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FPSO Applications. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .

By Yasmin Bhuj, CCI

2 FPSO Applications | 788 ©2005 CCI. All rights reserved.

FPSO Applications By Yasmin Bhuj, CCI USA

Background

Floating Production Storage and Off-loading (FPSO) vessels have

become increasingly popular concepts in recent years. Their main

advantage is the ability to operate without the need for a specific

export infrastructure. Crude can be exported by shuttle tanker.

Gas however, must either be flared or exported by pipeline so

FPSO’s suit low Gas Oil Ratios (GOR) fields especially. Other

advantages include:

Relatively short schedules (oil tankers can be converted relatively cheaply)

Can often be leased instead of bought, hence making very small fields economic

Can be used in any water depth

Early production

Large payload/deck space

Easy to remove and reuse

FPSOs are popular, especially on marginal or small fields as

they are cheap (especially conversions of existing tankers). One

obvious disadvantage is they use subsea trees, and another is the

lack of drilling/ workover facilities (although there are proposals

for FDPSO- FPSOs with drilling capabilities). It is even possible

to hire them from companies such as Oceaneering or Bluewater

Economic Philosophy

Companies operating FPSOs generically aim to achieve the

following 1

Rapid Deployment: target for 12 months between contract

award and sail away from the conversion yard

Fast track production from new discoveries to accelerate

generation of revenues and increase reliability and

availability of production data for the full field

development

Turret mooring to allow tandem as well as calm buoy

off-loading

Cost Effectiveness: by high degree of vendor and operator

involvement in the early projects, and repeat ordering for

subsequent copy jobs

Standardization: By the generation of generic design

philosophies and specifications for equipment, control &

safeguarding systems, etc. All these specifications

can be tailored for a special project by separate “functional

specifications” and “general conditions and data

specifications”.

After the successful start up of FPSO Kuito and FPSO Espadarte

by the end of 1999, Single Buoy Moorings Inc. (SBM) and IHC

Gusto Engineering BV recognized the need to standardize FPSO

designs and incorporate lessons learned from previous projects.

Using their generic model (FPSO-2000) as an example, a basic

description of the typical process is given below. It was designed

An FSPO is essentially a ship shape floating production vessel

(often built from a converted oil tanker). The vessel is moored in

place and connected to the subsea wellheads by flexible risers. It

may be spread moored (in calm waters) or moored with a turret,

allowing the vessel to weather vane, in harsher waters.

Process facilities can be anything from just a 3 phase separator

train with gas to flare to full export process systems with full

water and gas injection systems: a big (say 50 m x 150 m) FPSO

has a lot of deck space!

FPSO are very flexible; they’ve been used in thousands of meters

of water offshore Brazil to a few meters of water offshore Nigeria;

they can cope with as few as 2 -3 wells to as many as 60 or so,

and throughputs can vary from a couple of thousand bbl/d to

hundreds of thousands bbl/d. Storage can also range from a few

thousand barrels to over a million barrels.

©2005 CCI. All rights reserved. 788 | FPSO Applications 3

to cope with a wide range of field properties, and water depths

up to a maximum of 2,100 metres. The FPSO would be suitable

for relocation between fields during its lifetime.

Conversion of the existing tanker for FPSO service life was based

on 10 year on-site life without dry docking and major steel

renewals. Design and construction of new topside facilities was

intended for a minimum of 15 years life.

General Set-up Considerations

Vessel Conversion

The primary selection criteria for a vessel conversion are:

Good Hull Condition

Minimum Steel Renewal

Traceable History

Lay Out Suitable for Conversion, i.e

• noadditionalbulkheadsrequired,

• possibilitytoextendaccommodation

• Boiler,SteamTurbines,Off-loadingPumpssuitablefor

refurbishment

The refurbishment may comprise the removal of:

All deck and cargo piping,

Accommodation interior,

Asbestos,

Superfluous equipment

Topsides Lay Out

Refer to the generic diagram1 on the top of page 4. The topsides

lay out is based on the following philosophy:

A central pipe rack supports a travelling crane and provides central walkway

Modules mounted 4 meters above main deck, on module supports pre-installed on the main deck

Maximum separation between hydrocarbon containing

modules and accommodation

The turret is the point around which the FPSO weather vanes

and at which all risers are gathered. The number of risers is the

key parameter which defines the diameter and size of the turret.

The turret is also the part of the FPSO which is moored to the

sea-bed. Any turret therefore has a “fixed” part (moored to the

sea-bed) and a rotating part (part of the hull). Water depth has

large impact on the design of the mooring system. The anchor

chain, anchor and winch designs are especially dependant on

riser weight and loads resulting from current, wind, etc. There are

many designs of turret available. Turrets can be designed to be

permanent or disconnectable. They may be external or internally

mounted; internally mounted turrets are more expensive but

can cope with higher sea states. The combined living quarters,

recreational facilities, sick bay and bridge are located in the

accommodation block. The lay out is such that ample room is

provided for installation of future facilities.

Process

Crude Oil Separation

Refer to the block diagram1 on page 4. For example, the

production facilities may comprise a single train, which features

three stages of separation and stabilization. After bulk separation

in the HP Separator, the crude is heated to 80° C, and stabilized

in the IP and LP Separator. After stabilization, the crude is

dehydrated to specification using an electrostatic coalescer.

Produced water is flashed at near atmospheric pressure and

stored in the slop tanks for gravity settling and if required

hydrocyclone treating [on line or batch]. Ultimately, produced

water is disposed of overboard. Crude oil is stored temporarily

and produced water is disposed of overboard after final treatment

in the slop tanks.

Wash water is injected downstream of the LP Separator to reduce

the salt content of the crude within specifications. Wash water

is desalinated seawater, using reverse osmosis as desalination

method.


Chemical Injection

Extensive provisions for chemical injection include methanol,

pour points depressant, corrosion inhibitor, foam inhibitor,

demulsifier, scale inhibitor, etc. A dedicated chemical injection

module is provided for water injection purposes.

Nitrogen

A nitrogen generator is provided to increase availability of large

quantities of nitrogen offshore West Africa.

Fuel Gas and marine gas oil (MGO) System

Fuel gas is normally extracted immediately downstream of the

TEG Contactor, upstream of the final compression stage. Despite

the low dewpoint of the gas after dehydration at 140 bar /45° C,

20° C superheat is continuously maintained for protection of

turbomachinery and ease of operation.

In addition each FPSO will have it’s own particular features

dictated by the terrain in which it is situated. See the case study

below for a specific example.

Gas Compression, Treatment and Disposal

Reservoir pressure is maintained by gas injection, thus

minimizing flaring. All gas in excess of fuel gas is available for

reinjection. Gas lift is available via an extraction point on the

injection header.

The 2x 50% capacity main gas compressors receive gas from

the HP Separator and Flash Gas Compressor. These three stage,

common shaft, centrifugal compressors are driven by industrial

type gas turbines, iso-rated at 13.4 MW.

The 1x 100% capacity Flash Gas Compressor receives gas

from the IP – and LP- Separator. The two stage, oil free screw

compressor is driven by a 2.5 MW HV electric motor with

variable speed drive.

Gas dehydration to -10° C dewpoint at 310 bar is achieved by

conventional triethylene glycol (TEG) dehydration, which is

located upstream the 3rd compression stage. The TEG contactors,

operating at 140 barg, are dedicated for each compressor but

feature common TEG regeneration.

Utilities

Cooling & Heating Medium System

The Cooling and Heating medium systems are closed loop,

[inhibited] water based systems in which the driving force is

provided by seawater and low pressure steam from the vessel

system.

Power Generation

Electrical Power is provided by two, 100% capacity industrial

type gas turbines, 6.5 MW iso-rated. Emergency and Essential

Power Generators are provided in the engine room and below

the helideck.


Case Study

Terra Nova FPSO 2

The Terra Nova field is being developed using a Floating

Production Storage and Off-loading (FPSO) vessel. This vessel is

a ship-shaped production platform with integrated oil storage

from which oil is off-loaded to a shuttle tanker.

One of the largest Floating Production Storage and Off-loading

vessels ever built, the Terra Nova FPSO is 292.2 metres long and

45.5 metres wide (about the size of three football fields laid

end to end). From the keel to the helideck it stands more than

18 storeys high. The vessel can store 960,000 barrels of oil and

accommodate up to 80 personnel.

The wellheads and production manifolds are placed in glory

holes – excavations in the sea floor – that protect the equipment

from scouring icebergs.

Production System

Oil production wells are pre-drilled by a semi-submersible

drilling platform such as the one below.

A network of more than 40 kilometers of flexible flowline is used

to convey hydrocarbons to and from the wells. Produced gases

are separated from the oil and re-injected into the reservoir for

possible future extraction.

The connection between the FPSO and the subsea flowlines is

the spider buoy (the lower portion of the turret). The spider

buoy is the mooring point for the FPSO, and the pathway for

oil and fluids that flow to and from the FPSO and reservoir. The

spider buoy has a quick-disconnect feature, allowing the FPSO to

disconnect and leave the area in an emergency situation like the

approach of an iceberg. Crude oil is off-loaded from the FPSO

onto large shuttle tankers, which then move the oil to market.

Design, construction and installation of the FPSO, subsea

components and pre-production wells were carried out by a

consortium of companies comprising Petro-Canada, AGRA

Brown & Root, Hallibuton Energy Services, FMC Offshore

Canada Ltd., PCL Industrial Constructors Inc., Technip Coflexip,

and Doris ConPro Ltd


CCI FPSO Projects

We have worked on three main FPSO projects to date.

These are:

Connoco Phillips Belanak, South East Asia

ExxonMobil Saipem SA Erha, Nigeria

ExxonMobil Kizomba, Angola

The projects are described in more detail below. A

summary of the applications is given on page 9. See

also the data sheets starting on page 10.

Connoco Phillips Belanak, March 2003

Applications: Compressor Recycle

This vessel is located in the South China Sea off

Natuna Island, roughly 200 kilometers northeast

of Singapore, and is one of the most sophisticated

production facilities in the world. The vessel produces

approximately 7,800 standard barrels per day of

butane and 14,700 standard barrels per day of propane

plus 430 million standard cubic feet of gas and

100,000 barrels of oil.

CCI supplied seven anti-surge control valves for the

FPSO vessel’s LPG unit. These valves are considered

the most critical control valves on the FPSO because

they protect over $20 million worth of compressors.

Stringent specification requirements demanded

that CCI implement specialized design and control

measures, and the valves were custom designed for

each application. For example, while carbon steel is

a typical material for these types of valves, CCI used

duplex stainless steel for the FPSO valves since this

extra-hard material is the best substance available for

preventing corrosion in the valve body and bonnet.

Corrosion is a significant concern on the FPSO unit

because both the highly acidic fluid it handles and the

saltwater contribute to corrosion. The duplex material,

however, should allow the valves to resist corrosion

even when exposed to a salt-air environment.

The valves were also created to achieve repeatable Class

V super-tight shutoff, made possible by the pneumatic

actuator providing thrust of over 500 pounds per

linear inch. Preventing leakage and boosting overall

efficiency, this tight shutoff translates directly into

operational cost savings for the FPSO. Another special

feature of the valves supplied by CCI is their fast stroke

speed. The valves were designed to stroke in less than

one second under trip conditions and less than two

seconds in modulation. This stroke speed allows the


user to run the compressor close to the surge line for increased

efficiency. Finally, designed with 10 to 16 pressure-reducing

stages, the valves feature CCI’s unique DRAG® technology for

superior velocity and noise control to eliminate vibration and

the possibility of mechanical failure.

ExxonMobil Saipem SA Erha, July 2003

Applications

HP Separator Oil Train

Gas Injection to Flow Line to Drill

Flow Line Pigging

HP Compressor Master Controller

Water Injection Pump Minimum Flow

Methanol Header Pressure Control

Methanol Injection Pump Discharge

Gas Lift Manifold Control

HP Compressor Suction Pump

Dehydrator Train

CCI won a million-dollar-plus order from Saipem SA France

to supply 23 control valves to Exxon Mobil’s Erha FPSO vessel.

The 2,200,000-barrel FPSO will be located in the Erha field, 90

kilometers offshore Nigeria. The 23 valves to be supplied by CCI

are for high-pressure applications and range from 900 to 10,000

psi, 1” to 20” in diameter and carbon steel to duplex.

ExxonMobil Kizomba, September 2003

Applications

Test Flow Line Choke Valve

Production Stand-By Choke Valve

Kizomba lies in one of the first stretches of deepwater acreage

offered by the Angolan Government. The development

consortium is operated by ExxonMobil's subsidiary, Esso

Exploration Angola, which has a 40% stake in the field. The

partners also include Agip Angola (with a 20% share), BP

Exploration (with a 26.67% share) and Statoil (with a 13.33%

share). Sonangol, the Angolan State oil company, is the

concessionaire. Kizomba B will develop the Kissanje and Dikanza

discoveries in water depths of 3,300 ft to 3,400 ft. The project

will include the combination of a surface wellhead platform and

subsea wells tied back to an FPSO vessel3.


Endnotes

1 EPS Project “A”: FPSO Falcon, Design Challenges and Successful

Start-up of the first Generic FPSO design, Andries Mastenbroek

and Mattieu Ubas of HIC Gusto Engineering

2 http://www.petro-canada.ca/eng/about/business/8956.htm,

12/06/2004

3 http://www.offshore-technology.com/projects/kizomba/,

11/25/2004

Typical Applications Summary

Application Why Severe service Solution Recommended

Compressor RecycleReliability, Noise, Vibration, Leakage, Fast Stroking Speed

DRAG®

<85 dBATrim exit velocity head<70 psiShut-off Class V Stroke speed <1 s

Dehydrator Train Vibration, Noise Trim exit velocity <100 ft/s

Flow Line Pigging(gas/liquid duty)

Reliability, Leakage, VibrationShut-off: Class VTrim exit velocity <75 ft/sTrim exit velocity head 70 psi

Gas Injection to Flowline to Drill Reliability, Noise, VibrationDRAG®

Trim exit velocity head<70 psi

Gas Lift Manifold Control Reliability, Noise, VibrationDRAG®


HP Compressor Master Controller Reliability, Noise, VibrationDRAG®


HP Separator Oil TrainHigh Pressure, High Capacity, Vibration

High capacity cage guided valve

3rd Stage HP Compressor Suction PumpFlashing, Leakage, Erosion, Vibration

DRAG®

Shut-off: Class V Trim exit velocity <100 ft/s

Methanol Header Pressure Control Vibration DRAG®

Trim exit velocity<100 ft/s

Methanol Injection Pump Discharge Cavitation, Vibration, NoiseDRAG®


Production Standby Choke Valve(liquid/gas duty)

Multiphase Flow, Vibration, Erosion

DRAG®

Hard faced trimTrim exit velocity head<70 psi

Test Flowline Choke Valve(liquid/gas duty)

Multiphase Flow, Vibration, Erosion

DRAG®

Hard faced trimTrim exit velocity head<70 psi

Water Injection Pump Minimum Flow (Recirculation)

Cavitation, Vibration, NoiseDRAG®


Seawater Injection Pump DischargeCavitation, Vibration, Noise

DRAG®


Injection Compressor Suction Header To Hp FlareNoise, Vibration

DRAG®

Trim exit velocity<70 psi


CONTROL VALVE DATA SHEETProject Belanak FPSO Development Tag # T23FV 3165A/BCustomer Halliburton Far East Pte. Ltd Item # 01/02Ult. Client Conoco Indonesia Qty. 2Inq. TIC-36 Rev. Date 04-JUN-02 Model 100DProp. 010623-003040 Rev. Date 25-Jun-02 D-SHT Rev. 4 Dwg # 200679-1P.O. CNCO-BELK-PTIC36 Application LP compressor A/B Surge Control

1 Fluid Gas - Customer Defined Crit Press psi A Crit Temp deg FUnits Cond 1 Cond 2 Cond 2 Shut-off

2 Mass Flow Rate lbm/hr 319232 298816 250659 3 Inlet Pressure (P1) psi A 900.0 860.0 840.0 4 Outlet Pressure (P2) psi A 360.0 315.0 375.0 5 Differential (∆P) psi 540.0 545.0 465.0 18006 Inlet Temp. (T1) deg F 261 269 257 7 Molecular Weight 22.36 23.66 19.02 8 Compressibility 0.9500 0.9400 0.9600 9 Ratio of Spec. Heat 1.234 1.22 1.263 10 Required Flow Cv 169 160 157 11 Travel % 60 58 57 12 SPL dBA <85 <85 <85 13 Pipe In 8in (200mm) Sch 60 38 Actuator Type Pneumatic Double Acting Piston14 Pipe Out 8in (200mm) Sch 60 39 Mfr / Model CCI /200 sq.in.15 Pipe Matl In UNS 31803 Out UNS S31803 40 Failure Mode Fail Open via Spring16 Type Globe Size 8 X 8 inches 41 Supply Type Instrument Compressed Air17 Design P In 1800 Out 1800 psi G 42 Supply (Min) 80 psi G18 Design T In 450 Out 450 deg F 43 Supply (Max) 150 psi G19 Rating(s) In 900 Standard Out 900 Standard 44 Stem Orientation Vertical Up20 Material A890 Gr.6A / F51 45 Manual Override N/A21 Connect In RTJ Flange Integral to Body 46 Yoke material: Stainless Steel (A351-CF8M)22 Connect Out RTJ Flange Integral to Body 47 Positioner Type Smart23 Flow Dir. Flow to Open (UTP) 48 Mfr / Model Fisher / DVC601024 Bonnet Type Bolted 49 Input Signal 4-20 mA25 Bonnet Seal Standard 50 Increasing Signal Closes the Valve26 Packing Type Standard 51 Cam Characteristic Linear27 Packing Matl Teflon 52 Certified by CENELEC EEx’ia’ IIC T4, IP 6528 Trim Type Drag, Multi-Path, Multi-Stage 53 Filter (Filter Reg) Norgren B3829 Trim Size 6 inches Rated Cv 290 54 Limit/Torque Switch 1 Open and 1 Closed30 Trim Char. Linear 55 Position Feedback Yes, 4-20 mA31 Number of Pressure Reducing Stages 16 56 I - P Transducer N/A32 Plug Type Balanced 57 Solenoid Valve(s) 2 in series for Trip Open33 Stem Matl F51 58 Elect Housing STD See Line 74 & 7534 Plug Matl F51, Stellited 59 Seat Leakage ANSI/FCI Class V35 Seat Matl F51, Stellited 60 Open Time(s) <2 sec Modulation, <1 sec Trip36 Guide Matl F51 61 Close Time(s) <10 sec37 Max Press./Max Temp. 1800 psig/425 degF 62 Approx. Weight 3500 lbs

N o t e s / S p e c i a l I n s t r u c t i o n s63 To eliminate uncontrolled pressure letdown problems, a number of discrete pressure reduction stages are provided.64 The fluid Kinetic Energy (Velocity Head) exiting the trim will not exceed 70 psi (4.8 Bar).65 To maximize the noise attenuating benefits, flow direction will be flow to open.66 All noise levels shown above are based on no thermal or acoustic padding on the downstream pipe.67 To prevent flow induced vibration, Pressure Equalizing Rings (PER) are provided to assure equal pressure around the plug.68 For easy maintenance, the trim is a quick change type. No components are screwed or welded to the body or bonnet.69 Valve design to ASME B16.34, latest edition.70 Wetted parts per NACE STD MR-01-75.71 Control valve sizing is based on ISA S75.01, ‘Flow Equations For Sizing Control Valves’.72 Hardware capacity shown above assumes 70% over capacity margin73 Tubing is 316Ss with +2.5%Mo, Imperial size. Fittings are Swagelok, 316SS.74 Limit switches are two wire proximity type, EEx’ia’ IIB T3, IP66 P&F NJ2-11NG with Westlock model 3479 boxes..75 Solenoid valve is Maxseal, EExd, IP66 316SS material body/trim.76 Actuator and pneumatic components are suitable for max. air pressure of 150 psig.77 Flange groove finish 63 microinch.


CONTROL VALVE DATA SHEETProject ERHA FPSO-EPC1 Tag # 1-LV-66108-1Customer SAIPEM SA Item # 10Ult. Client ESSO E & P NIGERIA Qty. 1Inq. T122010-PRT-11.01-044 Rev. Date Model 10OGDProp. 030124-152154 Rev. Date D-SHT Rev. 4 Dwg # 200903-4P.O. Application Dehydrater Train 1 / 2

1 Fluid TEG Crit Press 20.46 Bar A Crit Temp - deg CUnits @ Norm. Flow Shut Off

2 Mass Flow Rate kg/hr 5200.0 3 Inlet Pressure (P1) Bar G 72.6 4 Outlet Pressure (P2) Bar G 2.5 5 Differential (∆P) Bar 70.1 160.06 Inlet Temp. (T1) deg C 38.5 7 Density kg/m3 1117.0 8 Vapor Pressure Bar G 72.6 9 Viscosity cpoise 16.3 10 Required Flow Cv 1.2 11 Travel ~80 12 SPL dBA <85 13 Pipe In 3in (75mm) Sch 160 38 Actuator Type Spring Diaphragm14 Pipe Out 3in (75mm) Sch 160 39 Mfr / Model CCI / 400RA15 Pipe Matl In Carbon Steel Out Carbon Steel 40 Failure Mode Fail Close16 Type Angle Size 1.0 X 1.0 inches 41 Supply Type Compressed Air17 Design P In 160.0 Out 160.0 Bar G 42 Supply (Min) 5.5 Bar G18 Design T In -45.0/95.0 Out -45.0/95.0 deg C 43 Supply (Max) 7.0 Bar G19 Rating(s) In 1500 Standard Out 1500 Standard 44 Stem Orientation Vertical Up20 Material LF2 / LF2 45 Manual Override N/A21 Connect In RTJ Flange 46 22 Connect Out RTJ Flange 47 Positioner Type Smart Positioner w/ Hart Protocol23 Flow Dir. Flow to Close (OTP) 48 Mfr / Model Fisher / DVC600024 Bonnet Type Bolted 49 Input Signal 4 to 20 mA25 Bonnet Seal Standard 50 Increasing Signal To Open the Valve26 Packing Type Standard 51 Cam Characteristic Linear27 Packing Matl Grafoil 52 28 Trim Type Drag, Multi-Path, Multi-Stage 53 Filter (Filter Reg) Fisher 67CFR29 Trim Size 3/8 inches Rated Cv 1.4 54 Limit/Torque Switch N/A30 Trim Char. Linear 55 Position Feedback N/A31 Number of Pressure Reducing Stages Min. 4 Stages 56 I - P Transducer N/A32 Plug Type Unbalanced 57 Solenoid Valve(s) N/A33 Stem Matl Inconel 718 58 Elect Housing STD EExd IIA T3, IP 5634 Plug Matl Inconel 718 59 Seat Leakage ANSI/FCI Class IV35 Seat Matl 316L SS 60 Open Time(s) < 10 sec36 Guide Matl Inconel 718 61 Close Time(s) < 10 sec37 62 Approx. Weight 165kg (365lbs) lbs

N o t e s / S p e c i a l I n s t r u c t i o n s63 Hardware capacity shown above assumes 25% over capacity margin.64 To eliminate uncontrolled pressure letdown problems, a number of discrete pressure reduction stages are provided.65 The liquid velocity exiting the trim will not exceed 100 ft/sec (30 m/sec).66 To prevent line trash damage to seating surfaces, the flow direction will be flow to close.67 To prevent flow induced vibration, Pressure Equalizing Rings (PER) are provided to assure equal pressure around the plug.68 For easy maintenance, the trim is a quick change type. No components are screwed or welded to the body or bonnet.69 Valve design to ASME B16.34, latest edition.70 Control valve sizing is based on ISA S75.01, ‘Flow Equations Sizing Control Valves’.71 72 73 74 75


CONTROL VALVE DATA SHEETProject ERHA FPSO-EPC1 Tag # 1-PV-54200-1 / 2Buyer Saipem SA Item # 16Owner Esso E & P Nigeria Qty. 2

Inq. T122010-PRT-11.01-044 Rev. 0 Date Model 100 DProp. 030124-152154 Rev. 0 Date 12 Feb 2003 D-SHT Rev. 2 Dwg # 200903-16P.O. Application Flow Line Pigging

1 Fluid Liquid / Gas Crit Press 0.00 Bar A Crit Temp Units Liquid Flow Fluid 1 Fluid 3 Fluid 5 Shut Off

2 Liquid Mass Flow kg/hr 214200 142000 119000 96350 3 Gas Mass Flow Rate kg/hr 30500 67000 81800 4 Inlet Pressure (P1) Bar G 96.0 96.0 96.0 96.0 5 Outlet Pressure (P2) Bar G 42.0 48.0 48.0 48.0 313.86 Differential (∆P) Bar 54.0 48.0 48.0 48.0 7 Inlet Temperature deg C 46.0 46.0 46.0 46.0 8 Liquid Vapor Press Bar A 0.9000 0.9000 0.9000 0.9000 9 Liquid Density kg/m3 850.0 850.0 850.0 850.0 10 Molecular Weight 19.0 19.0 19.0 11 Ratio of Spec. Heat 1.3 1.3 1.3 12 Compressibility 0.81 0.81 0.81 13 Required Flow Cv 37.36 59.26 84.19 89.39 14 Travel % ~31% ~49% ~70% ~75% 15 SPL dBA 75.0 16 Pipe In 10in (250mm) Sch 160 41 Actuator Type Pneumatic Double Acting Piston17 Pipe Out 10in (250mm) Sch 160 42 Mfr / Model CCI / Standard18 Pipe Matl In Carbon Steel Out Carbon Steel 43 Failure Mode Fail Open19 Type Angle Size 6 X 6 inches 44 Supply Type Compressed Air20 Design P In 314.0 Out 314.0 Bar G 45 Supply (Min) 5.5 Bar G21 Design T In 0.00/121.0 Out 0.00/121.0 deg C 46 Supply (Max) 7.0 Bar G22 Rating(s) In 2500 Std PN 420 Out 2500 Std PN 420 47 Stem Orientation Vertical Up23 Material A350-LF2/ A350-LF2 48 Manual Override Top Mounted Side Access24 Connect In RTJ Flange 49 25 Connect Out RTJ Flange 50 Positioner Type Smart Positioner w/ Hart Protocol26 Flow Dir. Flow to Close (OTP) 51 Mfr / Model Fisher / DVC 600027 Bonnet Type Bolted 52 Input Signal 4 to 20 mA28 Bonnet Seal Standard 53 Increasing Signal To Close the Valve29 Packing Type Standard 54 Cam Characteristic Linear30 Packing Matl Teflon 55 31 Trim Type Drag, Multi-Path, Multi-Stage 56 Filter (Filter Reg) Fisher 67CFR (Filter - Reg)32 Trim Size 4.0 inches Rated Cv 120 57 Limit/Torque Switch N/A 33 Trim Char. Linear 58 Position Feedback N/A 34 Number of Pressure Reducing Stages 6 59 I - P Transducer N/A 35 Plug Type Balanced 60 Solenoid Valve(s) N/A 36 Stem Matl 316 SS 61 Elect Housing STD Per Specification37 Plug Matl 316 SS 62 Seat Leakage ANSI/FCI Class V38 Seat Matl 316 SS 63 Open Time(s) < 12 sec39 Guide Matl 316 SS 64 Close Time(s) < 12 sec40 65 Approx. Weight 1200 Kg

N o t e s / S p e c i a l I n s t r u c t i o n s66 Hardware capacity shown above assumes 25% over capacity margin.67 Wetted parts per NACE STD MR-01-75.68 To eliminate uncontrolled pressure letdown problems, a number of discrete pressure reduction stages are provided.69 The liquid velocity exiting the trim will not exceed 100 ft/sec (30 m/sec).70 To prevent line trash damage to seating surfaces, the flow direction will be flow to close.71 To prevent flow induced vibration, Pressure Equalizing Rings (PER) are provided to assure equal pressure around the plug.72 For easy maintenance, the trim is a quick change type. No components are screwed or welded to the body or bonnet.73 Valve design to ASME B16.34, latest edition.74 Control valve sizing is based on ISA S75.01, ‘Flow Equations For Sizing Control Valves’.75


CONTROL VALVE DATA SHEETProject ERHA FPSO-ECP1 Tag # 1-PV-65300-1Owner SAIPEM S.A. Item # 8Buyer ESSCO E&P NIGERIA Qty. 1Inq. T122010-PRT-11.01-044 Rev. 0 Date Model 100DProp. 030124-152154 Rev. 0 Date 12Feb2003 D-SHT Rev. 4 Dwg # 200903-8P.O. t122010/opi/prt/11.10 Application Gas Injection Flowline To Drill Center 3/4

1 Fluid Gas - Customer Defined Crit Press Bar G Crit Temp deg CUnits MAX NORM Min Flow Min Flow 2 Shut-Off

2 Mass Flow Rate kg/hr 500000 329361 83060 157650 3 Inlet Pressure (P1) Bar G 380.6 380.6 380.6 380.55 4 Outlet Pressure (P2) Bar G 380.1 315.95 226.0 282.9 5 Differential (∆P) Bar 0.50 64.65 154.6 97.65 4586 Inlet Temp. (T1) deg C 65.0 65.0 65.0 65.0 7 Molecular Weight 19.7 19.7 19.7 19.7 8 Compressibility 0.9690 0.9690 0.9690 0.9690 9 Ratio of Spec. Heat 1.61 1.61 1.61 1.61 10 Required Flow Cv 1561 95.1 16.7 38.1 11 Travel ~80% ~25% ~20% ~22% 12 SPL dBA 75.0 75.0 75.0 75.0 13 Pipe In 20in (500mm) Sch 160 38 Actuator Type Pneumatic Double Acting Piston14 Pipe Out 20in (500mm) Sch 160 39 Mfr / Model CCI / Standard15 Pipe Matl In Carbon Steel Out Carbon Steel 40 Failure Mode Fail close16 Type Angle Size 18 X 18 inches 41 Supply Type Compressed Air17 Design P In 458.0 Out 458.0 Bar G 42 Supply (Min) 5.5 Barg18 Design T In -45.0/82.0 Out -45.0/82.0 deg C 43 Supply (Max) 7.0 Barg19 Rating(s) In API 10000 Std Out API 10000 Std 44 Stem Orientation Vertical Up20 Material AISI 4130/ 4130 45 Manual Override N/A21 Connect In API 10000 Hub (TECHLOK) 46 22 Connect Out API 10000 Hub (TECHLOK) 47 Positioner Type Smart Positioner W/ Hart Protocol23 Flow Dir. Flow to Open (UTP) 48 Mfr / Model Fisher/ DVC 600024 Bonnet Type Bolted 49 Input Signal 4-20 mA25 Bonnet Seal Standard 50 Increasing Signal To Open The Valve26 Packing Type Standard 51 Cam Characteristic Linear27 Packing Matl Teflon with Graphoil Ring 52 28 Trim Type Drag®, Multi-Path, Multi-Stage 53 Filter (Filter Reg) Norgren B73G29 Trim Size 12.0 inches Rated Cv 1960 54 Limit/Torque Switch NA 30 Trim Char. Bi-Linear 55 Position Feedback N/A 31 Number of Pressure Reducing Stages 12 56 I - P Transducer N/A 32 Plug Type Balanced 57 Solenoid Valve(s) N/A 33 Stem Matl INC 718 58 Elect Housing STD EExd IIA T3, IP 5634 Plug Matl 316 SS 59 Seat Leakage ASME/FCI Class IV35 Seat Matl 316 SS 60 Open Time(s) <3036 Guide Matl INC 718 Disk W/ Cage (17-4PH) on top 61 Close Time(s) <3037 62 Approx. Weight lbs

N o t e s / S p e c i a l I n s t r u c t i o n s63 Hardware capacity shown above assumes 25% over capacity margin.64 65 To eliminate uncontrolled pressure letdown problems, a number of discrete pressure reduction stages are provided.66 The fluid Kinectic Energy (Velocity Head) existing the trim will not exceed 70 psi (4.8 Bar).67 To maximize the noise attenuating benefits, flow direction will be flow to open.68 All noise levels shoen above are based on no thermal or acoustic padding on the downstream pipe.69 To prevent flow induced vibration, Pressure Equalizing Rings (PER) are provided to assure equal pressure around the plug.70 For easy maintenance, the trim is a quick change type. No componnets are screwed or welded to the body or bonnet.71 Valve design to API 6A, latest Edition.72 Control valve sizing is based on ISA S75.01, “Flow Equation s For Sizing Control Valves”.73 74 75


CONTROL VALVE DATA SHEETProject Erha FPSO-EPC1 Tag # 1-FV-65403-1Owner Saipem SA Item # 17Buyer Esso E & P Nigeria Qty. 1Inq. T122010-PRT-11.01-044 Rev. 1 Date Model 100 DProp. 030124-152154 Rev. 1 Date 5 Sept 03 D-SHT Rev. 8 Dwg # 200903-9P.O. Application Gas Lift Manifold Control

1 Fluid Gas - Customer Defined Crit Press Bar G Crit Temp deg CUnits MAX NORM MIN

2 Mass Flow Rate kg/hr 9804 5880 980 3 Inlet Pressure (P1) Bar G 183 183 183 4 Outlet Pressure (P2) Bar G 112 144 42 5 Differential (∆P) Bar 71 39 141 6 Inlet Temp. (T1) deg C 37.8 37.8 37.8 7 Molecular Weight 19.7 19.7 19.7 8 Compressibility .742 .742 .742 9 Ratio of Spec. Heat 1.88 1.88 1.88 10 Required Flow Cv 3.6 2.7 .28 11 Travel ~72% ~54% ~20% 12 SPL dBA 75.0 75.0 75.0 13 Pipe In 4in (100mm) Sch XXS 38 Actuator Type Spring Diaphragm14 Pipe Out 4in (100mm) Sch XXS 39 Mfr / Model CCI / Standard15 Pipe Matl In Carbon Steel Out Carbon Steel 40 Failure Mode Fail Close16 Type Globe Size 2 X 2 inches 41 Supply Type Compressed Air17 Design P In 200.0 Out 200.0 Bar G 42 Supply (Min) 5.5 Bar G18 Design T In 0/200 Out 0/200 deg C 43 Supply (Max) 7.0 Bar G19 Rating(s) In 2500 Out 2500 44 Stem Orientation Vertical Up20 Material A350-LF2/ A350-LF2 45 Manual Override N/A21 Connect In RTJ Flange 46 22 Connect Out RTJ Flange 47 Positioner Type Smart HART23 Flow Dir. Flow to Open (UTP) 48 Mfr / Model Fisher / DVC 6000 Series24 Bonnet Type Bolted 49 Input Signal 4 to 20 mA25 Bonnet Seal Gasket 50 Increasing Signal To Open the Valve26 Packing Type Standard 51 Cam Characteristic Linear27 Packing Matl Grafoil 52 28 Trim Type Drag®, Multi-Path, Multi-Stage 53 Filter (Filter Reg) Fisher 67CFR29 Trim Size 1 Inch Rated Cv 5 54 Limit/Torque Switch N/A30 Trim Char. Equal Percentage 55 Position Feedback N/A 31 Number of Pressure Reducing Stages 16 56 I - P Transducer N/A 32 Plug Type Balanced 57 Solenoid Valve(s) N/A 33 Stem Matl Inconel 718 58 Elect Housing STD Per Specification34 Plug Matl Inconel 718 59 Seat Leakage ASME/FCI Class IV35 Seat Matl 316 SS 60 Open Time(s) < 4 sec36 Guide Matl Inconel 718 61 Close Time(s) < 4 sec37 62 Approx. Weight 350 kgs

N o t e s / S p e c i a l I n s t r u c t i o n s63 Hardware capacity shown above assumes 25% over capacity margin.64 To eliminate uncontrolled pressure letdown problems, a number of discrete pressure reduction stages are provided.65 The fluid Kinetic Energy (Velocity Head) exiting the trim will not exceed 70 psi (4.8 Bar).66 To maximize the noise attenuating benefits, flow direction will be flow to open.67 All noise levels shown above are based on no thermal or acoustic padding on the downstream pipe.68 To prevent flow induced vibration, Pressure Equalizing Rings (PER) are provided to assure equal pressure around the plug.69 For easy maintenance, the trim is a quick change type. No components are screwed or welded to the body or bonnet.70 Valve design to ASME B16.34, latest edition.71 Control valve sizing is based on ISA S75.01, ‘Flow Equations For Sizing Control Valves’.72 73 74 75


CONTROL VALVE DATA SHEETProject ERHA FPSO-EPC1 Tag # 1-PV-65100-1BCustomer Saipem SA Item # 12Ult. Client Esso E & P Nigeria Qty. 1Inq. T122010-PRT-11.01-044 Rev. 0 Date Model 100DProp. 030124-152154 Rev. 0 Date 12 Feb 2003 D-SHT Rev. 6 Dwg # 200903-5P.O. Application HP Compressor Master Controller

1 Fluid Gas - Customer Defined Crit Press Bar G Crit Temp deg CUnits @ Max Flow @ Norm Flow @ Min Flow Shut Off

2 Mass Flow Rate kg/hr 166000 146800 49800 3 Inlet Pressure (P1) Bar G 381.3 380.5 381.3 4 Outlet Pressure (P2) Bar G 36.0 28.1 36.0 5 Differential (∆P) Bar 345.3 352.4 345.3 458.16 Inlet Temp. (T1) deg C 65.0 65.0 65.0 7 Molecular Weight 19.6 19.6 19.6 8 Compressibility 0.9690 0.9690 0.9690 9 Ratio of Spec. Heat 1.61 1.61 1.61 10 Required Flow Cv 27.6 24.3 8.3 11 Travel % ~79% ~69% ~24% 12 SPL dBA 80.5 82.2 75.0 13 Pipe In 10in (250mm) Sch 160 38 Actuator Type Pneumatic Double Acting Piston14 Pipe Out 16in (400mm) Sch 160 39 Mfr / Model CCI / Standard15 Pipe Matl In Carbon Steel Out Carbon Steel 40 Failure Mode Fail Close16 Type Z-Globe Size 5-1/8 X 5-1/8 inches 41 Supply Type Compressed Air17 Design P In 458.0 Out 458.0 Bar G 42 Supply (Min) 5.5 Bar G18 Design T In -45/200 Out -45/200 deg C 43 Supply (Max) 7.0 Bar G19 Rating(s) In API 10000 Std Out API 10000 Std 44 Stem Orientation Vertical Up20 Material AISI 4130 / 4130 45 Manual Override N/A21 Connect In API 10000 Hub (TECHLOK 6IN 46ST) 46 22 Connect Out API 10000 Hub (TECHLOK 6IN 46ST) 47 Positioner Type Smart Positioner w/ Hart 23 Flow Dir. Flow to Open (UTP) 48 Mfr / Model Fisher / DVC 600024 Bonnet Type Bolted 49 Input Signal 4 to 20 mA25 Bonnet Seal Standard 50 Increasing Signal To Open the Valve26 Packing Type Standard 51 Cam Characteristic Linear27 Packing Matl Grafoil 52 28 Trim Type Drag, Multi-Path, Multi-Stage 53 Filter (Filter Reg) Fisher 67CFR29 Trim Size 2.5 inches Rated Cv 35 54 Limit/Torque Switch N/A30 Trim Char. Linear 55 Position Feedback N/A31 Number of Pressure Reducing Stages 28 56 I - P Transducer N/A32 Plug Type Balanced 57 Solenoid Valve(s) N/A33 Stem Matl Inconel 718 58 Elect Housing STD EExd IIA T3, IP 5634 Plug Matl Inconel 718 59 Seat Leakage ANSI/FCI Class IV35 Seat Matl 316L SS 60 Open Time(s) < 20 sec36 Guide Matl Inconel 718 61 Close Time(s) < 20 sec37 62 Approx. Weight 1140 KG (2500 lbs)

N o t e s / S p e c i a l I n s t r u c t i o n s63 Hardware capacity shown above assumes 25% over capacity margin.64 65 To eliminate uncontrolled pressure letdown problems, a number of discrete pressure reduction stages are provided.66 The fluid Kinetic Energy (Velocity Head) exiting the trim will not exceed 70 psi (4.8 Bar).67 To maximize the noise attenuating benefits, flow direction will be flow to open.68 All noise levels shown above are based on no thermal or acoustic padding on the downstream pipe.69 To prevent flow induced vibration, Pressure Equalizing Rings (PER) are provided to assure equal pressure around the plug.70 For easy maintenance, the trim is a quick change type. No components are screwed or welded to the body or bonnet.71 Valve design to API 6A, latest edition.72 Control valve sizing is based on ISA S75.01, ‘Flow Equations For Sizing Control Valves’.73 74 75


CONTROL VALVE DATA SHEETProject ERHA FPSO-EPC1 Tag # 1-LV-54200-1A, B, C, DCustomer Saipem SA Item # 1/2/3/4Ult. Client Esso E & P Nigeria Qty. 4Inq. T122010-PRT-11.01-044 Rev. 0 Date Model 100 CProp. 030124-152154 Rev. 0 Date 12 Feb 2003 D-SHT Rev. 5 Dwg # 200903-1P.O. T122010/OPI/PRT/11.10 Application HP Separator Oil Train 1

1 Fluid Liquid / Gas Crit Press 0.00 Bar A Crit Temp Units @ Max. Flow @ Min. Flow Shut Off

2 Liquid Mass Flow kg/hr 455830 197500 3 Gas Mass Flow Rate kg/hr 121170 52500 4 Inlet Pressure (P1) Bar G 29.7 37.9 5 Outlet Pressure (P2) Bar G 29.0 36.9 6 Differential (∆P) Bar 0.70 1.0 313.87 Inlet Temperature deg C 96.0 96.0 8 Liquid Vapor Press Bar A 29.7 37 9 Liquid Density kg/m3 853.3 853.3 10 Molecular Weight 19.0 19.0 11 Ratio of Spec. Heat 1.3 1.3 12 Compressibility 1.0 1.0 13 Required Flow Cv 2798 911 14 Travel % ~80% ~26% 15 SPL dBA 80 80 2-Phase 16 Pipe In 24in (600mm) Sch XS 41 Actuator Type Pneumatic Double Acting Piston17 Pipe Out 24in (600mm) Sch XS 42 Mfr / Model CCI / Standard18 Pipe Matl In Carbon Steel Out Carbon Steel 43 Failure Mode Fail Open19 Type Angle Size 20.0 X 20.0 in 44 Supply Type Compressed Air20 Design P In 314.0 Out 314.0 Bar G 45 Supply (Min) 5.5 Bar G21 Design T In 121 Out 121 deg C 46 Supply (Max) 7.0 Bar G22 Rating(s) In API 5000 Std Out API 5000 Std 47 Stem Orientation Vertical Up23 Material AISI 4130 / 4130 48 Manual Override Yes, Top Mounted/Side Access24 Connect In API 5000 Hub (TECHLOK H20IN152) 49 25 Connect Out API 5000 Hub (TECHLOK H20IN152) 50 Positioner Type Smart Positioner w/ Hart Protocol26 Flow Dir. Flow to Close (OTP) 51 Mfr / Model Fisher / DVC 600027 Bonnet Type Bolted 52 Input Signal 4 to 20 mA28 Bonnet Seal Standard 53 Increasing Signal To Close the Valve29 Packing Type Standard 54 Cam Characteristic Linear30 Packing Matl Grafoil 55 31 Trim Type Cage Guided 56 Filter (Filter Reg) Fisher 67CFR32 Trim Size 14.0 inches Rated Cv 3500 57 Limit/Torque Switch N/A33 Trim Char. Linear 58 Position Feedback N/A34 Number of Pressure Reducing Stages Cage Guided 59 I - P Transducer N/A35 Plug Type Balanced 60 Solenoid Valve(s) N/A36 Stem Matl 316 SS 61 Elect Housing STD EExd IIA T3, IP 5637 Plug Matl 316 SS 62 Seat Leakage ANSI/FCI Class IV38 Seat Matl 316 SS 63 Open Time(s) < 40 sec39 Guide Matl 17-4 PH Cond. 1150M 64 Close Time(s) < 40 sec40 Wetted parts per NACE STD MR-01-75. 65 Approx. Weight 5400 kg (11800 lbs)

N o t e s / S p e c i a l I n s t r u c t i o n s66 For easy maintenance, the trim is a quick change type. No components are screwed or welded to the body or bonnet.67 Valve design to API 6A, latest edition.68 Hardware capacity shown above assumes 18% over capacity margin.69 Wetted parts per NACE STD MR-01-75.70 71 72 73 74 75


CONTROL VALVE DATA SHEETProject ERHA FPSO-EPC1 Tag # 1-LV-65128-1Customer SAIPEM SA Item # 8Ult. Client ESSO E & P NIGERIA Qty. 1Inq. T122010-PRT-11.01-044 Rev. Date Model 100OGDProp. 030124-152154 Rev. Date D-SHT Rev. 5 Dwg # 200903-3P.O. Application 3rd Stage HP Comp Suct Scrub 1 & 2

1 Fluid Water Condensate Crit Press 226.5 Bar A Crit Temp - deg CUnits @ Max. Flow @ Norm. Flow Shut Off

2 Mass Flow Rate kg/hr 995.0 995.0 3 Inlet Pressure (P1) Bar G 176.9 182.9 4 Outlet Pressure (P2) Bar G 0.30 2.3 5 Differential (∆P) Bar 176.6 180.6 272.06 Inlet Temp. (T1) deg C 37.8 37.8 7 Density kg/m3 995.0 995.0 8 Vapor Pressure Bar G 176.9 182.9 9 Viscosity cpoise 0.68 0.68 10 Required Flow Cv 0.17 0.16 11 Travel ~70 ~70 12 SPL dBA <85 <85 13 Pipe In 2in (50mm) Sch XXS 38 Actuator Type Spring Diaphragm14 Pipe Out 2in (50mm) Sch XXS 39 Mfr / Model CCI / 400RA15 Pipe Matl In Stainless Steel Out Stainless Steel 40 Failure Mode Fail Close16 Type Angle Size 1.0 X 1.0 inches 41 Supply Type Compressed Air17 Design P In 272.0 Out 272.0 Bar G 42 Supply (Min) 5.5 Bar G18 Design T In -100.0/200.0 Out -100.0/200.0 deg C 43 Supply (Max) 7.0 Bar G19 Rating(s) In 2500 Standard Out 2500 Standard 44 Stem Orientation Vertical Up20 Material F316 / F316 45 Manual Override N/A21 Connect In RTJ Flange 46 22 Connect Out RTJ Flange 47 Positioner Type Smart Positioner w/ Hart Protocol23 Flow Dir. Flow to Close (OTP) 48 Mfr / Model Fischer / DVC600024 Bonnet Type Bolted 49 Input Signal 4 to 20 mA25 Bonnet Seal Standard 50 Increasing Signal To Open the Valve26 Packing Type Standard 51 Cam Characteristic Linear27 Packing Matl Grafoil 52 28 Trim Type Drag, Multi-Path, Multi-Stage 53 Filter (Filter Reg) FISHER 67CFR29 Trim Size 3/8 inches Rated Cv 0.23 54 Limit/Torque Switch N/A30 Trim Char. Linear 55 Position Feedback N/A31 Number of Pressure Reducing Stages Min. 8 Stages 56 I - P Transducer N/A32 Plug Type Unbalanced 57 Solenoid Valve(s) N/A33 Stem Matl Inconel 718 58 Elect Housing STD EExd IIA T3,IP 5634 Plug Matl Inconel 718 59 Seat Leakage ANSI/FCI Class V35 Seat Matl 316L SS 60 Open Time(s) < 10 sec36 Guide Matl Inconel 718 61 Close Time(s) < 10 sec37 62 Approx. Weight 165kg (365lbs)

N o t e s / S p e c i a l I n s t r u c t i o n s63 Hardware capacity shown above assumes 25% over capacity margin.64 To eliminate uncontrolled pressure letdown problems, a number of discrete pressure reduction stages are provided.65 The liquid velocity exiting the trim will not exceed 100 ft/sec (30 m/sec).66 To prevent line trash damage to seating surfaces, the flow direction will be flow to close.67 To prevent flow induced vibration, Pressure Equalizing Rings (PER) are provided to assure equal pressure around the plug.68 For easy maintenance, the trim is a quick change type. No components are screwed or welded to the body or bonnet.69 Valve design to ASME B16.34, latest edition.70 Control valve sizing is based on ISA S75.01, ‘Flow Equations Sizing Control Valves’.71 72 73 74 75


CONTROL VALVE DATA SHEETProject ERHA FPSO-EPC1 Tag # 1-PV-67635-6Buyer Saipem SA Item # 21Owner Esso E & P Nigeria Qty. 1Inq. T122010-PRT-11.01-044 Rev. Date Model 100DProp. 030124-152154 Rev. 11 Date 21-Aug-03 D-SHT Rev. 2 Dwg # 200903-17P.O. Application Methanol Header Pressure Control

1 Fluid Liquid Crit Press Bar A Crit Temp deg CUnits @ Max Flow @ Min Flow Shut-Off

2 Mass Flow Rate kg/hr 53788 21515 3 Inlet Pressure (P1) Bar G 415.0 415.0 4 Outlet Pressure (P2) Bar G 315.0 315.0 5 Differential (∆P) Bar 100.0 100.0 458.06 Inlet Temp. (T1) deg C 26.0 26.0 7 Density kg/m3 791.0 791.0 8 Vapor Pressure Bar A 0.1300 0.1300 9 Viscosity cpoise 0.7900 0.7900 10 Required Flow Cv 7.1 2.8 11 Travel 12 SPL dBA 75.0 75.0 13 Pipe In 4in (100mm) Sch XXS 38 Actuator Type Pneumatic Double Acting Piston14 Pipe Out 4in (100mm) Sch XXS 39 Mfr / Model CCI / SC/V 20015 Pipe Matl In Carbon Steel Out Carbon Steel 40 Failure Mode Fail Close16 Type Globe Size 3 X 3 inches 41 Supply Type Compressed Air17 Design P In 458.0 Out 458.0 Bar G 42 Supply (Min) 5.5 Bar G18 Design T In 0.00/49.0 Out 0.00/49.0 deg C 43 Supply (Max) 7.0 Bar G19 Rating(s) In API 10000 Out API 10000 44 Stem Orientation Vertical Up20 Material AISI 4130/4130 45 Manual Override N/A21 Connect In Hub Techlok 3IN23ST 46 22 Connect Out Hub Techlok 3IN23ST 47 Positioner Type Smart Positioner w/ Hart Protocol23 Flow Dir. Flow to Close (OTP) 48 Mfr / Model Fisher / DVC 6000 Series24 Bonnet Type Bolted 49 Input Signal 4 to 20 mA25 Bonnet Seal Gasket 50 Increasing Signal To Open the Valve26 Packing Type Standard 51 Cam Characteristic Linear27 Packing Matl Grafoil 52 28 Trim Type Drag®, Multi-Path, Multi-Stage 53 Filter (Filter Reg) Fisher 67CFSR (Filter - Reg)29 Trim Size 1.5 inches Rated Cv 9.5 54 Limit/Torque Switch N/A 30 Trim Char. Linear 55 Position Feedback N/A 31 Number of Pressure Reducing Stages 10 Stages 56 I - P Transducer N/A 32 Plug Type Balanced 57 Solenoid Valve(s) N/A 33 Stem Matl Inconel 718 58 Elect Housing STD IP5634 Plug Matl Inconel 718 59 Seat Leakage ASME/FCI Class IV35 Seat Matl Inconel 718 60 Open Time(s) <10 sec36 Guide Matl Inconel 718 61 Close Time(s) <10 sec37 62 Approx. Weight 800 lbs

N o t e s / S p e c i a l I n s t r u c t i o n s63 To eliminate uncontrolled pressure letdown problems, a number of discrete pressure reduction stages are provided.64 The liquid velocity exiting the trim will not exceed 100 ft/sec (30 m/sec).65 To prevent line trash damage to seating surfaces, the flow direction will be flow to close.66 For easy maintenance, the trim is a quick change type. No components are screwed or welded to the body or bonnet.67 Valve design to API 6A, latest edition.68 Control valve sizing is based on ISA S75.01, ‘Flow Equations For Sizing Control Valves’.69 Quality per API 6A PSL 1.70 71 72 73 74 75


CONTROL VALVE DATA SHEETProject ERHA FPSO-EPC1 Tag # 1-PV-67635-2Customer SAIPEM SA Item # 13Ult. Client ESSO E & P NIGERIA Qty. 1Inq. T122010-PRT-11.01-044 Rev. Date Model 100OGDProp. 030124-152154 Rev. Date 22-MAR-04 D-SHT Rev. 5 Dwg # 200903-6P.O. Application Methanol Injection Pump Discharge

1 Fluid Methanol Crit Press 80.0 Bar A Crit Temp - deg CUnits @ Max. Flow @Norm Flow @Min. Flow Shut Off

2 Mass Flow Rate kg/hr 53788 53788 15820 3 Inlet Pressure (P1) Bar G 105 415 415 4 Outlet Pressure (P2) Bar G 1.5 1.5 .5 5 Differential (∆P) Bar 103.5 413.5 414.5 458.06 Inlet Temp. (T1) deg C 26.0 26.0 26 7 Density kg/m3 791.0 791.0 791.0 8 Vapor Pressure Bar G 0.13 0.13 0.13 9 Viscosity cpoise 0.79 0.79 0.79 10 Required Flow Cv 6.8 3.5 1.0 11 Travel % ~80% ~32% ~15% 12 SPL dBA 75.0 75.0 75.0 13 Pipe In 3in (75mm) Sch STD 38 Actuator Type Pneumatic Double Acting Piston14 Pipe Out 6in (150mm) Sch STD 39 Mfr / Model CCI / 113in215 Pipe Matl In Carbon Steel Out Carbon Steel 40 Failure Mode Fail Open16 Type Angle Size 2-1/16 X 2-1/16 41 Supply Type Compressed Air17 Design P In 458.0 Out 458.0 Bar G 42 Supply (Min) 5.5 Bar G18 Design T In 49.0 Out 49.0 deg C 43 Supply (Max) 7.0 Bar G19 Rating(s) In API 10000 Out API 10000 44 Stem Orientation Vertical Up20 Material AISI 4130 / 4130 45 Manual Override N/A21 Connect In API 10000 HUB (TECHLOK 3IN 23ST) 46 22 Connect Out API 10000 HUB (TECHLOK 3IN 23ST) 47 Positioner Type Smart Positioner w/ Hart Protocol23 Flow Dir. Flow to Close (OTP) 48 Mfr / Model Fischer / DVC600024 Bonnet Type Bolted 49 Input Signal 4 to 20 mA25 Bonnet Seal Standard 50 Increasing Signal To Close the Valve26 Packing Type Standard 51 Cam Characteristic Linear27 Packing Matl Grafoil 52 28 Trim Type Drag, Multi-Path, Multi-Stage 53 Filter (Filter Reg) Fisher 67CFR29 Trim Size 1.5 inches Rated Cv 6.8 54 Limit/Torque Switch N/A30 Trim Char. Linear 55 Position Feedback N/A31 Number of Pressure Reducing Stages Min. 22 Stages 56 I - P Transducer N/A32 Plug Type Balanced 57 Solenoid Valve(s) N/A33 Stem Matl Inconel 718 58 Elect Housing STD EExd IIA T3, IP 5634 Plug Matl Inconel 718 59 Seat Leakage ANSI/FCI Class IV35 Seat Matl 316L SS 60 Open Time(s) < 10 sec36 Guide Matl Inconel 718 61 Close Time(s) < 10 sec37 62 Approx. Weight 800kg (363lbs) lbs

N o t e s / S p e c i a l I n s t r u c t i o n s63 Hardware capacity shown above assumes 25% over capacity margin.64 To eliminate uncontrolled pressure letdown problems, a number of discrete pressure reduction stages are provided. 65 The liquid velocity exiting the trim will not exceed 100 ft/sec (30 m/sec).66 To prevent line trash damage to seating surfaces, the flow direction will be flow to close.67 To prevent flow induced vibration, Pressure Equalizing Rings (PER) are provided to assure equal pressure around the plug.68 For easy maintenance, the trim is a quick change type. No components are screwed or welded to the body or bonnet.69 Valve design to ASME B16.34, latest edition.70 Control valve sizing is based on ISA S75.01, ‘Flow Equations Sizing Control Valves’.71 72 73 74 75


CONTROL VALVE DATA SHEETProject Kizomba ‘B’ FPSO Tag # B1-HV-56206-14Buyer Fluor / Hyundai Item # 1Owner Esso Exploration Angola (Exxon Mobile) Qty. 4

Inq. Rev. Date 18Dec03 Model 100DProp. Rev. Date D-SHT Rev. Dwg # 200971-1P.O. Application Production Flow Line Stand-By Choke Valve

1 Fluid Liquid / Gas Crit Press 0.00 Bar G Crit Temp Units Max Flow Normal Flow

2 Liquid Mass Flow kg/hr 410300 995903 Gas Mass Flow Rate kg/hr 31470 6817.04 Inlet Pressure (P1) Bar G 52.0 18.15 Outlet Pressure (P2) Bar G 17.1 16.56 Differential (∆P) Bar 34.9 1.67 Inlet Temperature deg C 50.0 50.08 Liquid Vapor Press Bar G 52.0 18.19 Liquid Density kg/m3 868.0 878.010 Molecular Weight 18.61 19.3811 Ratio of Spec. Heat 1.22 1.2412 Compressibility 0.9 0.9613 Required Flow Cv 204.9 239.914 Travel 78% 95%15 SPL dBA < 80 < 8016 Pipe In OD 10.75 THK 1.052 inches 41 Actuator Type Pneumatic Double Acting Piston17 Pipe Out OD 10.75 THK 1.052 inches 42 Mfr / Model CCI / SCV 30018 Pipe Matl In Carbon Steel Out Carbon Steel 43 Failure Mode Fail Close via Springs19 Type Angle Size 6 X 6 inches 44 Supply Type Compressed Air20 Design P In 215.0 Out 215.0 Bar G 45 Supply (Min) 5.5 Bar G21 Design T In -29 to 138 Out -29 to 138 deg C 46 Supply (Max) 8.5 Bar G22 Rating(s) In 1500 Std PN 250 Out 1500 Std PN 250 47 Stem Orientation Vertical Up23 Material LF2/LF2 48 Manual Override N/A24 Connect In RTJ 6 in, 1500# 49 25 Connect Out RTJ 6 in, 1500# 50 Positioner Type Smart positioner w/ Hart Protocol26 Flow Dir. Flow to Close (OTP) 51 Mfr / Model Fisher / 6000DVC See Note 7427 Bonnet Type Bolted 52 Input Signal 4 - 20 mA28 Bonnet Seal Metal Seal 53 Increasing Signal To Open the Valve29 Packing Type Standard 54 Cam Characteristic Linear30 Packing Matl Teflon 55 31 Trim Type Drag, Multi-Path, Multi-Stage 56 Filter (Filter Reg) Fisher 67CFR32 Trim Size 4.0 inches Rated Cv 250 57 Limit/Torque Switch N/A 33 Trim Char. Linear 58 Position Feedback 4 - 20 mA Fisher 4211 See Note 7534 Number of Pressure Reducing Stages 4 Stages 59 I - P Transducer N/A 35 Plug Type Balanced 60 Solenoid Valve(s) N/A 36 Stem Matl Inconel 718 61 Elect Housing STD EExd. CL.1,DIV.2,GR.C&D37 Plug Matl 316 SS with Wallex 55 Overlay 62 Seat Leakage ASME/FCI Class IV38 Seat Matl 316 SS with Wallex 55 Overlay 63 Open Time(s) < 30 sec39 Guide Matl Inconel 718 64 Close Time(s) < 30 sec40 65 Approx. Weight 650 kgs

N o t e s / S p e c i a l I n s t r u c t i o n s66 To eliminate uncontrolled pressure letdown problems, a number of discrete pressure reduction stages are provided.67 The fluid Kinetic Energy (Veleocity Head) exiting the trim will not exceed 70 psi (4.8 bar).68 To prevent line trash damage to seating surfaces, the flow direction will be flow to close.69 To prevent flow induced vibration, Pressure Equalizing Rings (PER) are provided to assure equal pressure around the plug.70 For easy maintenance the trim is a quick change type. No components are screwed or welded to the body or bonnet. 71 Valve design to ASME B16.34, Latest Edition. Sand present in the fluid area, Diskstack Tortuous path inlet passage 6MM X 6MM72 Valve capacity shall not exceed Cv=317.73 Cv = 124 at 50% stroke, equivalent to a 2” orifice.74 Positioner tag number is B1-HY-56206-14A75 Position feedback tag number is B1-ZT-56206-14


CONTROL VALVE DATA SHEETProject Kizomba ‘B’ FPSO Tag # B1-HV-56207-1Buyer Fluor / Hyundai Item # 2Owner Esso Exploration Angola (Exxon Mobile) Qty. 1

Inq. Rev. Date 18Dec03 Model 100DProp. Rev. Date D-SHT Rev. Dwg # 200971-2P.O. Application Test Flowline Choke Valve

1 Fluid Liquid / Gas Crit Press 0.00 Bar G Crit Temp Units Max Flow

2 Liquid Mass Flow kg/hr 170070 3 Gas Mass Flow Rate kg/hr 14050 4 Inlet Pressure (P1) Bar G 18.1 5 Outlet Pressure (P2) Bar G 17.1 6 Differential (∆P) Bar 1.0 7 Inlet Temperature deg C 56.0 8 Liquid Vapor Press Bar G 18.1 9 Liquid Density kg/m3 872.9 10 Molecular Weight 19.7 11 Ratio of Spec. Heat 1.23 12 Compressibility 0.96 13 Required Flow Cv 551.7 14 Travel 95% 15 SPL dBA < 80 16 Pipe In OD 10.75 THK 1.052 inches 41 Actuator Type Pneumatic Double Acting Piston17 Pipe Out OD 10.75 THK 1.052 inches 42 Mfr / Model CCI / SCV 300 18 Pipe Matl In Carbon Steel Out Carbon Steel 43 Failure Mode Fail Closed Via Springs19 Type Angle Size 8 X 8 inches 44 Supply Type Compressed Air20 Design P In 215 Out 215 Bar G 45 Supply (Min) 8.5 Bar G21 Design T In -29 to 132 Out -29 to 132 deg C 46 Supply (Max) 5.5 Bar G22 Rating(s) In 1500 Std PN 250 Out 1500 Std PN 250 47 Stem Orientation Vertical Up23 Material A350 -LF2 / A350-LF2 48 Manual Override N/A24 Connect In RTJ, 8” 1500# 49 25 Connect Out RTJ, 8” 1500# 50 Positioner Type Smart positioner w/ Hart Protocol26 Flow Dir. Flow to Close (OTP) 51 Mfr / Model Fisher / 6000 DVC see note 7327 Bonnet Type Bolted 52 Input Signal 4 - 20 mA28 Bonnet Seal Standard 53 Increasing Signal To Open the Valve29 Packing Type Standard 54 Cam Characteristic Linear30 Packing Matl Teflon 55 31 Trim Type Drag, Multi-Path, Multi-Stage 56 Filter (Filter Reg) Fisher 67CFR32 Trim Size 6.0 inches Rated Cv 580 57 Limit/Torque Switch N/A 33 Trim Char. Linear 58 Position Feedback N/A 34 Number of Pressure Reducing Stages Min 2 Stages 59 I - P Transducer N/A 35 Plug Type Balanced 60 Solenoid Valve(s) N/A 36 Stem Matl Inconel 718 61 Elect Housing STD Exd, Cl.1, Div.2, Gr C&D37 Plug Matl 316 SS With Wallex Overlay 62 Seat Leakage ASME/FCI Class IV38 Seat Matl 316 SS With Wallex Overlay 63 Open Time(s) < 30 sec39 Guide Matl Inconel 718 64 Close Time(s) < 30 sec40 65 Approx. Weight 1818 kgs

N o t e s / S p e c i a l I n s t r u c t i o n s66 To eliminate uncontrolled pressure letdown problems, a number of discrete pressure reduction stages are provided.67 The fluid Kinetic Energy (Veleocity Head) exiting the trim will not exceed 70 psi (4.8 bar).68 To prevent line trash damage to seating surfaces, the flow direction will be flow to close.69 To prevent flow induced vibration, Pressure Equalizing Rings (PER) are provided to assure equal pressure around the plug.70 For easy maintenance the trim is a quick change type. No components are screwed or welded to the body or bonnet. 71 Valve design to ASME B16.34, Latest Edition. Sand present in the fluid area, Diskstack Tortuous path inlet passage 6MM X 6MM72 Valve capacity shall not exceed Cv=60073 Positioner tag number is B1-HY-56207-174 75


CONTROL VA LV E D ATA SH EETProject AGBAMI FPSO, Nigeria Tag # FV-6137Buyer HHI Item # 3Owner CHEVRON TEXACO Qty. 1Inq. Rev. Date Model 100DProp. 030919-14711-5 Rev. Date 26Feb2004 D-SHT Rev. 0 Dwg # LI 3 FV-6137P.O. Application Seawater Injection Pump No.1 Discharge

1 Fluid Sea Water Crit Press 221.2 Bar A Crit Temp 374.2 deg CUnits Max.Flow Norm.Flow Min.Flow Shut-Off

2 Liquid Vol Flow m3/hr 384.3 272.5 22.6 3 Inlet Pressure (P1) Bar G 344.7 344.7 344.7 4 Outlet Pressure (P2) Bar G 1.0 1.0 1.0 5 Differential (∆P) Bar 343.7 343.7 343.7 344.76 Inlet Temp. (T1) deg C 51.7 51.7 51.7 7 Density kg/m3 1001.7 1001.7 1001.7 8 Vapor Pressure Bar A 0.1343 0.1343 0.1343 9 Viscosity cpoise 0.5388 0.5388 0.5388 10 Required Flow Cv 24.0 17.0 1.4 11 Travel % 80 57 10 12 SPL dBA 75.0 75.0 75.0 13 Pipe In 6in (150mm) Sch XXS 38 Actuator Type Pneumatic Double Acting Piston14 Pipe Out 6in (150mm) Sch XXS 39 Mfr / Model CCI / Standard15 Pipe Matl In Carbon Steel Out Carbon Steel 40 Failure Mode Fail Open via Springs16 Type Angle Size 6 X 6 inches 41 Supply Type Compressed Air17 Design P In 448.0 Out 448.0 Bar G 42 Supply (Min) 5.516 Bar G18 Design T In 0.00/60.0 Out 0.00/60.0 deg C 43 Supply (Max) 6.895 Bar G19 Rating(s) In API 6500# Out API 6500# 44 Stem Orientation Vertical Up20 Material AISI 4130 (60 KSI Min.) 45 Manual Override Yes21 Connect In Hub [To be defined] 46 22 Connect Out Hub [To be defined] 47 Positioner Type Smart Positioner, Hart Protocol23 Flow Dir. Flow to Close (OTP) 48 Mfr / Model Fisher / DVC 6000 Series24 Bonnet Type Bolted 49 Input Signal 4 to 20 mA25 Bonnet Seal Standard 50 Increasing Signal To Close the Valve26 Packing Type Standard 51 Cam Characteristic N/A27 Packing Matl Teflon 52 28 Trim Type Drag®, Multi-Path, Multi-Stage 53 Filter (Filter Reg) Norgren B38SS Body (Filter-Reg)29 Trim Size 3.0 inches Rated Cv 30 54 Limit/Torque Switch Westlock 30 Trim Char. Linear 55 Position Feedback Integral w/Positioner 31 Number of Pressure Reducing Stages 22 Stages 56 I - P Transducer Integral w/Positioner 32 Plug Type Balanced 57 Solenoid Valve(s) N/A 33 Stem Matl 316 SS Chrome Plated 58 Elect Housing STD IEC/CENELE Zone2,EExe,T3,IP66 34 Plug Matl 316 SS Chrome Plated 59 Seat Leakage ASME/FCI Class IV35 Seat Matl 316 SS 60 Open Time(s) < 30 sec36 Guide Matl 316 SS 61 Close Time(s) < 30 sec37 62 Approx. Weight 600 kgs

N o t e s / S p e c i a l I n s t r u c t i o n s63 Hardware capacity shown above assumes 10% over capacity margin.64 To eliminate uncontrolled pressure letdown problems, a number of discrete pressure reduction stages are provided.65 The liquid velocity exiting the trim will not exceed 75 ft/sec (23 m/sec).66 To prevent line trash damage to seating surfaces, the flow direction will be flow to close.67 To prevent flow induced vibration, Pressure Equalizing Rings (PER) are provided to assure equal pressure around the plug.68 For easy maintenance, the trim is a quick change type. No components are screwed or welded to the body or bonnet.69 Valve design to API 6D, Latest Revision.70 Marine Environment. 71 Control valve sizing is based on ISA S75.01, ‘Flow Equations For Sizing Control Valves’.72 Wetted parts per NACE STD MR-01-75. 73 74 75


CONTROL VA LV E D ATA SH EETProject Agbami FPSo, Nigeria Tag # PV-4402ABuyer HHI Item # 54Owner Chevron Texaco Qty. 1Inq. Rev. Date Model 100DProp. 030919-14711-5 Rev. Date 26Feb2004 D-SHT Rev. Dwg # P.O. Application INJ COMP SUCT HDR TO HP FLARE

1 Fluid Gas - Customer Defined Crit Press psi A Crit Temp deg CUnits Max Norm Min Shut-Off

2 Gas Vol Flow Rate Nm3/hr 410011 137080 13887 3 Inlet Pressure (P1) Bar G 22.7 22.7 22.7 4 Outlet Pressure (P2) Bar G 4.4 1.3 6.18 5 Differential (∆P) Bar 18.3 21.4 16.52 22.76 Inlet Temp. (T1) deg C 53.65 53.65 49.44 7 Molecular Weight 26.73 26.73 26.73 8 Compressibility 0.9100 0.9900 0.9100 9 Ratio of Spec. Heat 1.171 1.171 1.171

10 Required Flow Cv 1192 415 40.5 11 Travel % 90 35 10 12 SPL dBA 83.9 84.2 75.0 13 Pipe In 14in (350mm) Sch STD 38 Actuator Type Pneumatic Double Acting Piston14 Pipe Out 14in (350mm) Sch 120 39 Mfr / Model CCI / Standard15 Pipe Matl In Carbon Steel Out Carbon Steel 40 Failure Mode Fail Close Via Volume Tank16 Type Globe Size 14 X 14 inches 41 Supply Type Compressed Air17 Design P In 22.7 Out 22.7 Bar G 42 Supply (Min) 5.516 Bar G18 Design T In 0.00/54.0 Out 0.00/54.0 deg C 43 Supply (Max) 6.895 Bar G19 Rating(s) In 300 Std PN 50 Out 300 Std PN 50 44 Stem Orientation Vertical Up20 Material A105 or WCB/A105 45 Manual Override Yes, Top Mounted/Side Access21 Connect In RF Flange 46 N/A22 Connect Out RF Flange 47 Positioner Type Smart Positioner23 Flow Dir. Flow to Open (UTP) 48 Mfr / Model Fisher / DVC 6000 Series24 Bonnet Type Bolted 49 Input Signal 4 to 20 mA25 Bonnet Seal Standard 50 Increasing Signal To Open the Valve26 Packing Type Standard 51 Cam Characteristic N/A27 Packing Matl Teflon 52 28 Trim Type Drag®, Multi-Path, Multi-Stage 53 Filter (Filter Reg) Norgren B38SS Body (Filter-Reg)29 Trim Size 14.0 inches Rated Cv 1370 54 Limit/Torque Switch Westlock 30 Trim Char. Linear 55 Position Feedback Integral w/Positioner 31 Number of Pressure Reducing Stages 10 Stages 56 I - P Transducer Integral w/Positioner 32 Plug Type Balanced 57 Solenoid Valve(s) N/A 33 Stem Matl 17-4 PH 58 Elect Housing STD IEC/CENELEC Zone 2, EEx,T3 34 Plug Matl 410 SS HT 59 Seat Leakage ASME/FCI Class VI35 Seat Matl 410 SS HT 60 Open Time(s) <30 sec36 Guide Matl 410 SS 61 Close Time(s) <30 sec37 62 Approx. Weight 1750 kgs

N o t e s / S p e c i a l I n s t r u c t i o n s63 64 To eliminate uncontrolled pressure letdown problems, a number of discrete pressure reduction stages are provided.65 The fluid Kinetic Energy (Velocity Head) exiting the trim will not exceed 70 psi (4.8 Bar).66 To maximize the noise attenuating benefits, flow direction will be flow to open.67 All noise levels shown above are based on no thermal or acoustic padding on the downstream pipe.68 To prevent flow induced vibration, Pressure Equalizing Rings (PER) are provided to assure equal pressure around the plug.69 For easy maintenance, the trim is a quick change type. No components are screwed or welded to the body or bonnet.70 Valve design to ASME B16.34, latest edition.71 Control valve sizing is based on ISA S75.01, ‘Flow Equations For Sizing Control Valves’.72 73 74 75

C O N TR O L VA LV E D ATA SHEETProject AGBAMI FPSO, Nigeria Tag # FV-6137Buyer HHI Item # 3Owner CHEVRON TEXACO Qty. 1Inq. Rev. Date Model 100DProp. 030919-14711-5 Rev. Date 26Feb2004 D-SHT Rev. 0 Dwg # LI 3 FV-6137P.O. Application Seawater Injection Pump No.1 Discharge

1 Fluid Sea Water Crit Press 221.2 Bar A Crit Temp 374.2 deg CUnits Max.Flow Norm.Flow Min.Flow Shut-Off

2 Liquid Vol Flow m3/hr 384.3 272.5 22.6 3 Inlet Pressure (P1) Bar G 344.7 344.7 344.7 4 Outlet Pressure (P2) Bar G 1.0 1.0 1.0 5 Differential (∆P) Bar 343.7 343.7 343.7 344.76 Inlet Temp. (T1) deg C 51.7 51.7 51.7 7 Density kg/m3 1001.7 1001.7 1001.7 8 Vapor Pressure Bar A 0.1343 0.1343 0.1343 9 Viscosity cpoise 0.5388 0.5388 0.5388 10 Required Flow Cv 24.0 17.0 1.4 11 Travel % 80 57 10 12 SPL dBA 75.0 75.0 75.0 13 Pipe In 6in (150mm) Sch XXS 38 Actuator Type Pneumatic Double Acting Piston14 Pipe Out 6in (150mm) Sch XXS 39 Mfr / Model CCI / Standard15 Pipe Matl In Carbon Steel Out Carbon Steel 40 Failure Mode Fail Open via Springs16 Type Angle Size 6 X 6 inches 41 Supply Type Compressed Air17 Design P In 448.0 Out 448.0 Bar G 42 Supply (Min) 5.516 Bar G18 Design T In 0.00/60.0 Out 0.00/60.0 deg C 43 Supply (Max) 6.895 Bar G19 Rating(s) In API 6500# Out API 6500# 44 Stem Orientation Vertical Up20 Material AISI 4130 (60 KSI Min.) 45 Manual Override Yes21 Connect In Hub [To be defined] 46 22 Connect Out Hub [To be defined] 47 Positioner Type Smart Positioner, Hart Protocol23 Flow Dir. Flow to Close (OTP) 48 Mfr / Model Fisher / DVC 6000 Series24 Bonnet Type Bolted 49 Input Signal 4 to 20 mA25 Bonnet Seal Standard 50 Increasing Signal To Close the Valve26 Packing Type Standard 51 Cam Characteristic N/A27 Packing Matl Teflon 52 28 Trim Type Drag®, Multi-Path, Multi-Stage 53 Filter (Filter Reg) Norgren B38SS Body (Filter-Reg)29 Trim Size 3.0 inches Rated Cv 30 54 Limit/Torque Switch Westlock 30 Trim Char. Linear 55 Position Feedback Integral w/Positioner 31 Number of Pressure Reducing Stages 22 Stages 56 I - P Transducer Integral w/Positioner 32 Plug Type Balanced 57 Solenoid Valve(s) N/A 33 Stem Matl 316 SS Chrome Plated 58 Elect Housing STD IEC/CENELE Zone2,EExe,T3,IP66 34 Plug Matl 316 SS Chrome Plated 59 Seat Leakage ASME/FCI Class IV35 Seat Matl 316 SS 60 Open Time(s) < 30 sec36 Guide Matl 316 SS 61 Close Time(s) < 30 sec37 62 Approx. Weight 600 kgs

N o t e s / S p e c i a l I n s t r u c t i o n s63 Hardware capacity shown above assumes 10% over capacity margin.64 To eliminate uncontrolled pressure letdown problems, a number of discrete pressure reduction stages are provided.65 The liquid velocity exiting the trim will not exceed 75 ft/sec (23 m/sec).66 To prevent line trash damage to seating surfaces, the flow direction will be flow to close.67 To prevent flow induced vibration, Pressure Equalizing Rings (PER) are provided to assure equal pressure around the plug.68 For easy maintenance, the trim is a quick change type. No components are screwed or welded to the body or bonnet.69 Valve design to API 6D, Latest Revision.70 Marine Environment. 71 Control valve sizing is based on ISA S75.01, ‘Flow Equations For Sizing Control Valves’.72 Wetted parts per NACE STD MR-01-75. 73 74 75

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