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HTTEKPVGAS

CAMAU GPMB

PROJECT: UPDATING FEASIBILITY STUDY FOR CAMAU GPP

LOCATION: CA MAU PROVINCE

CLIENT: PVGAS CAMAU GAS PROCESSING PLANT MANAGEMENT BOARD

STAGE: FEASIBILITY STUDY

PROCESS DESIGN CRITERIA

DISTIBUTION

Company !"y

PVGAS

CM GPMB

HTTEK

Process x

Control

Electrical

Fire Fighting x

Pipeline x

Piping x

Civil

Mechanical x

To"a#:

PVGAS $ CM GPMB

(APPD.)

A 03/0/!0"# $ss%e& 'or evie *.D.+ D.+.D *.+., *.+.,

R%& Da"% D%'()*p"*on By C+%(, E-M HTTEK

HUNG THINH

CONSULTANCY AND TECHNICAL SERVICE J-S-CA..-- ""/" Phan ,% $ch 1tr.2 ar& "2 +anBinh Dis.2 ,CMCP+on%: 0 4! "4 5 Fa/: 0 4! "4 #Ema*#: in'o6htte7.co8.vn5 e9- http//-.htte7.co8.vn

Do(- No-:

U$00012$PR$CRT$0003

45Pa6%'($ncl. this page)
mailto:[email protected]:[email protected]

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PE+:;$E+*AM GA1 GA1 P:CE11$*G P?A*+ P:PDA+$*G FEA11$B$?$+@ 1+>D@ F: GA1 P:CE11$*G P?A*+ P: #et Positive Suction .ead >e+uired

#P #et Present alue#> #on >eturn alve

P/.& Printed /ircuit .eat &'c!aner

P# Petroietna

PS Pressure Safety alve

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(&+uation D*E*)

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PE+:;$E+*AM GA1 GA1 P:CE11$*G P?A*+ P:PDA+$*G FEA11$B$?$+@ 1+>D@ F: GA1 P:CE11$*G P?A*+ P:efer also to ables D*E-2 and D*E-3 for level settins to be used for verticaland !oriontal se"arators, res"ectively*

Co)u(ns

D*2*E Floodin Factor

!e ter 6Flood Factor7 is used for "ur"oses of estiatin t!e iniuactive area and iniu down coer area* !is ter is t!e 6desin "ercentof flood7* A value of not ore t!at KK is norally used for vacuu towersand a value of not ore t!an 82 is used for ot!er services* !ese valuesare intended to liit entrainent to a""ro'iately E0* .i!er flood factorsay result in e'cessive entrainent andJor a colun sied too sall foreffective o"eration*

!e 6actual "ercent of flood7 s!ould be deterined once t!e final tray desin!as been co"leted and s!ould be in t!e rane of KD to 8D "ercent, ata'iu desin rates* !ese values ay vary, !owever, de"endin on t!e"articular a""lication*

D*2*2 iniu and a'iu a"our elocity /riteria

!is section contains uidelines for +uicly c!ecin a vendorRs desin forvalve trays*

!e a'iu slot velocity in feet "er second can be deterined fro t!efollowin e+uation5

)Density(

15max

VapourV = (&+uation D*2*E)

!e iniu slot velocity in feet "er second can be deterined fro t!e

followin e+uation5

)Density(

5.6max

VapourV = (&+uation D*2*E)

a"our density O lbsJcu*ft

!e iniu slot velocity calculation is based on iniu va"our flow andt!e area of t!e o"enin around t!e valve "eri"!ery (fully o"ened)* As a rule,t!e slot area for Boc! and $litsc! valves is e+ual to a""ro'iately 0*0E2 s+*ft* "er valve but t!is s!ould be c!eced wit! t!e vendor "articularly for #utterrays*

W!ere different wei!ted valves are s"ecified for a sinle dec, t!e iniuvelocity s!ould be tested for t!e iniu va"our flow usin t!e slot area for

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PE+:;$E+*AM GA1 GA1 P:CE11$*G P?A*+ P:PDA+$*G FEA11$B$?$+@ 1+>D@ F: GA1 P:CE11$*G P?A*+ P:eflu' "u"s s!all !ave a desin arin of 20*

#o desin arin is a""lied to "u"s in interittent or non-critical services*

D*3*2 4esin 4uty

#oral and rated flows will be identical in t!e followin services5

:nterittent service "u"s, e** su" "u"s, transfer "u"s*

W!en t!e "u" !as been overrated to allow a centrifual ty"e to be

s"ecified and if overratin is E0*

>e-circulation flow suc! as t!rou! a carbon filter*

!e siin of t!e "u" driver will be based on t!e res"ective desin duty t!atre+uires a'iu absorbed "ower, as deterined fro t!e .@S@Ssiulation* An efficiency of I0 will be assued for centrifual "u"s andKD for "ositive dis"laceent ty"e*

D*3*3 Selection ; Siin

/entrifual ty"e "u"s s!all be t!e default selection, unless t!e re+uireddifferential "ressure andJor flow ca"acity are outside t!e noral duty ranefor t!is ty"e of "u"*

D*3* #et Positive Suction .ead

For centrifual "u"s, t!e #PS.A ust e'ceed #PS.> by a arin of atleast E* W!ere layout constraints "revent settin t!e suction vessel at anelevation sufficient to ac!ieve t!e re+uired E #PS.A arin alternativesay be considered, suc! as "rovision of barrel (can) ty"e "u" andboosterJain confiurations*

W!ere flow conditions necessitate turndown to less t!an 30 of rated flowfor centrifual "u"s, iniu flow "rovisions s!all be ade* iniu flow

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PE+:;$E+*AM GA1 GA1 P:CE11$*G P?A*+ P:PDA+$*G FEA11$B$?$+@ 1+>D@ F: GA1 P:CE11$*G P?A*+ P: at inlet suction of t!e "u"* For suc! a""lications, an #PS.A of at leastK is norally recoended* .ence, if t!e suction vessel "ressure is nearsaturated va"our "ressure of t!e li+uid and, layout constraints "revent settint!e suction vessel at sufficient elevation to ac!ieve t!e re+uired #PS.A, itay be necessary to install a booster "u" u"strea of t!e ain "u"*

Co(pressors + &panders

D**E 4esin arin

#o standard desin arin will be a""lied to t!e flow rates or !ead ofco"ressors* /a"acity re+uireent for co"ressors in t!e "rocess syste

are norally based on a careful review of "roduction "rofile and ot!er"rocess re+uireents* #orally arins will be available in drives selected*:n any case careful consideration s!all be iven w!en selectin co"ressors"ecs and drives to ensure ca"acity re+uireents are et*

D**2 4esin 4uty

!e siin of t!e co"ressor driver will be based on t!e res"ective desinduty t!at re+uires a'iu absorbed "ower, as deterined fro t!e .@S@Ssiulation for an assued adiabatic efficiency of KD* An adiabatic efficiencyof KD will also be used for turbo e'"anders*

D**3 Selection ; SiinSiin and selection for co"ressors and e'"anders will be by vendor durinF&&4 "!ase*

"eat &c/an-ers

D*D*E 4esin arins

For Air coolers E0 desin arin will be considered on t!e re+uiredsurface* For s!ell and tube e'c!aners E0 desin arin will beconsidered on t!e re+uired surface area*

D*D*2 4esin 4uty

Flow rates corres"ondin to t!e desin a'iu !eat duty are s"ecified forsiin* :f t!is is not t!e a'iu flow rate, t!e a'iu flow rate s!ould beused to deterine t!e "ressure dro" t!rou! t!e e'c!aner* Additionally,w!ere a fluid !as a !i! "our "oint or !i! viscosity, it is andatory to c!ect!e e'c!aner siin for t!e duty corres"ondin to iniu flow rate case*

D*D*3 Selection ; Siin

!e ty"e of e'c!aner will be selected based on t!e ty"e of service andre+uired desin te"erature and "ressure*

Air coolers will be selected for coolin and condensin duties w!ere t!e

re+uired "rocess side outlet te"erature not less t!an Do/* Siin for aircoolers will be conducted usin A/9% co"uter software fro As"entec!*

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D*D* A""roac! e"erature

!e followin iniu a""roac! te"eratures are recoended for t!edesin of !eat e'c!aners5

S!ell and ube e'c!aners E0M/

Printed /ircuit e'c!aners (P/.&) 3M/

Plate .eat e'c!aners DM/

Air /oolers E0M/

Bettle >eboiler 3M/

!e desin air te"eratures for air coolers s!all be taen as 3DM/ a'*4esin !uidity s!all be E00 *

D*D*D Fluid >outin Arraneents

!e rules included !ere are for uidance only and s!ould not be consideredinfle'ible* !e eneral order of "riority to establis! t!e tubeside fluid is listedbelow5

a) A corrosive fluid or a fluid liely to de"osit coe, sedient or ot!ersolids suc! as catalyst*

b) !e !i!er foulin fluid*

c) !e less viscous of t!e two fluids, w!ere lare differences e'ist*

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!e total nuber of s!ells necessary for an e'c!aner is fre+uentlydeterined fro te"erature correction considerations* W!en t!ere is ate"erature cross between two fluids, two or ore s!ells (wit! ulti-"assbundles) ay be re+uired* 9t!erwise t!e nuber of s!ells de"ends on t!etotal surface re+uired and on t!e a'iu allowable bundle sie s"ecifiedby t!e client*

!e bundle sie (s!ell :*4*) is usually liited to a a'iu of I0 inc!es(ED2 ) because of aintenance considerations* :f t!e a'iu bundlesie is e'ceeded ulti"le saller e'c!aners ay be arraned in series or"arallel*

Series or Parallel Arraneents

W!ere "ossible, all 6s!ells7 (or as any as "ossible) s!ould be connected forseries flow because of t!e advantae in t!e 4 correction factor and aore econoical "i"in arraneent*

A reason for arranin s!ells in "arallel is to avoid e'ceedin allowable"ressure dro" values* Parallel arraneents are fre+uently re+uired wit!va"ours (seldo wit! li+uids) as in over!ead condensers* :t is desirable toliit t!e nuber of "arallel streas in order to avoid distribution "robles*!e followin et!ods ay be used to reduce t!e nuber of "arallel streas

to a iniu wit!out e'ceedin t!e allowable "ressure dro" w!en t!e fluid ison t!e s!ell side5

i) ?se of wide "itc! for baffles or su""ort "lates*

ii) ?se of double seental baffles*

iii) ?se of 6s"lit flow7 s!ells (&A or T ty"e)*

Stacin or Side by Side

W!en an e'c!aner service consists of a nuber of s!ell and tube units inseries, t!e s!ells are usually staced* :n eneral, stacin results in savinsin "i"in as well as "lot s"ace*

S!ells ay be staced a a'iu of two !i! alt!ou! for s!ells under 27


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PE+:;$E+*AM GA1 GA1 P:CE11$*G P?A*+ P:PDA+$*G FEA11$B$?$+@ 1+>D@ F: GA1 P:CE11$*G P?A*+ P:elievin 4evices in >efineries, Sevent! &dition, anuary 2000*

3* AP: >P D20 Part ::, Siin, Selection and :nstallation ofPressure->elievin 4evices in >efineries, Fift! &dition, Auust 2003*

* AP: SA#4A>4 D2E, Pressure->elievin and 4e"ressurinSystes, Fift! &dition, anuary 200K*

D* AP: SA#4A>4 2000, entin Atos"!eric and %owPressure Storae ans, Fift! &dition, A"ril ENN8*

I* AP: SA#4A>4 IE0, /entrifual Pu"s for Petroleu,Petroc!eical and #atural $as :ndustries , E0t! &dition, 9ctober 200

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2;31- #*n% '**n6 -----------------------------------------------------------------------------------------------2532- CONCLUSION ----------------------------------------------------------------------------------------25

3;- app%n.*(%'----------------------------------------------------------------------------------------------2

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+he content2 re'erences2 attach8ents an& an s%pple8entar in'or8ation 'orall engineering &oc%8ents shall 9e in English.>nits o' 8eas%re8ent 'or all engineering &oc%8ents shall 9e in the 1ste8$nternational (1$).

;-4 D%>*n*"*on' an. A)%&*a"*on'

4-4-3 D%>*n*"*on'

P:

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+P;* ;ietna8ese 1tan&ar&

;-1 Co.%' an. S"an.a).'

+he Fire Fighting 1ste8s shall 9e &esigne& generall in accor&ance ith 9%tnot li8ite& the 'olloing Co&es an& 1tan&ar&s P%9lishe& 9 the *ational FireProtection Association (*FPA) an& c%rrent ;ietna8ese Co&es an& 1tan&ar&s

Vietnamese standards:

+C;* !4!!- " Fire prevention an& protection 'or 9%il&ings str%ct%res Design re%ire8ents

+C;* 3!#- " Fire 1a'et General e%ire8ents

+C;* 3!- "4 Explosion 1a'et General e%ire8ents

+C;* 30- !00 Petrole%8 an& petrole%8 pro&%cts ter8inal Designre%ire8ents

+C;* 30- !00 Fire protection e%ip8ents 'or 9%il&ing an&constr%ction Provi&ing2 installation2 inspection2

8aintenance+C;* 4#- !003 Fire sa'et 'or petrole%8 an& petrole%8 pro&%cts

'acilities. General re%ire8ents

+C;* #3"-!00# Fire Protection. Porta9le an& heele& 'ireexting%isher. Part $ - 1election an& $nstallation

+C;* 40 - "3 Fire Exting%ishing 1ste8 General e%ire8ents o'Proect $nstallation An& >tilie

+C;* 4#4 - !00 ?i%e'ie& Petrole%8 Gas (?PG) Press%rie&1torage ?ocation2 Design2 Capacit an&$nstallation

"/!00"/++?+B+MBCA

eg%lation o' 'ire exting%ishers 'ire'ightinge%ip8ent in 1tores Petrole%8 An& Petrole%8Pro&%ct

International Standards:

*FPA "0 Porta9le Fire Exting%ishers

*FPA "" ?o expansion 'oa8 an& co89ine& agent sste8s

*FPA "#1tan&ar& 'or the $nstallation o' 1tan&pipes an& ,ose1ste8s

*FPA " 1tan&ar& 'or ater 1pra Fixe& 1ste8s 'or FireProtection


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PE+:;$E+*AM GA1 GA1 P:CE11$*G P?A*+ P:PDA+$*G FEA11$B$?$+@ 1+>D@ F: GA1 P:CE11$*G P?A*+ P:tilit Area A $$

"4 FI "4 1l%g Catcher Area A $" FI " :''spec B%llet Area A $

" FI " ?PG storage tan7 Area A $

" FI " Con&ensate storage tan7 A $

!0 FI !0 Process Area $B? A $

!" FI !" Process Area $B? A $

!! FI !! Process Area $B? A $


!# FI !# Process Area $B? A $

! FI ! Process Area $B? A $





30 FI 30 Process Area $B? A $

3" FI 3" Process Area $B? A $

3! FI 3! ?a9orator D $$

33 FI 33 G%ar& ,o%se " D $$

3# FI 3# G%ar& ,o%se ! D $$

3 FI 3 Diesel 1torage +an7 Area A $

34 FI 34 A8ine 1torage +an7 Area A $

Fireater &e8an& at the respective one is 9ase& on provi&ing s%''icient

coverage 'or 'ire exting%ish8ent2 expos%re protection an& 8itigatingescalation e''ect5

Maxi8%8 ater velocit ill 9e li8ite& to #. 8/s. Fire ater lines ill 9e

lai& %n&ergro%n&. +he %n&ergro%n& piping 8aterial shall 9e car9on steel2coate& an& rappe& ith catholic protection5

1iing o' the 'ireater p%8ps sho%l& ens%re that the are capa9le o'

s%ppling the re%ire& 'lo an& 8eeting the press%re re%ire8ent5

+he 8ain approach 'or e%ip8ent cooling protection is to %se 'ire 8onitor

or 'ire h&rant or co89ination thereo' in lie% o' ater spra sste8 as perthe 1a'et an& Fire Fighting Design Philosoph2 Doc no. *C1!+PGMFD300"0P,00"5

Fireater spra shall 9e provi&e& 'or the ?PG spheres an& h&rocar9on

containing e%ip8ent that cannot 9e reache& 9 'ire 8onitors an&h&rants5

A 30J contingenc has 9een incl%&e& into the act%al &e8an& o' &el%ge2

ta7ing into consi&eration o' overspra2 h&ra%lic i89alances2 preli8inaran& esti8ate& &i8ensions o' e%ip8ent2 location o' e%ip8ent et to 9e'inalie&5

For 9%il&ings locate& in each 'ire one2 the re%ire& 'ireater &e8an& ill

9e 9ase& on " hose strea8 'ire h&rant an& ! in&oor 'ire h&rant hose

strea8s.


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Con&ensate storage tan7 /Diesel storage tan7

(ater rate)30 l/8in/8

+C;* 30- !002 1ection.."4

Con&ensate storage tan7 /Diesel storage tan7

(Foa8 rate)"! l/8in/8!5#." l/8in/8!

+C;* 30- !002 1ection..""+C;* 30-!002 1ection.."0.!

?PG sphere / B%llet(ater rate)"0.! l/8in/8!

*FPA "2 1ection .#.!."

eactor/;essel(ater rate)"0.! l/8in/8!

*FPA "2 1ection .#.!."

P%8p/Co8pressor(ater rate)!0.# l/8in/8!

*FPA "2 1ection .3.!

:''ice B%il&ing/Fire 1tation /?a9orator B%il&ing

(1prin7ler &ensit)#.0 l/8in/8!

+C;* 3342 1ection 4.#ta9le !

areho%se/or7shop

(1prin7ler &ensit).!0 l/8in/8!

+C;* 3342 1ection 4.#ta9le !

+he 8ini8%8 operating press%re at ater spra noles is ".# 9arg as

per *FPA ".

1prin7ler sste8s ill 9e re%ire& 'or the :''ice 9%il&ing2 areho%se2

or7shop2 ?a9orator an& Fire 1tation.

Fireater tan7 is &esigne& 'or 3 ho%rs o' %ninterr%pte& ater s%ppl at the

8axi8%8 re%ire& rate as per +C;* !4!! re%ire8ent.

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Fire ater &e8an& 'or each one is s%88erie& in +a9le ." 9elo-Details o' the 'ireater &e8an& calc%lation is shone&shoe& in Appen&ix B.

+a9le ."- 1%88ar o' Fireater &e8an& calc%lation.

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n"

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E=*pm%n" "oD%#=6%

" M%ster /

Par7ingArea

340 +C;*

!4!!-"1ection "0.

! ! *A 340 *A

! :''ice "!!.3 +C;*!4!!-"1ection "0.2+C;* 33421ection 4.#

3 ! ##.3 !#!.3 *A

3 Canteen Garage/CarPar7ing

+C;*!4!!-"1ection "0.

3 ! *A " *A

# or7shop !"!. +C;*!4!!-"1ection "0.2+C;* 3342

1ection 4.#

3 ! "3#. 33!. *A

areho%se

!"!. +C;*!4!!-"1ection "0.2+C;* 33421ection 4.#

3 ! "3#. 33!. *A

4 Fire1tation

"!!.3 +C;*!4!!-"1ection "0.2+C;* 33421ection 4.#

3 ! ##.3 !#!.3 *A

asteatertreat8entarea

"0 *FPA "#2+C;*!4!!-"1ection "0.

3 "0 *A

FireaterP%8pho%se

"0 *FPA "#2+C;*!4!!-"1ection "0.

3 "0 *A

ControlB%il&ing

"0 *FPA "#2+C;*!4!!-"1ection "0.

3 *A "0 *A

"0 Electrical1itchroo8 an&+rans'or8er

"0 *FPA "#2+C;*!4!!-"1ection "0.

3 *A "0 *A

"" E8ergencDiesel

Generator

"0 *FPA "#2+C;*!4!!-"

1ection "0.

3 *A "0 *A

"! Poergeneration1tation

"0 *FPA "#2+C;*!4!!-"1ection "0.

3 *A "0 *A

"3 Pig?a%ncher/eceiverMetering17i&s

304.! *FPA "2*FPA"#

" 3 "!4.! #!4.! Pig la%nchers(";30"/";#0"

/";00")2 Pigreceiver (";00")2?PG Con&ensate

Metering s7i&s("M!!0"/"M!303)

"# ater+reating

Area

"0 *FPA "#2+C;*!4!!-"1ection "0.

3 *A "0 *A

Pile Calculation (Typical)Process Design CriteriaDocument No. U-00034-PRCI-C!CRT-000"Page 3K 37 o# 4$8R%&.0

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No o>+o'%o="#%"

o>+y.)an"

'

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>*)%+y.)a

n"

.%#=6%Sp)*n,#%)'

7m1+)8

A("=a#F*)%a"%

)p)o&*.%.7m1+)8

E=*pm%n" "oD%#=6%

" >tilit Area !".4##

!.3

*FPA "2

+C;*!4!!-"1ection "0.

" 3 .33!4!.

!

3.334

!.3

,P F%el gas

scr%99er (";3!0!)2Methanol +an7

(";30")2 1pentMethanol +an7

(";30#)2 Methanolinection p%8ps

("P30!A/B2"P303A/B)2 ,ot oil

expansion &r%8(";3#0")2 ,ot oil

heaters(",3#03A/B)

"4 1l%gCatcher

Area

30.#!#0

*FPA "2*FPA "#

3 ! 0.#!*A 30.#!#0

Gas 'ilter an&1eparators

(";"003A/B)

" :''spec

B%lletArea

"4!.

3.4

*FPA "2

*FPA "#

" ! ""!.

.4

"!.

.4

:''spec

B%llet (";!#!"):''spec trans'er

p%8ps ("P!#!!A/B)

" ?PG1torage+an7 Area

"!#.0 *FPA "2*FPA "#

" ! "04.0 "30.0 Cooling 'or overalls%r'ace area o'

sphere tan7(";!!0"A) on 'ire

an& cooling hal' thes%r'ace area o'

sphere tan7(";!!0"B) a&acentsphere tan7 on 'ire2

?PG +rans'erP%8ps ("P!!0"

A/B)

" Con&ensat

e1torage+an7 Area

4"!." +C;*

30-!002*FPA ""2 *FPA"

" ! #"0.!3 40.!3 Con&ensate storage

tan7s ("+!30"A/B)2Con&ensate trans'erp%8ps ("P!30!A/B)2+an7 Flare =: Dr%8(";3")2 +an7 Flare=: P%8p ("P33")

!0!0 ProcessArea

ProcessArea $B?

"#".3""!.#!

*FPA "2+C;*

!4!!-"1ection

"0.*FPA "2*FPA "#

!" !3 0 "!3.3""0.33

".3""3.33

"C"0!A/B/C 1alesGas Co8pressor2

";"0"A/B/C 1alesGas Co8pressor1%ction 1cr%99er2"E03A/B/C 1alesGas Co8pressor

A'tercooler2 ",3#""A/B/C 1ales Gas

Co8pressor

,>"C"0!A/B/C1ales Gas

Co8pressor2";"0"A/B/C 1ales

Gas Co8pressor1%ction 1cr%99er2"E03A/B/C 1alesGas Co8pressor

A'tercooler2 ",3#""A/B/C 1ales Gas

Co8pressor ,>

!"!" ProcessArea

ProcessArea $B?

"33.!".4

*FPA "2+C;*

!4!!-"1ection

"0.*FPA "2

*FPA "#

!! "! 0 "04.#!.3

"34.#.3

";"0" Con&ensate1%rge Dr%82

";"0! Con&ensateFractionator2 ";"0

Flash Gas

Co8pressor 1%ctionDr%82 Phase !

e%ip8ent Ethane


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o>+y.)an"

'

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.%#=6%Sp)*n,#%)'

7m1+)8

A("=a#F*)%a"%

)p)o&*.%.7m1+)8

E=*pm%n" "oD%#=6%

+reater =: &r%82

Ethane a9sor9er2P%8ps2 Exchangers2

Coolers";"0"Con&ensate 1%rge

Dr%82 ";"0!Con&ensate

Fractionator2 ";"0Flash Gas

Co8pressor 1%ctionDr%82 "+"!"! P%re

A8ine 1torage +an72"P"!0A P%reA8ine P%8p

!!!! ProcessArea

Process

Area $B?

".0#.!

*FPA "2+C;*

!4!!-"

1ection"0.*FPA "2

*FPA "#

!! !! 0 #!0.#04.3

0.44.3

";"#0#De8ethanierPhase ! '%t%re

p%8p";"#0#De8ethanier

!3!3 ProcessArea

ProcessArea $B?

0.0.

*FPA "2+C;*

!4!!-"1ection

"0.*FPA "2*FPA "#

!3 33 0 !."4!."4

!."4"""!."4

E"#04 Con&ensate1%9cooler2 Phase !

e%ip8ent Deethanier re'l%x&r%8. Deethanier2

e'rigerantpac7ageE"#04

Con&ensate1%9cooler2 Phase !

e%ip8ent Deethanier re'l%x&r%8. Deethanier2

e'rigerant pac7age

!#!# ProcessArea

ProcessArea $B?

..#

*FPA "2+C;*

!4!!-"1ection

"0.*FPA "2*FPA "#

3! 33 0 3!.!#0".!4

4.!!".!4

";30" Close&Drain ;essel2

"P"0!A/B ?PGCol%8n e'l%x

P%8ps2 ";"0#?PG Col%8n2"E"0! ?PG

Col%8n Con&ensorCooler2 "E"03

Con&ensate Pro&%ctCooler2 ";30"

Close& Drain ;essel2"P"0!A/B ?PGCol%8n e'l%x

P%8ps2 ";"0#?PG Col%8n2

"E"0! ?PGCol%8n Con&ensor

Cooler2 "E"03Con&ensate Pro&%ctCooler2 "E"0# ?PG

Col%8n Fee&Pro&%ct Exchanger

!! ProcessArea

ProcessArea $B?

"3.#"#!.04

*FPA "2+C;*

!4!!-"1ection

"0.*FPA "2*FPA "#

33 !! 0 #3#..3!

"#."#4.3!

"E"#"! Col&Gas/?i%i&s

Exchanger2 "E"#0!Col& Gas/Gas

Exchanger2 "E"#""ar8 Gas/?i%i&sExchanger2 "E"#0"

ar8 Gas/GasExchanger2 "L!"0"

egenerationpac7age"E"#"!Col& Gas/?i%i&s

Pile Calculation (Typical)Process Design CriteriaDocument No. U-00034-PRCI-C!CRT-000"Page 3N 39 o# 4$8R%&.0

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n"

.%#=6%Sp)*n,#%)'

7m1+)8

A("=a#F*)%a"%

)p)o&*.%.7m1+)8

E=*pm%n" "oD%#=6%

Exchanger2 "E"#0!

Col& Gas/GasExchanger2 "E"#""ar8 Gas/?i%i&sExchanger2 "E"#0"

ar8 Gas/GasExchanger2 "L!"0"

egenerationpac7age

!4!4 ProcessArea

ProcessArea $B?

43.4#".#

*FPA "2+C;*

!4!!-"1ection

"0.*FPA "2*FPA "#

3! !! 0 !.3"!#.3

4.3##.3

";"40" Merc%rG%ar& Be&2 ";"30"

Deh&ration $nlet1eparator2 ";"30!

Molec%lar 1ieveBe&2 "E"303

egeneration GasCooler2 "E"30#

egeneration GasCo8pressor A'ter

Cooler2 "F"30!A/Begeneration Gas

Filter (Gas)2 "F"303egeneration Gas

Filter (?i%i&)";"40"Merc%r G%ar& Be&2";"30" Deh&ration

$nlet 1eparator2";"30! Molec%lar1ieve Be&2 "E"303egeneration Gas

Cooler2 "E"30#egeneration GasCo8pressor A'ter

Cooler!! Process

AreaProcess

Area $B?

#0".""!0.!

*FPA "2+C;*

!4!!-"1ection

"0.*FPA "2*FPA "#

!! !! 0 4.3.

#!."".

";"003A/B GasFilter an&

1eparatorPhase !e%ip8ent Ethane+reater =: &r%82Ethane a9sor9er2

P%8ps2 Exchangers2Coolers

!! ProcessArea

ProcessArea $B?

!0.30.

*FPA "2+C;*

!4!!-"1ection

"0.*FPA "2*FPA "#

!! !! 0 43.04!.4

.04"0.4

"P"!0"A/B/C ,Pse8ilean sol%tionp%8ps2 "E"!0"

Fee& Pro&%ctGasExchanger2 ";"!03A8ine A9sor9er2"E"!0# 1ol%tion

Cooler2 ";"!0!A9sor9er 17i88ing

Dr%82 ";"!0A8ine ecover

Dr%82 ">"!0"A8ine 1%8p2

"E"0" Con&ensateFractionator:verhea&

Co8pressor2";"!0# Pro&%ct Gas

=: Dr%82"P"!0"A/B/C ,Pse8ilean sol%tionp%8ps2 "E"!0"

Fee& Pro&%ctGas

Exchanger2 ";"!03A8ine A9sor9er2"F"!0! Activate&


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.%#=6%Sp)*n,#%)'

7m1+)8

A("=a#F*)%a"%

)p)o&*.%.7m1+)8

E=*pm%n" "oD%#=6%

Car9on Filter2

";"!0! A9sor9er17i88ing Dr%82";"!0 A8ine

ecover Dr%82">"!0" A8ine1%8p2 "E"0"

Con&ensateFractionator:verhea&

Co8pressor2"E"!0# 1ol%tion

Cooler

!! ProcessArea

ProcessArea $B?

"4.!"34.!

*FPA "2+C;*

!4!!-"1ection

"0.*FPA "2*FPA "#

33 !! 0 "!."0.4

".".4

";"!0 ich1ol%tion Flash

Dr%82 ";"!04 ?PFlash

Col%8n";"!0 ich1ol%tion Flash

Dr%82 ";"!04 ?PFlash Col%8n

3030 ProcessArea

ProcessArea $B?

!".4!".4

*FPA "2+C;*

!4!!-"1ection

"0.*FPA "2*FPA "#

!! !! 0 00 340340

3"3" ProcessArea

ProcessArea $B?

#3.0#0."3

*FPA "2+C;*

!4!!-"1ection

"0.*FPA "2*FPA "#

!! "! 0 !#" #.0 #"3#.0

";30" ,P ar8et Flare =: Dr%82";3"" ?P Flare =:

Dr%8";30" ,Par8 et Flare =:Dr%82 ";3"" ?P

Flare =: Dr%83! ?a9orator "!!.3 +C;*

!4!!-"1ection "0.2+C;* 33421ection 4.#

3 ! ##.3 !#!.3 *A

33 G%ar&,o%se "

40 +C;*!4!!-"1ection "0.

3 "0 *A

3# G%ar&,o%se !

40 +C;*!4!!-"1ection "0.

3 "0 *A

3 Diesel1torage+an7 Area

!!." +C;*30-!002+C;*30-!00

" ! #." !." *A

34 A8ine1torage+an7 Area

30. *FPA "2*FPA "#

" ! "!. 34. P%re A8ine 1torage+an7 ("+!0!)2 P%re

A8ine P%8p("P"!0A)

@-1 (apa(*"y o> >*)%a"%) p=mp'

Accor&ing to +a9le ."2 the largest 'ire ater &e8an& is at Fire Ione "!2:''spec B%llet AreaProcess Area $B? ith "2!.4. 83/hr.

HFI"!K "2!.40 83/hr

Propose three (03) nos o' 'ireater p%8ps2 ! &%t an& " stan&9. +he'lorate o' each 'ireater p%8p shall 9e selecte& 9 0J o' the largest 'ire ater

&e8an&.H'lorate o' each 'ireater p%8p K "2!.40 (8

3/hr) x 0/"00 K 4.# #0 83/hr.

Pile Calculation (Typical)Process Design CriteriaDocument No. U-00034-PRCI-C!CRT-000"Page E 41 o# 4$8R%&.0

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PE+:;$E+*AM GA1 GA1 P:CE11$*G P?A*+ P:PDA+$*G FEA11$B$?$+@ 1+>D@ F: GA1 P:CE11$*G P?A*+ P:o) ma*n >*)%a"%) .*%'%# %n6*n%' p=mP

+he '%el cons%8ption 'or 8ain 'ireater &iesel engine p%8p shall 9e s%pplie& 9p%8pOs 8an%'act%rer &epen&ing on respective p%8pOs 8an%'act%rer. +he esti8ate&'%el cons%8ption 'or 'ireater &iesel engine p%8ps shall 9e calc%late& 9ase& on theesti8ate& poer rating the &iesel engine as per *PFA !0 section "".#.! an& section.4.!.3 as 'ollos-

F%el storage capacit o' the &iesel &a tan7 shall 9e at least e%al to " gal per hp

(.0 ? per 7).

+he %antit " gal per hp (.0 ? per =) is e%ivalent to " pint per hp (0.43# ? per7) per ho%r 'or ho%rs.

+he '%el s%ppl capacit shall 9e s%''icient to provi&e ho%rs o' 'ire p%8p operation

at "00 percent o' the rate& p%8p.

,ence the vol%8e o' '%el &a tan7 'or &iesel engine p%8p ; K Q ho%rs x &iesel

engine rate poer (=) x 0.43# (litres)/(=)/ho%rR S "0J vol%8e (space 'ro8 ,,

level to the top o' tan7)

; K "." x Q ho%rs x #0!.! (=) x 0.43# (litres)/(=)/ho%rR K !2!#."4 (litres) K 4-1

83

.Propose& '%el &a tan7 'or &iesel engine sie K ".!8 ($D) x !."8 (,)2 *ote- Diesel

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