specifications equipment design conditions
TRANSCRIPT
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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