment#
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: < $ 6(
- Develo% t e co#t e#timation for t e related modi:cation#
- a#ed on t e recovered conden#ate Auantit5 and t e ga# #ale#9 develo%
t e :r#t % a#e economic anal5#i#
2/ $ea#i ilit5 #tud5 for #elling t e total ga# %roduction;
- Pre%are t e reAuired #imulation# for treatment of 1= MM&C$D of ga# to
t e #ale# #%eci:cation; t e total ga# %roduction +ill e #old and no re-
injection to e con#idered > u#9 no conden#ate recover5 o%timi8ation to
e con#idered ot er t an t e ga# treatment reAuired to meet commercial
#%eci:cation# Conden#ate recover5 +ill #till e %o##i le and it +ill e #old
#e%aratel5
- De:ne t e reAuired %roce## modi:cation# for t e #econd % a#e
- Perform needed calculation# for modi:ed or %otential additional reAuired
eAui%ment#
- Develo% t e co#t e#timation for t e related modi:cation#
- a#ed on t e ga# #ale# develo% t e #econd % a#e economic anal5#i#
- '# an alternative economic o%tion9 one anal5#i# +ill e made for t e
im%lementation of t e reAuired modi:cation# on t e facilitie# to treat t ecom%lete 1= MM&C$D in one time and to #tart treatment of onl5 ,-=
MM&C$D in t e :r#t % a#e and u#e t e remaining Auantit5 to recover
conden#ate
!/ $ea#i ilit5 #tud5 for #ale# ga# tran#%ortation
- '##e##ment of t e di erent t5%e# of ga# tran#%ortation met od#9 de%end
on t e tie-in %oint location and ga# c aracteri#tic# > e o%tion of
tran#%ortation of non treated ga# +ill e al#o a##e##ed
- Pre%are t e reAuired #imulation#/ 5draulic calculation# for tran#%ort of
1= MM&C$D of ga# to a tie-in %oint to t e &>E. net+or3
- a#ed on t e ga# #ale# develo% an economic anal5#i#
,;e present report is de8oted to t;e 7rst p;ase= t;e feasibility study for
selling #$( of gas production and injection of t;e remaining >uantity4
1 !D OC MEN> &COPE > e o jective of t i# document i# to c ec3 t e o%era ilit5 and t e adeAuac5 of
t e e i#ting facilitie# and to #i8e reAuired additional eAui%ment# on ot CP$
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: ? $ 6(
and ot er unit# relevant to El i ane $ield Develo%ment Project > i# #tud5 a#
een carried out for a total ga# %roduction of 1=MM&C$D9 ca#e of #elling 1/! of
ga# %roduction and injecting t e remaining Auantit5 in order to recover
conden#ate
1 ,D E$"N">"ON& ' REF"'>"ON&
1 , 1 D E$ "N "> "ON&
$or t e %ur%o#e of t i# document t e follo+ing de:nition# # all a%%l5;
'@ner$Client EC MED Petroleum
Contractor EPC contractor
Engineering company Engineering Procurement and Project
Management 4EPPM6
Project El i ane-Detail Engineering for .a# C5cling
Production Pilot Project
Supplier$ 3endor > e %art5 4#6 + ic manufacture# and/or
#u%%lie# eAui%ment9 tec nical
Document#/dra+ing# and #ervice# to %erform t e
dutie# #%eci:ed
1 , 2 ' // RE F"'>"ON&
> e follo+ing a reviation# +ill e u#ed;
B1P : ottom-(ole Pre##ureCPF : Central Proce##ing $acilit5
EBBA : El i ane Gell ead num erE'S : EAuation of &tate1P : (ig Pre##ure113 : (ig er (eating Falue
, : @oule > om#on2P : )o+ Pre##urePC3 : Pre##ure Control FalvePFD : Proce## $lo+ DiagramSEEB : Electricit5 Com%an5 of El- i ane 4H &ociItI dJElectricitI El-
i ane K6S,EG : >uni#ian Com%an5 of Electricit5 and .a# 4H &ociItI >uni#ienne
dJElectricitI et de .a8K6,EG : >ri Et 5lene .l5col
1 = N">& O $ M E'& REMEN>
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: #* $ 6(
"n general9 &" unit# +ill e u#ed (o+ever9 t ere are recogni8ed e ce%tion# and
%referred unit# t at are u#ed in t e Oil .a# indu#tr5
,able #: Units of Measurement
Measured -uantity Preferred Unit DesignationCorro#ion 'llo+ance Millimeter# mmDen#it5 3ilogram %er cu ic meter 3g/m !
Electric Current 'm%ere ' milli-am%ere m'
Electric Potential Folt F
Electric Po+erGatt GLilo+att 3GMega+att MG
Electric Re#i#tance O m O mEnt al%5 Lilo @oule %er 3ilogram 3@/3g$orce Ne+ton or 3ilo Ne+ton N or 3N$reAuenc5 (ert8 (8(ead Meter# m(eat )oading Lilo+att# 3G(eat >ran#ferCoe icient
+att# %er #Auare meter %erdegree Cel#iu# G/m
2 C
)atent (eat 3ilo @oule# %er 3ilogram 3@/3g)engt millimeter#9 meter#9 3ilometer# mm9 m9 3m)uminance )u )Ma## Lilogram 3gMa## $lo+ Rate 3ilogram/ our 3g/Mec anical Po+er 3ilo+att#9 mega+att 3G9 MGDiameter "nc e# "n
Pre##ure ar gauge9 ar a #olute9Lilo%a#cal arg9 ara9 3Pa
Rotational &%eed revolution# %er minute RPM)o+er (eating Falue4)(F6
3ilocalorie# %er &tandard cu icmeter 3cal/&CM
&%eci:c (eat 3ilojoule# %er 3ilogram degreeCel#iu# 3@/3g C
&tre## Ne+ton %er #Auare meter N/m 2
>em%erature degree Cel#iu# C> ermal Conductivit5 +att %er meter Cel#iu# G/m C>ime 5ear / da5/ our/minute /#econd 59 d9 r9 min9 #
Felocit5 meter# %er #econd or meter#%er our m/#9 m/
Fe##el Dimen#ion# meter#9 millimeter# m9 mm Folume 4actual6 cu ic meter# m !
&tandard .a# Folume &tandard cu ic meter &CM 4Note 16
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: ## $ 6(
Measured -uantity Preferred Unit Designation
Folume .a# $lo+ meter /da5 4%er our6Million &tandard cu ic feet/da5&CMD 4&CM(6MM&C$D
Folume 4liAuid6 Cu ic meter m !
Folume $lo+ 4liAuid6
Cu ic meter/ ourCu ic meter/ da5arrel/da59 arrel Oil/da59 arrelGater/da59 arrelConden#ate/da5
m ! /m ! /da5PD9 OPD9GPD9 CPD
Pi%e/No88le #i8e# "nc e# "n
D5namic Fi#co#it5Linematic Fi#co#it5
Centi%oi#e# cPCenti#to3e# c&t
&tandard condition# are 1 01!2= ara at 1= = C
Normal condition# are 1 01!2= ara at 0 C%4 DES.G/ D!,!
2 1E NF"RONMEN>') D '>'
2 1 1 C )"M '> "C 'ND ME> EO RO) O."C') CO ND "> "ON &
El- i ane +eat er i# c aracteri8ed 5 moderate +inter and #moot er #ummer
mean+ ile #ome occa#ional #torm# ma5 occur
'ns;ore Data: Gind Direction and #%eed;
o Dominant +ind direction ENE
o Ma imum +ind #%eed;
One our +ind #%eed; 1!0 3m/
One minute +ind #%eed; 1 , 3m/ De#ign 'm ient >em%erature#;
o Mean minimum air tem%erature; 0 Co Mean ma imum air tem%erature; !2 C
o Ma imum air tem%erature; =0 C Relative (umidit5; 0- * 'ir %re##ure; 1, ! %#ia Rainfall;
o Minimum mont l5 rainfall; 1 mm
o Ma imum mont l5 rainfall; ,1 mm
' s;ore Data:
Minimum #ea ed tem%erature; 1! C
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: #% $ 6(
&till +ater level 4average6; 0 m Ma imum centenar5 +ave eig t; = = m &+ell eig t ; ! = m Period a##ociated +it ma imum +ave; 12 1 # Ma imum tide elevation a ove #till +ater; Q1 1 m One our +ind #%eed; 1!0 3m/ One minute +ind gu#t; 1 , 3m/ &urface current #%eed; 1 1 m/# =0 de%t current #%eed; 0 B m/# ottom current #%eed; 0 = m/# Conductivit5 420 C6; =0 m&/cm
2 1 2 . RO ND 'ND &O") C ON D">"ON&
> e o # ore #oil %ro%ertie# are inve#tigated 5 %re##ure-metric #urve59 t e main
re#ult# could e #ummari8ed in t e follo+ing ta le;
,able %: El5Bibane ' s;ore Soil Pro7le
Dept; Soil ,ypeE ecti8e
2imitPressure
Sub5GradeModulus
Friction !ngle
&and#tone Q != ar# 00-1000 !0-!=12m-20m (ard ,0 ar# 1000-1100 !=-,0
> e &ei#mic 7one; 8one 0
2 2G E))& J ) OC'>"ON
> e ta le given elo+ indicate# +ell#J location
,able (: &ells 2ocation
&ell Statu U,M U,M y "emar s
E
None 1!B,2 ! 02!10 &ame a# E
E
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: #( $ 6(
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: #9 $ 6(
Parameter E>uipment
DesignPres4 barg
Design,emp4 HC
Capacity$Dimensions
Compress
or I59** !$B
First
Stage
&uction/di#c arge
!0/*, =
- -
Second
Stage
&uction/di#c arge
*, 2/22*- -
1eater 15#*% Outlet >em% == C
2 = .'& REV "R ED &PE C"$"C '> "ON 4&>E.& PEC "$ "C '>"ON&6
> e reAuired #ale# ga# #%eci:cation# are #ummari8ed in t e ta le elo+;,able 6: "e>uired Gas Speci7cations
Parameter Unit 3alue
(ig er (eating Falue 3cal/Nm ! B!00 W 1022*
Go e "nde 3cal/Nm ! 11B 1 W 12 ,0
Gater content 4%%m6 U *0( 2& content mg/Nm ! 2&ulfur content mg/Nm ! =0.a# tem%erature C 10 W =0CO 2 content mol 0 =( 2 and N 2content mol
O2 content mol 0
(4 C!2CU2!,.'/ ME,1'DS
! 1P ROCE&& DE&".N > OO)&
> e #oft+are (Y&Y& 4ver#ion !6 i# u#ed for t e %roce## #imulation under
#tead5 #tate condition#
&c lum ergerJ# P"PE&"M modeling &oft+are ver#ion 200B i# u#ed for %roce##calculation and 5draulic #imulation for t e #tud5 at #tead5 #tate for t e %i%eline
connecting t e %i%ing outlet t e CP$ +it t e tie-in %oint on t e &>E. ga#
net+or3
! 2> (ERMODYN'M"C&
> e #imulation# ave een %erformed a#ed on Z'mine %ac3age? in amine unit
#imulation and ZPeng/Ro in#on EO&? u#ing t e inar5 coe icient data %rovided
5 (Y&Y&
! !M ODE) DE&CR"P>"ON 9 '>>ERY ) "M">& 'ND ' && MP>"ON&
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: #+ $ 6(
! ! 1 $ ) "D R E&ERFO"R
> e ga# and oil com%o#ition# 4'%%endi 26 re#%ectivel5 inlet and outlet t e (P
#e%arator are recom ined and reintroduced a# a feed #tream (ence t e#e%arated ga# com%o#ition i# given in t e ta le elo+;
,able : Estimated separated Gas composition
C'MP'/E/,S M'2E F"!C,.'/CO 2 0 01
Nitrogen 0 01 2Met ane 0 *2=Et ane 0 0 *!
i- utane 0 00
n- utane 0 00B*i-Pentane 0 00!n-Pentane 0 00!1n-(e ane 0 001=Pro%ane 0 0!!en8ene 0 0002
C5clo e ane 0 00022-M%entane 0 000!-M%entane 0 000!2-M e%tane 0 0001
>oluene 0 0001n-(e%tane 0 000n-Octane 0 0001n-Nonane 0 0001
2-M e ane 0 0002!-M e ane 0 0001
! ! 2 G E)) (E' D&
> e +ell ead #tream from E
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: #6 $ 6(
calculation#
' t ermal conductivit5 of t e %i%e material of ,= G/m\ L +ill e a##umed
! ! , $ "R &> & EP'R'> "ON
> e CP$ inlet %roduction i# carried into t e (P t ree % a#e# #e%arator 4F-10016
a# a :r#t removal of +ater and conden#ate > i# #e%arator a# a de#ign %re##ure
of 100 arg + ic can limit t e CP$ inlet %re##ure > e ga# at t e inlet of
#e%arator i# con#idered at !1 arg and !1 C
! ! = ' M"NE N">
"n order to remove car on dio ide from inlet ga#9 an amine unit i# fore#een
do+n#tream (P t ree % a#e #e%arator 4F-10016
> e 'mine unit +ill e de#igned to treat 1 MM&C$D of ga# +it 1 mol
CO 29 5 circulating lean amine #olution 4!0 +t DE'6 t roug t e contactor to
remove car on dio ide from inlet ga# and #ati#f5 t e cu#tomerJ# reAuirement of
0 = CO 2 Ric amine from t e ottom of t e Contactor i# a# ed from
a%%ro imatel5 !2 ara to = ara t roug a level control valve and #ent to t e
'mine $la# Drum to #e%arate t e 5drocar on ga# from DE' #olution > e ric
DE' i# eated to a%%ro imatel5 = C 5 t e Ric /)ean 'mine E c anger and
t en fed to t e 'mine Regenerator > e lean amine i# cooled t roug t e
Ric /)ean 'mine E c anger and %um%ed via t e 'mine oo#ter Pum%# to t e
)ean 'mine 'ir Cooler and t en t roug lean amine :lter# > e lean amine i#
cooled to a%%ro imatel5 ,0 C and routed ac3 to t e 'mine Contactor after
adju#tment of amine #olution o+ rate and com%o#ition 5 t e +ater ma3e-u%
! ! . )YCO )D E(YDR '> "ON N">
"n order to %revent 5drate formation9 a >E. contactor unit i# fore#eenu%#tream of t e @-> om#on conden#ate removal unit
"n order to %revent 5drate formation9 a >E. contactor unit i# fore#een
u%#tream of t e @-> om#on conden#ate removal unit
> e #+eet ga# from t e 'mine Contactor i# routed to t e .l5col contactor 4>-
106 near it# ottom and o+# u%+ard t roug t e ottom tra5 to t e to% tra5
and out at t e to% of t e column )ean gl5col i# fed at t e to% of t e column and
it# o+# do+n from tra5 to tra59 a #or ing +ater va%or from ga# > e Contactor
o%erate# at ] =0 C and !0 ara +it a lean >E. De 5drated ga# from t e
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: # $ 6(
Contactor over ead i# eated t roug t e .a#/.l5col (eat E c anger 4E-!106 to
== C and routed to t e @-> om#on unit to recover conden#ate
Ric >E. from t e contactor 4>- 106 +ill e %re eated t roug t e over ead
conden#er on t e gl5col #tri%%er #till column and a# ed to a%%ro imatel5 , ,
ara in t e gl5col a# tan3 4F-1206 > e a# ed ga# i# #ent to t e are net+or3
> e ric >E. i# ne t :ltered efore entering t e .l5col reconcentrator 4(-,106
to remove t e a #or ed +ater > e lean >E. #e%arated from +ater i# cooled in
t e 'ir/.l5col eat e c anger 4E-!206 and %um%ed t roug t+o .l5col %um%#
4P-=10'/ 6 to t e .a#/.l5col eat e c anger 4E-!106 for furt er cooling efore
returning to .l5col contactor >- 10
! ! C ON DEN &'>E R EM OF') N">
"n order to remove an5 conden#ate9 t e ga# # ould %a## t roug a liAuid
removal unit 5 reduction of tem%erature 5 u#ing a @oule-> om#on e %an#ion
unit > e conden#ate removal unit con#i#t# of t e follo+ing item#;
(eat E c anger 4E@-,0016; ga#/ga# eat e c anger
> e eat e c anger de#ign %re##ure i# = arg for ot # ell and tu e# #ide
+ ic +ill limit t e ma imum o%erating %re##ure efore t e @oule-> om#on
e %an#ion
@>-Falve 4PCF-,0016
> e e %an#ion %re##ure !0 arg i# con#idered t e lo+e#t value reac ed 5 t e
valve and + ic de:ne t e com%re##or :r#t #tage #uction %re##ure 'ctuall5 t e
@> valve i# full5 o%ened
&e%arator 4F@-,0016
"t i# %rovided to #e%arate ga# from t e formed conden#ate after %re##uree %an#ion
> e :gure given elo+ # o+# a #c ematic of t e conden#ate removal unit
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H"#$ E%&'#()"*G#+,G#+
D*- G#+
W"$ G#+
E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: #< $ 6(
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: #? $ 6(
Figure %: Condensate remo8al unit 5,;omson unit
! ! * "N@E C> "ON .'& COMPR E && OR
' multi#tage injection ga# com%re##or i# #imulated to increa#e t e injection ga#
%re##ure from !0 arg to a%%ro imatel5 1=* arg via t+o #tage# com%re##or 't
t e level of t e com%re##orJ# #cru er#9 t e %o##i le formed conden#ate i#
rec5cled to t e MP #e%arator 4F-1006
! ! B C ON DEN &'>E & >' / ") "7 '> "ON
> e removed conden#ate from di erent CP$ unit# i# #ent to conventional t+o
% a#e# #e%arator# 4F-100 F-1016 reAuiring a long re#idence time for
conden#ate #ta ili8ation > en t e eated conden#ate o+ing from t e eater
4(-1026 i# #ent to t e #torage tan3# 4>-101 '/ 6
> e recu%erated Auantit5 of conden#ate # all e #ta ili8ed at a #uita le %roce##
o%erating condition#
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: %* $ 6(
> e (Y&Y& o+# eet of t e CP$ con#idering t e ne+ con:guration i# # o+n in t e follo+ing :gure
Figure (: 1JSJS PFD of t;e CPF
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: %# $ 6(
> e #u - o+# eet of 'mine nit i# modeled a# # o+n in t i# :gure;
Figure 9: ,;e !mine Unit Modeled Flo@ s;eet
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: %% $ 6(
> e #u - o+# eet of De 5dration nit i# modeled a# # o+n in t i# :gure;
Figure +: ,;e ,EG Unit Modeled Flo@ s;eet
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: %( $ 6(
94 DES.G/ 'F ,1E /E& !M./E U/.,
, 1 &E)EC>"ON $'C>OR& $OR >(E >YPE O$ 'M"NE
> e c oice of t e %roce## #olution i# determined 5 t e %re##ure and tem%erature
condition# at + ic t e ga# to e treated i# availa le9 it# com%o#ition +it re#%ect to
major and minor con#tituent#9 and t e %urit5 reAuirement# of t e treated ga#
ME'; eliminate# #imultaneou#l5 and non-#elective 5drogen #ul:de and car on
dio ide "t i# ine %en#ive (o+ever9 it a# #everal dra+ ac3# $ir#t9 it react# in an
irrever#i le manner +it merca%tan# "n addition9 it# va%or %re##ure i# relativel5
ig 9 re#ulting in greater lo##e# com%ared to ot er amine# $or t e#e rea#on#9 it i#
mainl5 u#ed + en t e concentration of acid ga#e# i# relativel5 lo+9 t erefore +ecannot u#e it
D.'; "t i# more e %en#ive t an t e DE' and a# al#o t e di#advantage of
5drocar on# a #or%tion9 t erefore +e cannot u#e it
D"P'; a%%lication# mainl5 concern t e treatment of ga# containing CO&9 a# +ell a#
t e recover5 and rec5cling of ( 2&
> e t+o t5%e# of amine# commonl5 u#ed for removal of CO 2 from natural ga# are
DE' and MDE'
> e main #election factor# of t5%e# of amine# for t e %uri:cation of natural ga# are
li#ted ere 5;
- CO 2 &electivit5
- Linetic# of reaction +it CO 2
- Corro#ivit5
- 'mine con#um%tion and %rice
- 'mine degradation
- > ermod5namic# of reaction +it CO 2
, 2CO 2 &E)EC>"F">Y
&electivit5 i# a alance et+een t e ma## tran#fer rate# of t e acid ga#e# com%eting
for t e amine in t e #olvent > e le## reactive t e amine9 t e etter t e #electivit5
MDE' i# fairl5 #elective to+ard# (2& removal ga#e# containing ot ( 2& and CO 2
ecau#e it doe# not react directl5 +it CO 2 "n #uc ca#e9 DE' i# t e e#t #olution
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: %9 $ 6(
, !L "NE>"C& O$ RE'C>"ON G">( CO2
> e reaction et+een CO2 and DE' amine# i# #igni:cantl5 fa#ter t an t e reaction
et+een CO2 and MDE'9 t erefore t e DE' i# favored 3ineticall5
, ,C ORRO&"F">Y
> e DE' i# more corro#ive t an MDE' ut in t i# ca#e t e corro#ion i# not an
im%ortant factor for t e #election of t e amine t5%e ecau#e t e e i#ting facilit5 i#
#i8ed for t e mo#t corro#ive amine t5%e
, =' M"NE CON& MP>"ON 'ND PR"CE
> e oiling tem%erature of DE' i# ig er t an t at of MDE' t erefore t e lo##e# of
amine are greater for t e ca#e of MDE'
> e DE' i# le## e %en#ive t an MDE' t erefore t e DE' i# favored according to
%rice factor
, > (ERMODYN'M"C& O$ RE'C>"ON G">( CO2
ot t5%e# of amine #olution# are almo#t total t erefore t e5 are
t ermod5namicall5 favored (o+ever9 t e MDE' doe# not react directl5 +it CO 2
t erefore it# conver#ion rate i# lo+er com%ared to DE' conver#ion rate
(ence in t i# ca#e t e DE' i# t ermod5namicall5 favored
>o #ummari8e9 a# %er &electivit5 for CO 29 Price of amine9 Linetic# of reaction +it
CO 29 Corro#ivit59 'mine degradation and 'mine con#um%tion9 and t ermod5namic#
of reaction +it CO 29 t e %erformed amine for t e ga# treatment i# t e DE'> e criteria of c oice of t e t5%e of amine are #ummari8ed in t e follo+ing ta le;
,able ermod5namic Q -Price of amine Q -Linetic# of reaction +it
CO 2Q -
Corro#ivit5 - Q 'mine degradation Q Q
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: %+ $ 6(
C oice criteria DE' 4!06 MDE' 4,0 6 'mine con#um%tion Q -
> erefore +e ave c o#en to u#e t e DE' #olution for natural ga# treatment
, M '"N E V "PMEN>& &"7"N.
, 1 D E>E RM "N '>"ON O$ 'M "N E $)OGR '> E
> e met od to calculate t e minimum amine o+ rate in ca#e of DE' #olution i#
# o+n in '%%endi 1
> e main outcome# are #ummari8ed in t e follo+ing ta le;
,able ?: amine Ko@ rate calculation
Parameter !ctual Processsc;eme
MM 1=
Xa 41 W 0 =6/1 U0 1
^ * =B
M) 0 !
G> !0
DE! recirculation rateUSGPM 2 !
DE! recirculation ratem ( $; 0
$or amine #olution# +it DE'9 t e minimum ca%acit5 of lean amine circulation
%um%# for t e actual %roce## #c eme # all e over t an 0 m!/
#ing t e c emical reaction9 to eliminate t e acid ga# t e amine molar o+ # all e
t+ice of t e CO 2 o+ rate9 in t i# ca#e t e DE' circulation rate i# eAual to #*49
m ! / u#ing a correction factor of 10
, 2 & "7 "N. O $CO2'/& OR /ER
> e met od for calculating t e diameter of t e a #or%tion column i# # o+n in
'%%endi 2
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: %6 $ 6(
> e main de#ign data are illu#trated in t e follo+ing ta le;
,able #*: C'% !bsorber Design Data
Parameter# Falue
Gas processed Ko@rate MMSCFD #6Gas processed Ko@rate
MMSCMD*49+(
Contactor pressure Paa (%**
Contactor diameter m *4?6%
> e main (Y&Y& #imulation re#ult# for t e CO 2 a #or er are illu#trated in t e
follo+ing ta le;
,able ##: C'% !bsorber Main Si ing "esults
Parameter# Falue
Gas processed Ko@rate MMSCFD #+4?+
Contactor pressure bara (%
/umber of stages #*
!bsorber diameter m *4 6%
Section ;eig;t m 64#
,ray spacing m *46#
!mine solution li>uid 8olume Ko@ m ( $;
#*49
Mol L C' % inlet contactor #4 %
Mol L C' % outlet contactor *4(*9
Con#idering t e a ove calculation re#ult#9 t e #i8ing re#ult# of t e +or#t ca#e are
con#idered;
,able #%: "esults of si ing of absorption column
De#ign Parameter Falue
Diameter of column 4m6 0 B 2(eig t of column 4m6 1
Num er of %late# 10
, ! ' M"NE R E.ENER '>O R
> e met od for calculating t e diameter of t e regeneration column i# # o+n in
'%%endi !
>ac3ing in con#ideration t e de#ign ca%acit5 of t e recirculation %um% of #*49m ! / t e minimum diameter of t e amine regenerator column # ould e of =1 2
mm
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: % $ 6(
> e main (Y&Y& #imulation re#ult# for t e 'mine regenerator are illu#trated in t e
follo+ing ta le;
,able #(: !mine "egenerator Main Si ing "esults
Parameter# Falue
amine processed 8olume Ko@ m ( $; #*49Fraction of C'% in reac; amine outlet
absorber mol L#46%
"egenerator pressure bara #4+
/umber of stages #*
"egenerator diameter m *46*?
Section ;eig;t m 64#
"eboiler duty MMB,U$; 94+%?Fraction of C'% outlet regenerator mol L *4%
Con#idering t e a ove calculation re#ult#9 t e #i8ing re#ult# of t e +or#t ca#e are
con#idered;
,able #9: "esults of si ing of regenerator column
De#ign Parameter Falue
Diameter of column 4m6 0 1
(eig t of column 4m6 1Num er of %late# 10
, , ) E'N 'M "N E C"RC ) '> "O N PMP &
> e data of lean amine circulation %um%# are #ummari8ed in t e follo+ing ta le;
,able #+ : Data for lean amine circulation pumps calculation
De#ign Parameter nit Falue
Folume o+ for t e amine #olution# m ! / #*49&uction %re##ure ara 1 ,
Di#c arge %re##ure ara !2 2
Fa%or %re##ure ara 0 ,!
Ma## den#it5 Lg/m ! 100B
&i8ing re#ult# are # o+n in t e ta le given ello+;
,able #6: 2ean amine circulation pumps main design parameters
De#ign Parameter# nit Falue(5draulic %o+er 3G * 21,
Electrical %o+er 3G 1,
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: %< $ 6(
De#ign Parameter# nit Falue
(M> mCE !02
, * &"7 "N . O$ (E '> E XC ('N. ER
, * 1 & "7 "N. O $)E'N 'M "N E '"R COO)E R
> e #i8ing of t e lean amine air cooler i# %erformed u#ing t e #oft+are (>$&
> e data of lean amine air cooler are #ummari8ed in t e follo+ing ta le;
,able # : Calculation data of lean amine air cooler
Design Parameter Unit 3alue
>em%erature of amine #olution inlet aircooler C *0
>em%erature of amine #olution outlet aircooler C ,0
'mine #olution o+ rate Lg/ B 2! 1
'ir cooler inlet %re##ure ar !2 2
&i8ing re#ult# are mentioned in t e ta le given ello+;
,able #u e# %er undle - 9+>u e %a##e# - 9
'rea reAuired m 2 9+
>u e lengt m ?4 9
&ee >EM' # eet of amine air cooler in a%%endi
, * 2 & "7 "N. O $R"C(/)E' N' M"NE (E'> EXC( 'N .ER
> e #i8ing of t e ric /lean amine eat e c anger i# %erformed u#ing t e #oft+are(>$&
> e data of ric / lean amine eat e c anger are #ummari8ed in t e follo+ing ta le;
,able #?: Calculation data of lean$ric; amine ;eat e c;anger
Design Parameter Unit 3alue
>em%erature of ric amine inlet eat e c anger C ,0 2=>em%erature of ric amine outlet eate c anger C =
>em%erature of lean amine inlet eat e c anger C 112
Ric amine o+ rate Lg/ 100== 2
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: %? $ 6(
Design Parameter Unit 3alue
lean amine o+ rate Lg/ B 2! 1
(eat e c anger inlet %re##ure ar 9
&i8ing re#ult# are mentioned in t e ta le given ello+;
,able %*: Calculation results of lean$ric; amine ;eat e c;anger
De#ign Parameter nit Falue
>u e %a##e# - %
'rea reAuired m 2 4#
>u e lengt m (4*9EM' # eet of ric / lean amine eat e c anger in a%%endi
, * ! & "7 "N. O $R E.E NE R'>O RCONDEN &ER
> e data of conden#er are #ummari8ed in t e follo+ing ta le;
,able %#: Design parameters of amine condenser
De#ign Parameter# Unit Falue
,emperature inlet condenser HC ??4+
,emperature outlet condenser HC 6*
Condenser inlet pressure bar #4%
Ko@ rate g$; #+%+4#%
1eat duty MMbtu$;r %4%6
, * , & "7 "N. O $R E.E NE R'>O RR E/O")E R
> e data of Regenerator Re oiler are #ummari8ed in t e follo+ing ta le
,able %%: "eboiler main design parameters
De#ign Parameter# Unit Falue,emperature inlet "eboiler HC ##%4+
Ko@ rate g$; ##+?
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: (* $ 6(
De#ign Parameter# nit "nlet ve##el )iAuid outlet .a# outlet
Ma## o+ rate 3g/ B 1 0* B 1 , == *
Folumetric o+ rate m ! / 11 2! 1 * B !
Pre##ure ara ! ! !>em%erature C ,0 ,0 ,0
Ma## den#it5 3g/m ! 10*, 1 =B!
> e re#ult# of #i8ing are #ummari8ed in t e follo+ing ta le;
,able %9: !mine Kas; drum si ing results
De#ign Parameter nit FalueDiameter m 0 =
)engt m ! !
+4 "E3.S.'/ 'F ,EG U/., DES.G/
= 1REF"&"ON O$ >E. CON>'C>OR DE&".N
Using GPS! standard
> e revie+ of t e >E. contactor i# %erformed u#ing t e .P&' #tandard9 t e
calculation %rocedure# are attac ed in '%%endi ,
> e integral #cru er i# alread5 modeled a# %er t e actual %roce## #c eme
> e ta le elo+ # o+# integral #cru er dimen#ion#;
,able %+: integral scrubber dimensions
Parameter Unit 3alue
Diameter m 0 B1,,
(eig t m 2 2*
> e follo+ing data are con#idered for contactor #i8ing;
,able %6: Glycol contactor .nput parameters
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: (# $ 6(
Parameter 3alueContactor o%erating %re##ure4 ara6 !0
.a# den#it5 43g/m!6 2! =)iAuid den#it5 43g/m!6 110
.a# o+ rate 4&m!/ 6 1* !0
> e main re#ult# are #ummari#ed in t e follo+ing ta le;
,able % : Glycol contactor Main "esults
Parameter 3alue
> e +ater content inlet contractor4mg/&m ! 6 2*!= 1B
> e +ater content outletcontractor 4mg/&m ! 6 1!! B!
Gater removal 43g/ 6 =0 !2
.l5col o+rate 4m ! / r6 0 *
Diameter 4m6 0 *,
Num er of tra5# *
>ra5 #%acing 4m6 0 1
' #or er eig t 4m6 , **
Using 1JSJS simulation
' (Y&Y& #imulation %erformed to model t e actual contactor > 10 including it#
diameter9 internal# 4 u le ca% tra5#6 e#timate t e >E. contactor #i8e con#idering
t e follo+ing in%ut data;
,able %
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: (% $ 6(
Parameter 3alue
Contactor %re##ure 4 ara6 !0.a# >em%erature inletcontactor 4 C6 ,=Ma imum .l5col o+rate4m! / r6 0 *
.a# %roce##ed o+rate4MM&C$D6 1=
' #or er diameter 4m6 0 B1,
>ra5# t5%e u le Ca%>ra5#Num er of tra5# *
&ection eig t 4m6 , *
>ra5 #%acing 4m6 0 1
> e main &imulation re#ult# are # o+n in t e follo+ing ta le;
,able %?: Glycol contactor Main si ing "esults
Parameters 3alueGater content inlet contactor43g/ 6 =0 1
Gater content inlet contactor4%%m6 !2!= *Gater content outlet contactor43g/ 6 1 1
Gater content outlet contactor4%%m6 ###4(
> e +ater content do+n#tream t e .l5col contactor >- 10 i# 111 ! %%m9 "t doe#nJt
com%l5 +it &>E. reAuirement 4Gc *0 %%m69 for t i# rai#on a de#ign revie+ of
regeneration unit +it t e e %ected ga# o+ rate i# made availa le in ne t
%aragra%
= 2C RREN> >E. RE.ENER'>"ON N"> DE&".N
= 2 1 . )YCO )$) '&(>'NL OPE R'>"N. D'>' ' NDD "M EN& "O N&
> e data of .l5col a# drum are #ummari8ed in t e follo+ing ta le
,able (*: Glycol Kas; drum operating data
De#ign Parameter# nit "nlet ve##el )iAuid outlet .a# outlet
Ma## o+ rate 3g/ * ! * 0 ! Folumetric o+ rate m ! / ! B! 0 *1! 2 =
>em%erature C *0 *0 *0
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: (( $ 6(
De#ign Parameter# nit "nlet ve##el )iAuid outlet .a# outlet
Ma## den#it5 3g/m ! 2= = 10 0 1 1 *
> e dimen#ion# of .l5col a# drum are #ummari8ed in t e follo+ing ta le;
,able (#: Glycol Kas; drum dimensions
De#ign Parameter nit E i#ting FalueDiameter m 0 ,0
)engt m 1 =
= 2 2 ( E'> EXC( 'N.E R&" NP> D'>'
= 2 2 1 '"R/. )YCO )( E'> EXC( 'N .E RE!20
> e data of .l5col air cooler are #ummari8ed in t e follo+ing ta le
,able (%: Calculation data of Glycol air cooler
Design Parameter Unit 3alue
>em%erature of gl5col inlet air cooler C 1* ,
>em%erature of gl5col outlet air cooler C 1,0
.l5col o+ rate Lg/ *B B
'ir cooler inlet %re##ure ar 1 10!
Dut5 Btu$;r 120000
= 2 2 2 .)YCO)/. )YCO )(E'> EXC( 'N .ER
> e data of ric gl5col/lean gl5col eat e c anger are #ummari8ed in t e follo+ingta le
,able ((: Calculation data of glycol$ glycol ;eat e c;anger
Design Parameter Unit 3alue>em%erature of lean gl5col inlet eate c anger C #??4em%erature of lean gl5col outlet eate c anger C #em%erature of ric gl5col inlet eate c anger C *
>em%erature of ric gl5col outlet eate c anger C
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: (9 $ 6(
,able (9:Glycol regen$Dry gas economi er ;eat e c;anger data
Design Parameter Unit 3alue>em%erature of gl5col regen inlet eat
e c angerC #(?
>em%erature of gl5col regen outlet eate c anger C +9
>em%erature of dr5 ga# inlet eat e c anger C 9em%erature of dr5 ga# outlet eat e c anger C +(49
eat e c anger inlet %re##ure ar (*4#
= ! .)YC O) PMP &
> e data of gl5col %um%# are #ummari8ed in t e follo+ing ta le;,able (+ : Data for Glycol pumps si ing
De#ign Parameter nit Falue
Folume o+ for t e gl5col .P( %#*
&uction %re##ure ara 1 1
Di#c arge %re##ure ara !0
&uction tem%erature C 1!*
Fa%or %re##ure ara 1 1*
Ma## den#it5 Lg/m ! 10*
= , CO NDEN&E RC O") EXC('N .E R
> e data of conden#er are #ummari8ed in t e follo+ing ta le;
,able (6: Main Design parameters of Glycol unit condenser
De#ign Parameter# Unit Falue
,ype 5 Coil e c;anger
1eat duty Btu$;r 9 %+*
= = RE .ENER '> OR RE/ O")ER
> e data of Regenerator Re oiler are #ummari8ed in t e follo+ing ta le
,able ( : "eboiler main design parameters
De#ign Parameter# Unit Falue
,ype 5 Fired ;eater e c;anger
1eat duty Btu$;r 9
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: (+ $ 6(
= ). &>R"PP "N . CO ) MN
> e lean gl5col do+n#tream t e re oiler %a##e# t roug t e )ean .l5col
&tri%%ing .a# Column t at contact# t e lean gl5col +it dr5 ga# from a# drum9furt er removing +ater from t e gl5col to t e ig er %uritie# reAuired 5 t i#
o%eration9 t e main de#ign data for t e ). #tri%%ing ga# are #ummari8ed in t e
follo+ing ta le;
,able (
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: (6 $ 6(
ig er +ater content in t e dr5 ga# #tream leaving t e contactor > e lo+er %urit5 i#
t e ig er dr5 ga# +ater content i#
> e ne t #te% i# to %erform t e regeneration %roce## trou le # outing a# long a#t e lean gl5col %urit5 i# lo+
t e follo+ing regeneration %arameter# a# to e revie+ed to im%rove regenerated
gl5col %urit5;
#tri%%ing ga# o+rate#tri%%ing ga# column de#ign#till column de#ign
= * RE.ENER'>"ON PROCE&& >RO )E &(O >"N.
= * 1 &> R "P P"N. .'&$) OG R '> E
+ en increa#ing #tri%%ing ga# o+rate feeding ). #tri%%ing column 9 it +ill
conden#e t e eavier com%onent 4 >E. 6 in t e #tream leaving re oiler #tage 9and
t e +ater va%our goe# ac3 to t e #till column and +ill e rejected from t e to%9 a#a re#ult t e regenerated gl5col %urit5 i# im%roved
> e %ro%o#ed #olution i# to add additional amount# of #tri%%ing ga# coming from
amine u# drum to t e e i#ting one coming from gl5col a# tan3
> e follo+ing %roce## #c eme # o+# t e gl5col %urit5 im%rovement 9 to ring it
from B 2 to B* = + en increa#ing #tri%%ing ga# o+rate
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: ( $ 6(
> e ne+ regenerated gl5col %urit5 B* = i# #+eet a le decrea#e t e dr5 ga# +ater
content from 111 ! %%m(2o to , , %%m(2o #o t at it meet# clo#el5 t e &>E.
reAuirement 4 *0 %%m(2o 6
> e follo+ing %roce## o+ #c eme # o+# t e main #imulation re#ult# u#ing t e
im%roved regenerated >E. %urit5
> e #tri%%ing ga# column diameter # all e revie+ed #ince t e feed ga# o+rateincrea#ed
= * 2 &> R "P P"N. .'&C O)M N DE&".N 4D "' ME >E R6
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: (< $ 6(
> e #tri%%ing ga# column diameter i# eing recalculated via (Y&Y& #oft+are 4 tra5
#i8ing utitlit5 69 t e actual #tri%%ing ga# diameter i# 0 2 m 9 and a# %er t e attac ed
#i8ing re#ult# t e diameter # ould e 0 ! m
> e follo+ing ta le # o+# t e reAuired #tri%%ing ga# column de#ign;
/ / 9:;S< S 1==TS 1
S< E > 3==TS 1
I < 9/ P ?
S< D ;< < $;% 0.3048
M @ F9 > $ % 8.45
+ S< 9 A < $;2%
7.2(7o icit5 No cla##i:eda8ard
&torage
Protect from#unlig t &tore ina +ell-ventilated
%lace
2P ROP'NE R ECE"FER
> e #i8ing of Pro%ane receiver drum i# determined 5 referring to #tandard DEP> e data of Pro%ane receiver drum are #ummari8ed in t e follo+ing ta le
,able 9#: Propane "ecei8er .nput Data
De#ign Parameter# nit "nlet ve##el )iAuid outlet .a# outlet
Ma## o+ rate 3g/ = ,1 0 =* = ,0
Folumetric o+ rate m ! / 2=1, 0 000B 2=1,
Pre##ure ara 1 0 1 0 1 0
>em%erature C -!B -!B -!B
Ma## den#it5 3g/m ! 2 ! =*= 2 !
> e re#ult# of #i8ing are #ummari8ed in t e follo+ing ta le;
,able 9%: Propane "ecei8er Main si ing Data
De#ign Parameter nit Falue
Diameter m 0 B*
(eig t m 2 2=
!P ROP'NE C OMPRE&&OR
> e main data reAuired for com%re##or #i8ing are a# follo+;
,able 9( : Stage # Main Data
Property 3alue
Gas Molecular &eig;t 994#
Compressibility Factor *4?
Gas Mass Flo@rate g$;r + 9#
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: 9* $ 6(
Property 3alue
Suction ,emperature HC 5(
Suction Pressure bara #4#
Disc;arge Pressure bara 94+
Duty & #9(
,able 99 : Stage % Main Data
Property 3alue
Gas Molecular &eig;t 994#
Compressibility Factor *4?(
Gas Mass Flo@rate g$;r + + e main data reAuired for t e #imulation are a# follo+;
,able 9+: Propane Condenser .nput Data
Parameter# "nlet Outlet
Pressure bara 1B 1* *
,emperature HC 10, =,
Flo@rate g$;r = =* = =*
> e re#ult# of #i8ing are #ummari8ed in t e follo+ing ta le;
,able 96: Propane Condenser Main si ing Data
De#ign Parameter nit Falue
(eat E c anged 3G (?#
=P ROP'NE E CONOM"7ER F@-,00!;
> e #i8ing of Pro%ane economi8er drum i# determined 5 referring to #tandard DEP> e data of Pro%ane economi8er drum are #ummari8ed in t e follo+ing ta le
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: 9# $ 6(
,able 9 : Propane Economi er .nput Data
De#ign Parameter# nit "nlet ve##el )iAuid outlet .a# outlet
Ma## o+ rate 3g/ = =* !!* 2! 1
Folumetric o+ rate m ! / 2!B 12 , 2!! 2Pre##ure ara , , ,
>em%erature C -0 , -0 , -0 ,
Ma## den#it5 3g/m ! 2, 0! =!0 1 10 1
> e re#ult# of #i8ing are #ummari8ed in t e follo+ing ta le;
,able 9 e #i8ing of t e .a#/Pro%ane i# %erformed u#ing t e #oft+are (>$& 4#ee
'%%endi *6
> e main #i8ing re#ult# of t i# eat e c anger are #ummari8ed in t e ta le elo+;
,able 9?: Gas$Propane E c;anger Main si ing Data
De#ign Parameter nit Falue
E c ange area m2 #?4+
(eat e c anged 3G % ?4?
>u e Num er - B2
& ell "D mm !!
)engt m ! =
. '& /. '& O >)E> C O)D &EP'R'>OR ( E'> E XC('N.ER E@-,001'
> e #i8ing of t e .a#/.a# Outlet cold #e%arator i# %erformed u#ing t e #oft+are
(>$& 4#ee '%%endi *6
> e main #i8ing re#ult# of t i# eat e c anger are #ummari8ed in t e ta le elo+;
,able +*: Gas$Gas 'utlet Cold Separator ;eat E c;anger Main si ing Data
De#ign Parameter nit Falue
E c ange area m2
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: 9% $ 6(
De#ign Parameter nit Falue
>u e Num er - !,
Num er of tu e %a##e# %er # ell - 2
& ell "D mm 1B! *
*. '& /) "V "D ( E'> E XC('N.ER E@-,002
> e #i8ing of t e .a#/)iAuid i# %erformed u#ing t e #oft+are (>$& 4#ee '%%endi
*6
> e main #i8ing re#ult# of t i# eat e c anger are #ummari8ed in t e ta le elo+;
,able +#: Gas$Propane E c;anger Main si ing Data
De#ign Parameter nit Falue
E c ange area m2 %49
(eat e c anged L+ 9*4u e Num er - !
Num er of tu e %a##e# %er # ell - 2
& ell "D mm 1B! *
)engt m 1 22
BC O)D &EP'R'>OR
> e #i8ing of cold #e%arator drum i# determined 5 referring to #tandard DEP> e data of cold #e%arator drum are #ummari8ed in t e follo+ing ta le
,able +%: Cold Separator .nput Data
De#ign Parameter# nit "nlet ve##el )iAuid outlet .a# outlet
Ma## o+ rate 3g/ +6#6 ##*+ 9+##
Folumetric o+ rate m ! / (*4+( (4%6 % 4%
Pre##ure ara
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: 99 $ 6(
' #en#itive #tud5 i# %erformed for di erent %i%eline diameter# 4, inc 9 inc 9 *
inc 9 10 inc and 12 inc 6 to #elect t e a%%ro%riate diameter for tran#ferring t e
treated ga# from t e E %lant to t e &>E. net+or3
&imulation 5%ot e#e# are %re#ented in follo+ing ta le;
,able +6: Simulation 1ypot;eses
Property 3alueDistance From t;e CPF to tie5in
point m%+
Ele8ation Di erence m
NestimatedO+
"e>uired Pressure in t;e tie5inpoint @it; S,EG /et@or bara
6
Pipeline "oug;ness mm *4*9+
,;ermal Conducti8ity &$m%4I 9+
Mean ons;ore ground
temperature HC%*
Gas Flo@rate mmscfd +4 %
> e re#ult# of t i# #imulation are # o+n in t e :gure# elo+;
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: 9+ $ 6(
Figure 6: Pressure Pro7le of gas e port pipeline
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: 96 $ 6(
Figure : 3elocity Pro7le of gas e port pipeline
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: 9 $ 6(
> e re#ult# of t i# #imulation for di erent %i%eline diameter are #ummari8ed elo+;
,able + : Pipeline calculation "esults
Diameter
4inc 6
.a# o+
rate
4MM&C$D6
Pre##ure
do+n#tre
am PCF
4 ara6
)oadingPre##ure
at tie-in
%oint
4 ara6
Felocit
5 4m/#6
Ma
velocit5
4m/#6
Pre##ure
dro%
4 ar/100
m6
Ma
%re##ure
dro%
4 ar/100m6
9 +
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: 9< $ 6(
Parameter ,reated Gas S,EGSpeci7cations
Pre##ure 4 arg6 = at tie in %oint
>em%erature 4 C6 20 10 - =0Molar o+ `MM&C$D = 0 , -(ig er eating Falue43cal/Nm ! 6 1090=
B!00 - 1022*
Go e "nde 43cal/Nm ! 6 129!B 11B 1 - 12 ,0
Ma## Den#it5 43g/m ! 6 ] >P *1 B -
Molecular Geig t 2* 01 -
Gater content 4%%m6 , , *0
CO 2 content 4 mol6 0 ! 0 =
( 2& content 4mg/Nm ! 6 0 2
( 2 and N 2 content 4 mol6 =
O2 content 4 mol6 0 0
> e follo+ing ta le # o+# recovered conden#ate #%eci:cation ;,able +?: Condensate speci7cation
Property 3alue 'ctual volume o+ 4 arrel/da56 ]
=0 C/1'tm*0* =
>rue FP 4 ara6 ] ! * C 0 2 BReid FP 4 ara6 ] ! * C 0 0==
Ma## Den#it5 43g/m ! 6 *, 1
Fi#co#it5 4cP6 0 !B*1
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: 9? $ 6(
#*4 !PPE/D.CES
10 1 'PPEND"X 1 ; REC"RC )'>"ON R'>E O$ DE' &O) >"ON
"n ca#e of u#ing t e DE' #olution t e recirculation rate i# calculated 5 t e follo+ing;
L DEA =192 MMX a
WT ML
G ere;
)DE'; DE' #olution minimum recirculation rate 4 &.PM6
MM ; ga# o+ MM&C$D
G> ; amine #olution +eig t %ercent circulated
M) ; mol loading9 mole# acid ga#/mole
Xa ; reAuired reduction in total acid ga# fraction
^ ; &olution den#it5 4l /gal6
10 2 'PPEND"X 2; 'M"NE CON>'C>OR D"'ME>ER C')C )'>"ON
> e amine contactor column diameter i# determined referring to t e given correlation;
Dc= 10750 Q PG ere;
Dc U Contactor diameter in mm
P U Contactor %re##ureV U ga# %roce##ed o+ rate
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: +* $ 6(
10 ! 'PPEND"X !; 'M"NE RE.ENER'>OR D"'ME>ER C')C )'>"ON
> e column diameter i# determined u#ing t e given correlation
Dr=
160 L
G ere;
) U 'mine circulation rate 4m ! / 6 U i# t e de#ign ca%acit5 of t e lean amine
circulation %um% !!0-P'-001'/
Dr U Regenerator diameter in mm
10 , 'PPEND"X ,; .P&' &>'ND'RD $OR >E. CON>'C>OR &"7"N.
> e Auantit5 of +ater t at # all e removed i#;
W r = W i W o 4mg +ater/&m ! +et ga#6
> e +ater content of #+eet ga# re#%ectivel5 inlet and outlet contractor can e
calculated u#ing L'CEL correlation;
W i= A1 P
+ B1
W o= A2 P
+ B2Git ;
P; > e o%erating %re##ure at t e >E. contactor 4 ara6
A1 9 A2 , B1 9 B 2 ; con#tant at t e o%erating tem%erature #ing t e LREM&ER
ROGN art9 +e can de:ne t e a #or%tion ratio 4' rU! =6.iven t i# ratio t e lean gl5col o+ rate can e determined u#ing t i# correlation;
Q TEG = W o
( E 1 1 ) Ar mg 4mg/ 6
Git ;
E; E icienc5 of t e a #or er
G O ; G ater content ou tlet contractor 4mg/&m!6
mg ; .a# o+ rate 4&m!/ 6
>o calculate t e contactor diameter9 t e follo+ing correlation can e u#ed;
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: +# $ 6(
G= C ( g ( l g))0.5
$? ,;H. %
g ; .a# den#it5 43g/m ! 6
l ; )iAuid den#it5 43g/m ! 6
> e contactor #ection can e calculated 5 t e follo+ing eAuation;
S=mgG
Git ;
mg ; .a# o+ rate 43g/ 6
> e contactor diameter can e calculated 5 t e follo+ing eAuation;
D= 4 S (m)10 = 'PPEND"X =; NOR&OL &>'ND'RD $OR &"7"N. O$ .'& )"NE
"n line# + ere %re##ure dro% i# not critical9 ga# velocit5 # all not e ceed limit# + ic ma5
create noi#e or vi ration# %ro lem# '# a rule of t um t e velocit5 # ould e 3e%t elo+;
V = 175 ( 1 )0.43
G ere;
F ; > e ma imum velocit5 of ga# to avoid noi#e in m/#
^ ; > e den#it5 of ga# in 3g/m!
or 0 m/#9 + ic ever i# ever t e lo+e#r
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: +% $ 6(
10 'PPEND"X ; 'M"NE N"> (E'> EXC('N.ER& >EM' &(EE>& Rich / Lean Amine heat exchanger
002/'R11/12 0,/10
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: +( $ 6(
Amine Air cooler
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: +9 $ 6(
10 'PPEND"X ; .)YCO) N"> (E'> EXC('N.ER& >EM' &(EE>&
002/'R11/12 0,/10
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: ++ $ 6(
Gas/glycol heat exchanger
Gas/glycol heat exchanger
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: +6 $ 6(
glycol/ glycol heat exchanger heat exchanger
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: + $ 6(
002/'R11/12 0,/10
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: +< $ 6(
10 * 'PPEND"X *; C("))"N. N"> (E'> EXC('N.ER& >EM' &(EE>& Gas/Propane EJ-4003 E!A "heet
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: +? $ 6(
Gas/Gas #$tlet col% separator EJ-400&A E!A "heet
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: 6* $ 6(
Gas/li'$i% EJ-400 E!A "heet
002/'R11/12 0,/10
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7/24/2019 ECUMED Sizing Report for the First Phase Rev_0 MCH (Rpar) (2)
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: 6# $ 6(
Air-Cooled Heat Exchanger Specification Sheet ( condenser -chilling unit )
10 B 'PPEND"X B; &>R"PP"N. .'& CO) MN DE&".N
002/'R11/12 0,/10
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7/24/2019 ECUMED Sizing Report for the First Phase Rev_0 MCH (Rpar) (2)
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!", /'4"E34 *P!GE: 6% $ 6(
LIQUID !"#ILE (#!"$ %!A&)
1__TS-1 2__TS-1 3__TS-1
Mass Flow (kg/h) 922.6 918.8 912.1
Liquid Flow (m3/s) 2.6 1!-""# 2.63#!-""# 2.6"$!-""#
Mol!%ula& '!igh 1##." 1# .8 1#$.2
T!m !&a u&! (*) 2"".9 199.# 19$."
+!,si (kg/m3) 966.9 968.9 9$1.8
is%osi (% ) ". 99# ".6"$2 ".62#6
Su&0a%! T!,sio,(d ,!/%m)
29.3$ 29.#9 29.$"
'A "U! !"#ILE (%" %!A&)
1__TS-1 2__TS-1 3__TS-1
Mass Flow (kg/h) 1$.$9 13.96 $.21
as Flow ( *T_m3/h) 2".#$ 1 .$8 8.#6"
Mol!%ula& '!igh 32.1# 31.2$ 21.18
T!m !&a u&! (*) 199.# 19$." $.2
+!,si (kg/m3) ".8691 ".88#9 ".8 28
is%osi (% ) 1.61 !-""2 1.69 !-""2 1.212!-""2
Fluid &!ssu&! ( a&) 1."1# 1." 8 1.1"3
002/'R11/12 0,/10
%ra Si ing* stripping gas colu+n si ing ( dia+ater)
SE%U
T&a S!% io,4 TS-1 5* L Liquid +&aw4 "."" 7
S!% io,_1
S!% io, S a& 1__TS-1
S!% io, ,d 3__TS-1
, !&,als a%k!d
Mod! +!sig,
% i:! 00
S a us *om l! !
+!sig, Limi *ha,!lli,g
Limi i,g S ag! 1__TS-1
,%lud! a o& ;!ad 00
S ECI#ICA%I",S
S!% io,_1S!% io, S a& 1__TS-1
S!% io, ,d 3__TS-1
, !&,als a%k!d
Mod! +!sig,
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E-U.PME/,S S.0./G "EP'", F'" ,1E F."S, P!",/'4"E34 *P!GE: 6( $ 6(
10 10 >"E-"N PROCED RE >O 'DD 'M"NE $)'&( F'POR >O &>R"PP"N. .'&
PROCE&&
Plea#e refer to t e %i%ing and in#trumentation diagram entitled PROCE&& $)OG
.)YCO) DE(YDR'>"ON
P'CL'.E 9 document No R02-0 -DG.-PR-00-00,
> e >ie in %oint i# located do+n#tream of t e E&DF-,10 valave and t e u%#tream of
t e valve NE- 00* 4 t e line in + ic mounted a re#triction ori:ce RO-,106
> e i#olation +or3 i# guaranteed 5 clo#ing 9 t e E&DF-,10 and valve NE- 00*