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    SPECIFICATIONEQUIPMENT DESIGN CONDITIONS

    02 IFD Issued for Design 22-Jul-11 F.Le Frapper V. Fort X.Grandiaud

    01 IFC Issued for Comments 03-May-11 F.Bessieres F.Le Frapper X.Grandiaud

    Rev Status Revision Memo Date Written By Checked By Approved By

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    INDEX

    1 GENERAL ..................................................................................................................................................4

    2 REFERENCE DOCUMENTS .....................................................................................................................4

    2.1 Project Documents............................................................................................................................4 2.2 Codes and Standards........................................................................................................................4

    3 DEFINITIONS.............................................................................................................................................4

    4 ABBREVIATIONS......................................................................................................................................4

    5 ENVIRONMENTAL AND SITE CONDITIONS...........................................................................................5

    5.1 Facilities General Location................................................................................................................5 5.2 Facilities Coordinates........................................................................................................................6 5.3 Environmental Conditions .................................................................................................................6

    5.3.1 Ambient Air Temperature .............................................. .................................................... ...........................6 5.3.2 6 5.3.3 Relative humidity..........................................................................................................................................6 5.3.4 Solar Radiation.............................................................................................................................................6 5.3.5 Prevailing Wind ................................................. .................................................... .......................................6 5.3.6 Rain fall ...................................................... ........................................................ ..........................................7

    5.4 Soil Characteristics............................................................................................................................7 5.5 Hydrological data...............................................................................................................................7 5.6 Seismic Data .....................................................................................................................................7

    6 EQUIPMENT DESIGN CONDITIONS........................................................................................................8

    6.1 Design life..........................................................................................................................................8 6.2 Temperature and humidity ................................................................................................................8 6.3 Blast Conditions ................................................................................................................................8 6.4 Design Conditions for Transportations..............................................................................................8 6.5 Flare Radiations ................................................................................................................................8 6.6 Environmental Pollution.....................................................................................................................9

    6.6.1 Emissions for Hydrocarbon Installation Equipment .............................................. ........................................9 6.6.2 Emissions for Electrical Generators and Boilers...........................................................................................9 6.6.3 Rejected Water Regulation Performances Criteria.....................................................................................10

    7

    THE PRESENT PARAGRAPH CONCERNS ONLY RAINWATER AND FRESH WATER REJECT.REQUIREMENT FOR OPEN DRAIN REJECT ARE IN HOLD.......................................................................10

    7.1.1 Noise .................................................. ....................................................... .................................................10

    8 UTILITY ....................................................................................................................................................11

    8.1 Electrical..........................................................................................................................................11 8.1.1 Piraa CPF.................................................................................................................................................11 8.1.2 Curaray Terminal........................................................................................................................................12 8.1.3 Piraa PPiX................................................................................................................................................13

    8.2 Fuel Gas ..........................................................................................................................................13 8.2.1 Fuel Gas Design.........................................................................................................................................13 8.2.2 13 8.2.3 Fuel Gas Composition................................................................................................................................14

    8.3 Diesel Oil .........................................................................................................................................15 8.3.1 Piraa CPF.................................................................................................................................................15 8.3.2 Curaray Terminal........................................................................................................................................15 8.3.3 Diesel Oil Composition ..................................................... .......................................................................... 16

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    8.4 Crude Oil .........................................................................................................................................18 8.5 Instrument Air ..................................................................................................................................20

    8.5.1 Piraa CPF.................................................................................................................................................20 8.5.2 Curaray Terminal........................................................................................................................................20 8.5.3 Piraa PPiX................................................................................................................................................20

    8.6 Nitrogen...........................................................................................................................................20 8.7 Chemical Injection...........................................................................................................................21

    8.7.1 Piraa CPF.................................................................................................................................................21 8.7.2 22 8.7.3 Arabela River Water Pumpng Station......................................... ............................................................... 22 8.7.4 22 8.7.5 Piraa PPiX................................................................................................................................................22 8.7.6 Curaray Terminal........................................................................................................................................23

    8.8 Utility Water .....................................................................................................................................23 8.8.2 23

    8.9 Potable water ..................................................................................................................................27 8.9.1 Potable Water Design data.........................................................................................................................27 8.9.2 Potable Water Quality ................................................ ........................................................ ........................27

    8.10 Fire Water.......................................................................................................................................31 8.10.1 Fire Water Design data ............................................... .................................................... ...........................31 Note 1 : the firewater ring main at CT is not pressurised and dry during normal operation. When required, the ringmain is fed by two fire water pumps discharging firewater at 8.7 barg (working) minimum (12.5 barg design). ........31 8.10.2 Fire Water Composition..............................................................................................................................31

    8.11 Foam ...............................................................................................................................................31 8.12 MP Flare Network............................................................................................................................32 8.13 LP Flare Network.............................................................................................................................32 8.14 Thermal Oil ......................................................................................................................................32

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    1 GENERAL

    The purpose of this document is to list the project data for the mechanical design and specifications ofequipment relevant to the Peru Block 67 Field Development (Piraa CPF, CT and pads PPi1 and PPi3).This is a general specification. All specific required data shall be found in the dedicated equipmentspecification or data sheet.

    2 REFERENCE DOCUMENTS

    2.1 Project Documents

    [1] PP67-PE-GEN-00-DOR-RP-I-001 Geological and Geotechnical Synthesis Report[2] PP67-PE-GEN-00-DOR-RP-I-002 Hydrological Synthesis Report

    2.2 Codes and Standards

    [3] DS 062-2010-PCB/ 7th October 2010 Aprueban LMP emisiones gaseosas[4] Norma E.030 (2006) Diseo Sismorresistente[5] Ministerio de Salud del Peru El reglamento de la Calidad del Agua para

    Consumo Humano[6] World Bank Group Air emissions and ambient air quality

    3 DEFINITIONS

    Company Perenco Peru Petroleum LimitedContractor DORIS Engineering

    4 ABBREVIATIONS

    AMB Ambient ATM Atmosphere

    CO2 Carbon DioxydeCPF Central Processing FacilitiesDLB Design Level BlastHP High PressureLHV Lower Heating ValueLP Low PressureNO2 Nitrogen DioxideSLB Strength Level Blast

    SO2 Sulphur Dioxide

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    5 ENVIRONMENTAL AND SITE CONDITIONS

    5.1 Facilities General Location

    The site is located on the Maranon Basin in the north-east part of the Peru and is situated in the Amazonrainforest between the Andean Cordillera and the Guyana Shield. Altitude is comprised between 140 m and200 m above sea water level.

    Phase 0 will focus on Piraa field (CPF, PPi1 and PPi3) and CT:

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    5.2 Facilities Coordinates

    Location Reference Point East North Elevation aboveMASL

    CURARAY TERMINAL AS PER EIA 455586.00 9827611.00 160 m

    PIRAA CPF AS PER EIA 458762.00 9788030.00 173 m

    PIRAA 2D 45968838 9787571.78PPI1

    AS PER EIA 459710.00 9787630.00171 m

    PIRAA 3D 458880.00 9783999.97PPI3

    AS PER EIA 45887600 9783999.00178 m

    5.3 Environmental Conditions

    5.3.1 Ambient Air Temperature

    Minimum dry-bulb temperature in winter (C) Minimum dry-bulb temperature in summer (C)

    18.5 28

    5.3.2 Relative humidity

    Minimum Humidity (%) Maximum Humidity (%)

    80 92

    5.3.3 Solar Radiation

    Solar radiation (maximum) = 0.98 kW /m2

    5.3.4 Prevailing Wind

    Minimum wind is 0ms which is actually the most often case with time frequency of 47%.

    Prevailing directions is from North, for 22.8%, with a mean maximal speed of 1.8 m/s and East, for 19.5%,with a mean maximal speed of 1.6 m/s.

    The following design wind speed above ground level shall be considered in all directions:

    All directions-Design Wind Speed

    Return Period 1 year 100 yearsWind Speed (m/s) 6 19

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    5.3.5 Rain fall

    YearlyMonthly Maximum Daily MaximumMinimum Mean Maximum

    540 mm 132 mm 2180 mm 3460 mm 5760 mm

    5.4 Soil Characteristics

    Geological and geotechnical data shall be extracted from the geological and geotechnical synthesis reportRef. [1].

    5.5 Hydrological data

    Hydrological data shall be extracted from the Hydrological Synthesis Report Ref. [2].

    5.6 Seismic Data

    According to Peruvian standards for seismic design (Ref. [4]), the project site is characterized in the followingway:

    Site parameter: Zone 1 corresponding to a zone factor of Z=0.15, Type of soil profile S3 (conservative) on all sites corresponding to a soil amplification factor S of 1.4, Facilities category of importance A: essential facilities corresponding to a U-factor of 1.5.

    Seismic design base shear shall then be computed according the methodology proposed in Ref. [4] forstructural elements and non-structural elements (article 23 respectively).

    The following maximum accelerations shall then be considered: Equipments, tanks, piping : H = 0.29g.

    According to Ref. [4], no vertical seism acceleration shall be considered for zone 1.

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    6 EQUIPMENT DESIGN CONDITIONS

    6.1 Design life

    The equipment shall be designed for a minimum life of 20 years.

    6.2 Temperature and humidity

    Depending on equipment location, following Air design data shall be considered:

    Air design Temperature (C)Location of equipment

    Min MaxAir Humidity design range (%)

    Outdoors 18.5 28 80/92Buildings 22 26 45/55

    The design temperature for guaranteed performance of air cooling system is 28C.The black body temperature is the temperature induced by solar radiation on metal equipment. This is theminimum value for the design temperature and shall be taken into account only for equipment and pipinglocated outdoor. Black Body Temperature = 43 C.

    6.3 Blast Conditions

    Blast event shall not be considered for equipment design.

    6.4 Design Conditions for Transportations

    Equipment shall be designed to withstand here below accelerations in case of sea transportation to site:

    Equipment shall be designed to withstand here below accelerations in case of road transportation to site:

    6.5 Flare Radiations

    Equipments shall be designated to sustain the following radiations:Emergency Flaring Max continous flaringSystem

    kW/m Btu/hr/ft kW/m Btu/hr/ftFlare drum 6.3 2000 4.7 1500Flare piping 9.5 3000 4.7 1500

    Atmospheric storage 3.2 1000 2.4 750Pressure vessel storage 2.0 630 1.6 500Process equipment 4.7 1500 3.2 1000

    Acceleration (g)

    Roll and Pitch 0.9heave 0.8

    Acceleration (g)

    Longitudinally 0.3Vertical & Transverse 0.1

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    6.6 Environmental Pollution

    6.6.1 Emissions for Hydrocarbon Installation EquipmentLatest Peruvian reglementation for hydrocarbon installation emissions is supplied in the Decree DS-062-2010-PCB Aprueban LMP emisiones gaseosas dated of the 7 th October 2010 [6]. The concernedspecification is showed in the following table related to new hydrocarbon installations:

    Regular ParametersActivities of Processing and Refining

    Oil(mg/Nm)

    Particulate Matter (PM) 50Organic Volatile compounds (COV) 20Sulfur Oxid (SOx)

    - Sulphur recovery unit- Other units

    N/A

    150500Nitrogen Oxid (NOx)- Using combustible gas- Using combustible oil

    450N/AN/A

    Nickel (Ni) 1Vanadium (V) 5

    6.6.2 Emissions for Electrical Generators and Boilers As far electrical installations are concerned, unless a new Peruvian Decree is entered in force, the WorldBank shall apply.

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    6.6.3 Rejected Water Regulation Performances CriteriaThe present paragraph concerns only rainwater and fresh water reject. Requirement for open drain reject arein HOLD.

    Waste Water Discharge StandardsParameter Mg/l

    TPH 20 ppmvChloride 500 (Rivers, lakes, reservoirs)Chrome (VI) 0.1Total Chrome 0.5Mercury 0.02Cadmium 0.1

    Arsenic 0.2Phenol for FCC discharge of refinery 0.5Sulphur for FCC discharge of refinery 1.0BOD 50COD 250Residual chlorine 0.2

    Ammoniac nitrogen 40Total Coniforms (NMP/100mL)

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    7 UTILITY

    7.1 Electrical

    7.1.1 Piraa CPF

    Nominal VoltageOperational

    voltageRange

    Neutral System Service

    Maximumvoltage dropat equipment

    terminalsInternal PowerGeneration6.6 kV AC 60 Hz(3ph 3 wire)

    5 % Earthed by Earthingtransformer

    Normal Power

    Internal Power

    Generation480V AC 60 Hz(3ph 3 wire)

    5 % Earthed by high

    impedance (ITsystem)Neutral notdistributed

    Emergency Power

    Power DistributionHV motors 5 %HV / LV transformers 5 %

    6.6 kV AC 60 Hz(3ph 3 wire)

    5 % Earthed by Earthingtransformer

    HV / HV transformers 5 %33 kV AC 60 Hz(3ph 3 wire)

    5 % Earthed trough animpedance

    Well pads supply 5 %

    MCCMain LV distribution

    2 %

    Motors 5 %

    480 V AC 60 Hz(3ph 3 wire)

    5 % IT system Withpermanent insulation

    monitoring

    Neutral notdistributed LV voltage transformer230 V AC UPS 2 %

    Lighting distribution boardLightings fittings 8 % max to the

    farthest fittingSmall distribution systemand socketsWelding sockets

    400/230 V AC 60 Hz(3ph 4 wire)

    5 % TNS neutral earthedand distributed

    Heat tracing and motorspace heaters

    230 V AC UPS 60 Hz(2 ph 2 wire)

    10 % Isolated IT systemWith permanent

    insulation monitoring(neutral notdistributed)

    Vital PowerControl and Safetysystems (PCS, PSS, ESDand FGS)Instrumentation,

    All telecommunicationsGenerator 48 V DC

    48 V DC(2 pole 2 wire)

    10 % Unearthed systemWith permanent

    insulation monitoring

    Vital PowerControl of HV and LVswitchgear

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    7.1.2 Curaray Terminal

    Nominal Voltage OperationalvoltageRange

    Neutral System Service

    Maximumvoltage dropat equipment

    terminalsInternal PowerGeneration480 V AC 60 Hz(3ph 3 wire)

    5 % Earthed by highimpedance (IT system)Neutral not distributed

    Normal powerEmergency power

    Power DistributionMCCMain LV distribution

    2 %

    Motors 5 %

    480 V AC 60 Hz(3ph 3 wire)

    5 % IT system Withpermanent insulation

    monitoringNeutral not distributed LV voltage transformer

    230 V AC UPS

    2 %

    Lighting distribution boardLightings fittings 8 % max to the

    farthest fittingSmall distribution systemand socketsWelding sockets

    400/230 V AC 60 Hz

    (3ph 4 wire)

    5 % TNS neutral earthedand distributed

    Heat tracing and motorspace heaters

    230 V AC UPS 60 Hz(2 ph 2 wire)

    10 % Isolated IT systemWith permanent

    insulation monitoring(neutral not

    distributed)

    Vital power:Control and Safetysystems (PCS, PSS, ESDand FGS)

    Instrumentation, All telecommunicationsGenerator 48V DC

    48 V DC(2 pole 2 wire)

    10 % Unearthed systemWith permanent

    insulation monitoring

    Vital power:Control LV switchgear

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    7.1.3 Piraa PPiX

    Nominal Voltage OperationalvoltageRange

    Neutral System Service

    Maximumvoltage dropat equipment

    terminalsPower Distribution

    33 kV AC 60 Hz(3ph 3 wire)

    5 % Earthed trough animpedance

    HV / LV transformers 5%

    MCCMain LV distribution

    2 %

    Motors 5 %

    480 V AC 60 Hz(3ph 3 wire)

    5 % IT system Withpermanent insulation

    monitoringNeutral notdistributed

    LV voltage transformer230 V AC UPS

    2 %

    Lighting distribution boardLightings fittings 8 % max to thefarthest fitting

    Small distribution systemand socketsWelding sockets

    400/230 V AC 60 Hz(3ph 4 wire)

    5 % TNS neutral earthedand distributed

    Heat tracing and motorspace heaters

    230 V AC UPS 60 Hz(2 ph 2 wire)

    10 % Isolated IT systemWith permanent

    insulation monitoring(neutral notdistributed)

    Vital PowerControl and Safetysystems (PCS, PSS, ESDand FGS)Instrumentation,TelecommunicationsGenerator 48 V DC

    48 V DC(2 pole 2 wire)

    10 % Unearthed systemWith permanent

    insulation monitoring

    Vital PowerControl of HV and LVswitchgear

    7.2 Fuel Gas

    7.2.1 Fuel Gas DesignThe fuel gas system design data is as follows:

    Design temperature (C) 115Operating Temperature (C) 50Design Pressure (barg) 13Operating Pressure (barg) 1.5 / 2LHV (MJ/Sm) 53.72 / 56.97Molecular Weight 33.49 / 35.07Filtration NoneWater Content (% mol) 5

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    7.2.2 Fuel Gas Composition

    Phase 0 - Dehydrator Train Phase 0 - Centrifuge Train Phase 1CO2 6.408205 6.493482 6.075222

    Nitrogen 9.684670 9.564435 10.434824Methane 44.223432 43.882450 47.399612Ethane 4.965198 5.040715 4.801487

    Propane 6.619640 6.734889 5.869281i-Butane 1.115466 1.132354 0.942265n-Butane 1.566770 1.588743 1.311905i-Pentane 0.395510 0.399531 0.329460

    n-Pentane 0.298777 0.301448 0.250440n-Hexane 0.225732 0.226365 0.203492Mcyclopentan 0.104592 0.104838 0.095726

    Benzene 0.017951 0.017990 0.016600Cyclohexane 0.042592 0.042634 0.040089

    n-Heptane 0.078663 0.078391 0.080358Mcyclohexane 0.034470 0.034355 0.035454

    Toluene 0.004761 0.004740 0.005072n-Octane 0.023971 0.023777 0.027556

    E-Benzene 0.001190 0.001180 0.001410m-Xylene 0.001266 0.001254 0.001517o-Xylene 0.000962 0.000953 0.001161

    C9* 0.007616 0.007539 0.009292

    C10* 0.002163 0.002138 0.002723C11* 0.000649 0.000641 0.000821C12* 0.000208 0.000205 0.000262C13* 0.000091 0.000090 0.000114C14* 0.000023 0.000023 0.000029C15* 0.000005 0.000005 0.000006C16* 0.000001 0.000001 0.000001C17* 0.000000 0.000000 0.000000C18* 0.000000 0.000000 0.000000C19* 0.000000 0.000000 0.000000

    C20+ - Cetico (UP)* 0.000000 0.000000 0.000000C20+ - Glauconitico* 0.000000 0.000000 0.000000

    C20+ - Dorado* 0.000000 0.000000 0.000000C20+ - Paiche* 0.000000 0.000000 0.000000

    H2O 4.113889 4.113583 4.117196NBP[0]-2* 3.162835 3.206155 2.699418

    NBP[0]-13* 2.711475 2.744036 2.298340NBP[0]-27* 2.832649 2.861083 2.406558NBP[0]-42* 3.097992 3.122127 2.669397NBP[0]-56* 2.740320 2.755021 2.424642NBP[0]-70* 2.262467 2.268112 2.090232NBP[0]-85* 1.610317 1.609505 1.573581NBP[0]-99* 0.942933 0.939588 0.984944

    NBP[0]-113* 0.458942 0.456120 0.511154NBP[0]-127* 0.180499 0.179002 0.212865NBP[0]-141* 0.048607 0.048134 0.059668NBP[0]-156* 0.010097 0.009988 0.012745NBP[0]-171* 0.002407 0.002379 0.003080

    Gas Composition% Mole

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    7.3 Diesel Oil

    7.3.1 Piraa CPF

    Design 6 bargPressure Working 2.4 /1.4 bargDesign min/max 43CTemperature Working Ambient

    CoarseFiltration 25 microns and larger

    WaterFiltration 15 ppm vol maximum

    7.3.2 Curaray Terminal

    Design 3.5 bargPressure Working 1.2 / 0.2 bargDesign 43CTemperature Working Ambient

    CoarseFiltration 25 microns and larger

    WaterFiltration 15 ppm vol maximum

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    7.3.3 Diesel Oil Composition

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    7.4 Crude Oil

    Design 18 / 93 CTemperature Working 50 CDesign min/max 5 bargPressure Working 2 / 0 barg

    Oil with naphta Oil after Heatingup at 150C

    Visco @ 25C cSt 620 3587Visco @ 50C cSt 175 601LHV - -flash point C 4,86 61,18Composition % molCO2 0,084826 0,00276849Nitrogen 0,005287 0,000164188Methane 0,049979 0,001512844Ethane 0,096708 0,003704652Propane 0,428802 0,026229212i-Butane 0,160902 0,01550549n-Butane 0,290779 0,032506046

    i-Pentane 0,161725 0,029511006n-Pentane 0,151795 0,030969857n-Hexane 0,350048 0,124953434Mcyclopentan 0,171287 0,063071872Benzene 0,029061 0,010481691Cyclohexane 0,089910 0,036942901n-Heptane 0,446226 0,254549926Mcyclohexane 0,187801 0,108644022Toluene 0,033373 0,019957972n-Octane 0,616425 0,50778124E-Benzene 0,038134 0,03238534

    m-Xylene 0,051320 0,045090525o-Xylene 0,044295 0,039946308C9* 0,647534 0,654480205C10* 0,909530 1,097653117C11* 0,991209 1,308808928C12* 1,063355 1,486928086C13* 1,454230 2,107318427C14* 1,425456 2,122521028C15* 1,508136 2,287233734C16* 1,379510 2,113085674C17* 1,347279 2,075596704C18* 1,416511 2,188390994C19* 1,396849 2,16115272C20+ - Cetico(UP)* 10,280147 15,94475274

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    C20+ -Glauconitico* 26,218735 40,66588383C20+ - Dorado* 0,000000 0,000000C20+ - Paiche* 0,000000 0,000000H2O 9,194673 0,028686397NBP[0]-2* 0,639348 0,079012188NBP[0]-13* 0,778508 0,117969406NBP[0]-27* 1,189893 0,224097841NBP[0]-42* 1,959300 0,459885395NBP[0]-56* 2,658552 0,771635288NBP[0]-70* 3,658208 1,333047775NBP[0]-85* 4,617904 2,10064298NBP[0]-99* 5,324140 3,021802787

    NBP[0]-113* 5,406859 3,73900863NBP[0]-127* 4,925860 4,085715026NBP[0]-141* 3,122222 2,99999371NBP[0]-156* 1,769961 1,942651105NBP[0]-171* 1,227407 1,495368276

    % mol 37,278162 22,370830Diluant% vol 16 7,51

    Additional compounds to be considered :Oil Oil + Naphta

    Sulfur 2.5 Wt% 2.3 Wt%Nickel 96 ppm 91 ppm

    Iron 11 ppm 6.4 ppm

    Vanadium 358 ppm 324 ppm

    Asphaltene (C7 insolubles) 11.9 Wt% 9.5 Wt%

    Salt 10 ptb max 10 ptb max

    BS& W 0.5 % 0.5 %

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    7.5 Instrument Air

    7.5.1 Piraa CPF

    Design 18C/72CTemperature Working 18.5C/38CDesign 11 bargPressure Working 9 barg

    Oil and Particle contents ISO 8573-1 Class2Water dew point ISO 8573-1 Class2

    7.5.2 Curaray Terminal

    Design 18C/72CTemperature Working 18.5C/38CDesign 10 bargPressure Working 8 barg

    Oil and Particle contents ISO 8573-1 Class2Water dew point ISO 8573-1 Class2

    7.5.3 Piraa PPiX

    Design 18C/72CTemperature Working 18.5C/38C

    Design 10 bargPressure Working 8 bargOil and Particle contents ISO 8573-1 Class2Water dew point ISO 8573-1 Class2

    7.6 Nitrogen

    Design 18C/72CTemperature Operating 18.5C/38CDesign 11 bargPressure Normal 7.7 barg

    Purity 98%Oil content Oil FreeWater Dew Point ISO 8573-1 Class2

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    7.7 Chemical Injection

    7.7.1 Piraa CPF

    7.7.1.1 Anti-Fouling

    Design min/max 18/43 CTemperature Operating AmbientDesign 15.6 bargPressure Normal Atm 10 barg

    7.7.1.2 Demulsifier:

    Design min/max 18/43 CTemperature Operating AmbientDesign 15.6 bargPressure Normal Atm 10 barg

    7.7.1.3 Anti-Foam

    Design min/max 18/43 CTemperature Operating AmbientDesign 15.6 bargPressureNormal Atm 13 barg

    7.7.1.4 Corrosion inhibitor

    Design min/max 18/43 CTemperature Operating AmbientDesign 15.6 bargPressure Normal Atm 13 barg

    7.7.1.5 Acid

    Design min/max 18/43 CTemperature Operating AmbientDesign 15.6 bargPressure Normal Atm 13 barg

    7.7.1.6 Biocide

    Design min/max 18/43 CTemperature Operating AmbientDesign 15.6 barg

    Pressure Normal Atm 13 barg

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    7.7.1.7 O2 scavenger

    Design min/max 18/43 CTemperature Operating AmbientDesign 15.6 bargPressure Normal Atm 13 barg

    7.7.1.8 Reverse Demulsifier

    Design min/max 18/43 CTemperature Operating AmbientDesign 15.6 bargPressure Normal Atm 13 barg

    7.7.1.9 High Temperature Oil Demulsifier

    Design min/max 18/43 CTemperature Operating AmbientDesign 15.6 bargPressure Normal Atm 13 barg

    7.7.1.10 High Temperature Corrosion Inhibitor

    Design min/max 18/43 CTemperature Operating AmbientDesign 15.6 bargPressure Normal Atm 13 barg

    7.7.2 Arabela River Water Pumpng Station

    7.7.2.1 Biocide

    Design min/max 18/43 CTemperature Operating AmbientDesign Tank Full of

    LiquidPressureNormal Atm

    7.7.3 Piraa PPiX

    7.7.3.1 Oil Demulsifier

    Design min/max 18/43 CTemperature Operating AmbientDesign 93 barg

    Pressure Normal 16 barg

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    7.7.3.2 Corrosion inhibitor

    Design 18/43 CTemperature Operating AmbientDesign 93 bargPressure Normal 16 47 barg

    7.7.4 Curaray Terminal

    7.7.4.1 Corrosion inhibitor

    Design 18/43 CTemperature Operating AmbientDesign 15.6 bargPressure Normal 3 barg

    7.7.4.2 Biocide

    Design min/max 18/43 CTemperature Operating AmbientDesign Tank Full of

    LiquidPressureNormal Atm

    7.8 Utility Water

    7.8.1.1 Piraa CPF

    Design 18 / 43CTemperature Working AmbientDesign 13 bargPressure Working 11 barg

    CoarseFiltration 100 microns

    Water shall be sourced to Piraa CPF from Arabela River. Water composition from Arabela River is resumedon the following table:

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    7.8.1.2 Curaray Terminal

    Design 18/43 CTemperature Working AmbientDesign 13 bargPressure Working 11 barg

    CoarseFiltration 100 microns

    Water shall be sourced to the Curaray Terminal from Curaray river. Water composition from Curaray River isresumed on the following table:

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    7.9 Potable water

    7.9.1 Potable Water Design data

    7.9.1.1 Piraa CPF

    Design 18/43 CTemperature Working Ambient

    Design 15 bargPressureWorking 6.7 barg

    7.9.1.2 Curaray Terminal

    Design 18/43 CTemperature Working Ambient

    Design 15 bargPressure Working 6.7 barg

    7.9.2 Potable Water Quality

    Potable water quality requirements are extracted from: El reglamento de la Calidad del Agua para ConsumoHumano from Peruvian Health ministry [5].

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    7.10 Fire Water

    7.10.1 Fire Water Design data

    7.10.1.1 Piraa CPF

    Design 18/43 CTemperature

    Working AmbientDesign 12.5 bargPressure Working 8.8 barg

    CoarseFiltration 100 microns

    7.10.1.2 Curaray Terminal

    Design 18/43 CTemperature

    Working Ambient

    Design Note 1Pressure Working Note 1Coarse

    Filtration 100 microns

    Note 1 : the firewater ring main at CT is not pressurised and dry during normal operation. When required, thering main is fed by two fire water pumps discharging firewater at 8.7 barg (working) minimum (12.5 bargdesign).

    7.10.2 Fire Water Composition

    Fire water composition is assumed to be the same as Curaray River for CT and as Arabela River for PiraaCPF.

    7.11 Foam

    Design min/max18/43 C

    TemperatureOperating AmbientDesign 10 barg Note 1

    Pressure Normal

    Note 1 ; To be confirmed by Vendor

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    7.12 MP Flare Network

    Max. Design 10 / 135 CTemperature

    Normal AMB

    Design 3.5 bargPressure

    Normal ATM

    7.13 LP Flare Network

    Max. Design 10 / 115 CTemperatureNormal AMB

    Design 3.5 bargPressure

    Normal ATM

    7.14 Thermal Oil

    Type and Characteristics To be confirmed by Fired HeaterSupplier

    Design Pressure (barg) 11.3Working Pressure (barg) 2 / 6Design Temperature (C) 18 / 270

    Working Supply Temperature(C) 230

    Working Return Temperature(C) 160