Albacora Project Pa Traducir

8/17/2019 Albacora Project Pa Traducir

1/22

TABLE OF CONTENTS

CONCEPTUAL STUDY.......................................................................................................................1

1. Purpose:...............................................................................................................................3

2. Project Description...............................................................................................................3

3. Metocean and Environmental Details for the FSO and sumarine !ine "nstallation.............#

#. Specifications.......................................................................................................................$

$. %e&ulator' and Permittin& %e(uirements.............................................................................)

*. Desi&n !ife...........................................................................................................................+

). Earl' Production Facilities on ,1-+-...................................................................................+

/.0 Moorin& S'stem.................................................................................................................12

10.0 "nterconnectin& Sumarine !ine.........................................................................................12


2/22

1. Purpose:

his onceptual Stud' is a document that provides the &eneral and technical"nformation to e used in the ne 4asic Desi&n and Detail En&ineerin& of the"nstallation of Earl' Production Facilities on ,1-+- Platform.

2. Project Description

he lacora Field hich lies ithin the 4loc5 ,-1 oncession rea is developedand operated ' 4P, Ener&' "nc. he Field is located appro6imatel' + miles off thecoast of Peru 1 mile south of the international oundar' ith Ecuador.

he field as ori&inall' discovered ' enneco in 1/)2 ith the drillin& of the +-7-2e6plorator' ell hich tested over $000 4OPD and si&nificant (uintiles of natural&as. Suse(uent development activities ' enneco and later ' 4elco Petroleumere onl' partiall' successful ith the field finall' temporaril' aandoned in 8anuar'1/)+. total of appro6imatel' 1009000 4O ere produced from the 3 productionells efore the field as shut in. #-pile platform remains at the site alon& iththe 3 shut-in production ells.

he field development provides for collectin& the oil9 &as and ater produced fromthe lacora field on the e6istin& platform ,1-+-. he platform has a top dec59 ameanine dec5 and a ell head dec59 here ill e installed the Earl' ProductionFacilities to process the fluids of oil9 &as and ater. he oil ill e delivered toFloatin& Stora&e Offloadin& ;FSO< via sumarine pipeline9 in the platform the &as

ill e urner and the ater treated efore of its disposal. he oil ill e periodicall'loaded from the FSO to the shuttle tan5er for transportation to the alara %efiner'appro6imatel' 100 Miles south of the site.

he Production rate to e process for the Production Facilities is the folloin&:

• Ma6imum oil production of 109000 4OPD hree Phase Separators

• Ma6imum ater production of /9000 4=PD

• Ma6imum &as production of 20 MMSFD orch >as flare

• Ma6imum emulsion Oil?=ater $9000 4PD reater

he Platform ,1-+- has 777 free conductors to e drillin& . he @uAuanu FSOhas a stora&e capacit' of 3+9000 44!S. he production of Oil ill e are sentdirectl' ' one *B sumarines lines from ,1-+- Platform to a P!EM located near the spread moorin& station and *C fle6ile hose from the P!EM to the @uAuanuFSO. he &as produced ill e urner and the ater ill disposal in the Platform.

his scope document ill outline the asic field development option and providethe asis for a - 20 cost for the proposed facilities.

he estimated schedule for this project ill e 10 months ;pril 2010


3/22

3. etoce!n !n" En#iron$ent!% Det!i%s &or t'e FSO !n" su($!rine Line)nst!%%!tion

he ater depth is 31 meters. mient eather9 seaed and marine conditionsshould in &eneral e similar to those for orvina.

he coastal areas of Peru are e6ceptionall' dr' and mild. Prevalent ave hei&htsare $ to + feet. Sell directions are &enerall' from the south ;#$ from the south920./ from the southeast9 and 2).* from the southest


4/22

0.$ Iour =ind #) MPI1 Minute =ind $) MPI 22.3 MPIMa6. "nstantaneous >ust *+ MPIurrent 0.23/ to 0.+)$ m?sec at surface

urrent 0.0#+ to 0.331 m?sec. at $ m. elo surface

Ma6imum rainfall rate 1.$ inches per hour

SEI"D%O9 ma' 200/

*. Speci&ic!tions

he folloin& standards are to e used as &uides and to e folloed e6plicitl'here applicale. dditional discussion ma' e re(uired to resolve (uestionsre&ardin& applicailit' or to revie discretionar' issues.

4S lass rules - >uide For 4uildin& and lassin& Floatin& Production J Stora&eS'stems- %ules For 4uildin& and lassin& Steel Kessels- %ules For lassin& Facilities on Offshore "nstallations- >uide for 4uildin& and lassin& Facilities on Offshore"nstallations

"MO %e&ulations - ode for the onstruction and E(uipment of Moile OffshoreDrillin& Gnits9 1/+/ amendments 1//1 ;MODG code<- "nternational onvention on !oad !ines 1/**

M%PO! 1/)3 "ncludin& Protocol of 1/)+9 edition 1//) amendment

1///O"MF =here applicale

@FP =here applicale

SOLAS 1974 !ifesafin&

"S S33$ Specification for Structural Steel 4uildin&s lloale StressDesi&n and Plastic Desi&n ith ommentar'

=S D1.1 Structural =eldin& ode Steel Fifteenth Edition

SE ) Minimum Desi&n !oads for 4uildin&s and Other Structures

SI%E *2 Kentilation for cceptale "ndoor ir Lualit'

@S" 10.#-1//0 Personnel Ioists and Emplo'ee Elevators for onstruction andDemolition Operations9 Safet' %e(uirements for

P" 2 Specifications for offshore cranes

P" SPE 128 Specification for Oil and >as Separators Seventh Edition

P" %P 1# %ecommended Practice for nal'sis9 Desi&n9 "nstallation9 andestin& of 4asic Surface Safet' S'stems for Offshore ProductionPlatforms Fifth Edition Errata - 1//#

P" %P 1#E %ecommended Practice for Desi&n and "nstallation of OffshoreProduction Platform Pipin& S'stems Fifth Edition

P" %P 1#F %ecommended Practice for Desi&n and "nstallation of ElectricalS'stems for Offshore Production Platforms hird Edition

P" %P 1#> %ecommended Practice for Fire Prevention and ontrol on Open'pe Offshore Production Platforms

P" 1#8 Desi&n and Iaard nal'sis for Offshore Production Facilities

P" %P $00 %ecommended Master Practice for lassification of !ocations forElectrical "nstallations at Petroleum Facilities First Edition


5/22

;Supersedes %P $009 %P $0049 %P $00<

P" $0$ %ecommended Master Practice for lassification of !ocations forElectrical "nstallations at Petroleum Facilities lassified as lass"9 ,one 09 and ,one 2

P" %P $20 P " Siin&9 Selection9 and "nstallation of Pressure-%elievin& Devicesin %efineries Part " - Siin& and Selection Si6th Edition Errata -1//#

P" %P $20 P "" Siin&9 Selection9 and "nstallation of Pressure-%elievin& Devicesin %efineries Part "" - "nstallation Fourth Edition

P" %P $21 >uide for Pressure-%elievin& and Depressurin& S'stems FourthEdition

SM *?*M Standard Specification for >eneral %e(uirements for %olledStructural Steel 4ars9 Plates9 Shapes9 and Sheet Pilin&

SM 123 %EK Standard Specification for ,inc ;Iot-Dip >alvanied< oatin&s on"ron and Steel Products ;SIO M111<

SM 1$3?1$3M Standard Specification for ,inc oatin& ;Iot-Dip< on "ron and Steel

Iardare ;SIO @o. M232< SME "@ """-1-/2-*) "nterpretation """-1-/2-*) ll Sections of the 4oiler and Pressure

Kessel ode Mandator' %e(uirements9 Specific Prohiitions9 and@onmandator' >uidance for onstruction ctivities ;ll Editionsand ddenda<

SME SE " 4PK SE"O@ " %ules for onstruction of Poer 4oilers ddenda - 1//$ ddenda - 1//* "nterfiled ;4oiler and PressureKessel odes<

SME SE "" 4PK SE"O@ "" Materials Part - Ferrous MaterialSpecifications ddenda - 1//$ ddenda - 1//* "nterfiled ;4oilerand Pressure Kessel odes<

SME SE "" S-3++?S-3++M

Specification for Gltrasonic E6amination of Ieav' Steel For&in&s SM 3++? 3++M-/1 ;4oiler and Pressure Kessel odes<

SME SE "" S-$)+?S-$)+M

Specification for Strai&ht-4eam Gltrasonic E6amination of Plainand lad Steel Plates for Special pplications SM $)+?$)+M-/2 ;4oiler and Pressure Kessel odes<

SME SE "" D PPE@D"7 $

>uideline on the pproval of @e Materials Gnder the SME4oiler and Pressure Kessel ode

SME SE K"""D"K"S"O@ 1

4PK SE"O@ K""" %ules for onstruction of Pressure KesselsD"K"S"O@ 1 @on-"nterfiled ;4oiler and Pressure Kessel odes<

SME SE K""" D1@M PP 4

pproval of @e Materials Gnder the SME 4oiler and PressureKessel ode

SME SE K""" D2@M PP F

@onmandator' pproval of @e Materials Gnder the SME 4oiler and Pressure Kessel ode

SME 41*.#) !ar&e Diameter Steel Flan&es @PS 2* hrou&h @PS *0

SME 41*.#+ Steel !ined 4lan5s

SME 41*.$ Pipe Flan&es and Flan&ed Fittin&s @PS 1?2 hrou&h @PS 2#

SME 431.1 Poer Pipin&

SME 431.3 Process Pipin&

SME 431.+ >as ransmission and Distriution Pipin& S'stems

> Standard @o. / Measurement of >as ' Multipath Gltrasonic Meters

SSP SP 1 Solvent leanin& ;Steel Structures Paintin& Manual9 h 2 -Surface Preparation Specs.<

SSP SP * 8oint Surface Preparation Standard ommercial 4last leanin&

;@E @o. 3: 1//#< ;Steel Structures Paintin& Manual9 h 2 -Surface Preparation Specs.


6/22

+. ,e-u%!tor !n" Per$ittin- ,e/uire$ents

ll modifications and provisions must meet the re(uirements and approval of Peruvian authorities ;D>E9 OS"@E%>9 D"P"9 and ransportationE includin& the plans to install the ProductionFacilities on ,1-+- Platf. and the FSG.

0. Desi-n Li&e

he Earl' Production Facilities e installed on ,1-+9 durin& the duration of thedrillin& jos9 appro6imatel' 02 'ears

he desi&n service life of the moorin& s'stems shall have a minimum desi&nservice life of at least 30 'ears or in accordance ith re&ulations9 4S or other&overnin& industr' standards.

. E!r% Pro"uction F!ci%ities on 14Ahe production facilities that ill e installed on ,1-+-9 should e desi&ned tomana&e the Oil9 >as and =ater produced in the first Phase.

.1 F%o5%ines &ro$ t'e 5e%%s

Flolines ill e 3C nominal rated for 3)0$ psi& in accordance ithpipin& specifications for this class and P" 1#E siin& criteria. de(uateranch fittin&s are to e provided to monitor pressure9 temperature9

allo for chemical injection9 provision of pressure sensin& lines to thecontrol panel ;PSI!


7/22

Gpon loss of si&nal from the MP9 the control panel causes all SSKNs9SDKNs and SSSKNs to e closed ;!evel 1 Shutdon


8/22

ill e 2+3 psi& ith a 1?+C corrosion alloance and e SME stamped.4affles and level controls ill e provided.

. 7!-e T!n8 9:ST; !n" Tr!ns&er Pu$p S8i"

he an5 shall e used for chec5in& the oil meter?shrin5a&e factors andfor measurin& volumes at rates for accurate flo meter measurement.he capacit' of tan5 shall e at least 100 4ls and ill or5 atatmospheric pressure. he KS ill consist of a sin&le- or doule-compartment vessel and a level- measurin& s'stem ith si&ht &lasses or ma&netic levels. o prevent overpressure and overfillin&9 the KS shalle fitted ith a pressure-relief valve and a hi&h- and lo- level alarms'stem. Desi&ned ith a diverter9 a vorte6 rea5er9 and stiffenin& rin&scapale of ithstandin& a vacuum in the vessel. Fitted ith samplin&9pressure9 and temperature ports. 'pass manifold shall e also

included to permit isolatin& of the sur&e tan5 from flo process. he oilill &o to the sumarine line and the &as ill e flared.

.4 F%!re Boo$

he flare oom of 120 Ft. flare ip of 10 Ft 6 +B has een desi&ned for 1$-20 MMSFD ith the ma6imum radiation ;not includin& solar radiation< at the ase of the flare to e less than $00 4G?hr?ft2. heflare oom ill e installed eteen the loer and upper dec5s in theside northest.

.< E$u%sion oi%= >!ter Tre!t$ent ? 6ori@ont!% Tre!ter= E%ectrost!tic Sste$

Ioriontal reater of !.P. )2B 6 12 Ft. 6 2+3 M=P ith Electrostaticcoalescence s'stem ill e provided9 in hich independent and Dh'drophilic electrodes are emplo'ed to provide more completedeh'dration of an oil emulsion. he field is produced eteen an electrode arra' and the ater-oil interface herein the electrodearra' is positioned parallel to the interface hich acts as a &roundedelectrode. he emulsion is introduced into the field in an evenl'distriuted manner at the interface. he field promotes drop-drop anddrop-interface coalescence of the ater phase in the enterin& emulsion.he continuous oil phase passes upard throu&h the perforated electrode arra' and enters a stron& D field produced eteen closel'

spaced D electrodes in hich small dispersed droplets of ater entrained in the continuous phase are removed primaril' ' collection ath'drophilic D electrodes. !ar&e droplets of ater collected ' theelectrodes mi&rate donard throu&h the electrode arra' to theinterface.

he reater is to e desi&ned to process $9000 4PD of emulsionoil?ater produced. he tar&et outlet concentration ill e less than 30ppm measured &ravimetricall'. 4affles and level controls ill e providedas re(uired.

4. Uti%it Sste$s.


9/22

4.1 Fire Fi-'tin- Sste$ on FSO !n" 14A P%!t&or$

he FSO ill have a Fire fi&htin& s'stems desi&ned and installed in

accordance ith the rules9 standards and reference documents of SO!S chapter ""-29 Part >eneralB and Part D Fire Safet' measuresfor tan5ersBhe fire fi&htin& s'stem ill include to independent diesel en&inedriven fire pumps. Each ill have a capacit' of 2000 &pm at 1$0 psi&.One pump is desi&nated as the primar' pump and the other as thestand' pump. joc5e' pump ill maintain the fire ater header char&ed to a pressure of 120 psi& normall'. he primar' fire pump is setup to start automaticall' upon receivin& a si&nal from the Fire J >asdetection panel or upon loss of pressure in the fire ater header. "f theprimar' pump does not start in three start attempts9 the stand' pumpill attempt to start. he pumps are started usin& utilit' air. ac5up

startin& s'stem usin& stored nitro&en &as is also provided. he firepumps can e started from the local control panel or from the remote fireand &as panel located in the M Sitch&ear room. Diesel stora&e for each en&ine driver is for 1+ hours of run time.

On the ,1-+- Platform the Facilities9 the spra' s'stem should edesi&ned to provide a ater of e6posed surface of the vessels. Gpondetection of fire in an' one9 all delu&e valves are automaticall'operated9 ith provision for manual operation. "n addition to suppl'in& tothe delu&e s'stem9 the fire ater pumps also provide ater to manuall'operated hose reels. o hose reels each are provided in the perimeter of Facilities and utilit' module. One fire hose station ill e installed at

each level of the livin& (uarters.

4.2 )nstru$ent!tion !n" Contro% P'i%osop'!evel controllers ill e pneumaticall' and locall' operated. Meterin&ill e recorded locall'.

4.3 Po5er 7ener!tion !n" Distri(utionhe Poer Suppl' ill e provided ' the Drillin& %i&.

4.* Cr!nerane ill e provided ' the Drillin& %i& and ender 4ar&e.


10/22

4readth: 1/.$ mtsDepth: $./ mtsDraft: #.# mts. ;full load<Oil apacit': 3+9000 44!S

he @uAuanu 4ar&e should e sumitted to the folloin&s or5s:

• Modification s'stem to permit the loadin& and offloadin& in the

same time.

• "ndependent tan5 for ater produced.

• ccommodations.

• Port riser "nstallation on o.

• %elocate En&ine %oom.

1. )nterconnectin- Su($!rine Line

%i&id sumarine !ine and Fle6ile line?hose riser are to e installedeteen ,1-+ - and the @uAuanu and @uAuanu to Shuttle an5er. Iose%iser is e6pected to e on the order of 10$ ft in len&th9 ut desi&n is inpro&ress to determine e6act confi&urations.

1.1 Fro$ 14A P%!t&or$ to NUUANU FSO ? 0 ANS) C%!ss 1+

a< porch t'pe structure ill e installed on the o of the FSO to supportthe end of the hose and on the platform a Pi& !auncher.

< ri&id pipeline seamless of * $?+B O.D. 6 0.2+0B Sch. #0 P" $! 4 629/00 Ft.9 ill e installed on the sea ottom and the riser clamped onthe 8ac5et until its connection ith the Pi& !auncher on ,1-+-Platform9

c< riser of *B ".D. 6 10$ Ft. Fle6ile Sumarine Ioses ill connect theP!EM on the sea ottom ith the Pi& rap @S" lass 1$0 %.F installedon the FSO.

1.2 Fro$ NUUANU FSO to s'utt%e t!n8er 4 ANS) C%!ss 1+

a< structure ill e installed on the FSO to support the riser of 10$ Ft.Fle6ile Sumarine hoses doule arcass. his riser ill connect theP!EM on the sea ottom ith the support.

< ri&id pipeline seamless of + $?+B O.D. 6 0.322B P" $! 4 Sch. #0 6#9000 Ft.9 ill e installed eteen the P!EMs on the sea ottom.

c< riser of +B ".D. 6 10$ Ft. Fle6ile Sumarine Ioses doule carcass illconnect the P!EM on the sea ottom ith the calm uo' installed on thesea level.

1.3 Etern!% Corrosion contro%


11/22

4oth sumarine lines ill e protected ith hree !iner E6ternal oatin&3.0 m.m. film thic5ness and athodic Protection ' inc &alvanic anodes

PPE@D"7

1. !4O% Field rea

2. Fluid Description- lacora Oil and Deliver'>as

3. Process Flo Dia&ram

#. !a' Out Production Facilities on ,1-+- Platf

$. Orientation ,1-+- Platform9 FSO 9 Shuttle

Kessel and Sumarine lines*. Preliminar' ost

). Estimated hrono&ram


12/22

1. ALBACO,A Fie%" Are!


13/22

2. F%ui" Description

A%(!cor! Oi% !n" De%i#er 7!s


14/22

: Well Stream Composition

Component Sep Liquid Mole % Sep Gas Mole % Well Stream Mole %

Carbon Dioxide 0 0.09 0.04

Nitrogen 0 0.12 0.06Methane 4.78 93.74 4.64

!thane 0.4 1.2 0.89

"ro#ane 1.99 2.2 2.09

$%o&b'tane 1.3 0.74 1.14

N&b'tane 2.98 0.87 1.94

$%oentane 2.3 0.49 1.43

Nentane 1.99 0.17 1.09

(exane 8.71 0.1 4.49

(exane ) 7.13 0.18 38.19

Hydrocarbon Properties

A"$ *ra+it, o- he#tane% ) 34.3 degree% A"$

S#ei-i *ra+it, o- Se#arator *a% .629

Mo/e'/ar eight o- (e#tane% ) 221

'bb/e "oint "re%%'re 3283 #%i

S#ei-i *ra+it, o- (e#tane% ) .846


15/22

3. Process F%o5 Di!-r!$


16/22

*. L! Out Pro"uction F!ci%ities on 14AP%!t&

>ELL 6EAD DEC


17/22

LO>E, DEC


18/22

UPPE, DEC

+. Orient!tion 14A P%!t&or$ FSO S'utt%eesse% !n" Su($!rine %ines


19/22

0. Pre%i$in!r Cost


20/22

COST COPONENT TOTAL COST

ite$s DESC,)PT)ON EST)ATE 9G;

EN7)NEE,)N7 STUD)ES1 4S" E@>"@EE%"@> 1$0

2 DE"! E@>"@EE%"@> *00

# O@SG!"@> 100

$ PE%M"S $0

SUBTOTAL: ATE,)ALS S ;used< 19000

12 P"P"@>9 K!KES @D F""@>S #00

13 E!E%"! ELG"P. J ME%"!S 2$0

1# "@S%GME@ ELG"P. J ME%"!S 300

1$ >S F!%E SHSEM +0

1* SD SHSEM /0

1) O%%OS"O@ P%OE"O@ ;Paint9 anodes9 etc< $0

SUBTOTAL: ATE,)ALS +4+G

LABO,1+ ELG"PME@ I@D!"@> @D SE"@> )0

1/ S%GG%! F4%""O@ ;flare oom9 ou's9 clams9 etc< $00

20 P"P"@> F4%""O@ @D "@S!!"O@ 20021 P"PE!"@E "@S!!"O@ 300

22 O@%EE DEI *0

23 E!E%"! "@S!!"O@ @D IOOQ-GP $0

2# "@S%GME@"O@ "@S!!"O@ @D IOOQ-GP +0

2$ OMM"SS"O@"@> @D S%GP #0

2* D"K"@> 300

2) M"S. OFFSIO%E SE%K"ES *0

SUBTOTAL: LABO, 100G

TOTAL EST)ATED COST 430+G

CONT)N7ENCY 2 H 103G

TOTAL EST)ATED COST >)T6 CONT)N7ENCY 134

ALBACO,A F)ELD COST EST)ATED

EA,LY P,ODUCT)ON ON 14A AND OO,)N7 SYSTES


21/22

. Esti$!te" C'rono-r!$


22/22

4.

/.

Albacora Project Pa Traducir

Documents

Transcript of Albacora Project Pa Traducir