788-tp-fpso-applications.pdf

7/30/2019 788-TP-FPSO-Applications.pdf

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22591 Avenida Empresa

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788 | 01/05 2004 CCI DRAG is a registered trademark of CCI.

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

By Yasmin Bhuj, CCI


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

FPSO Applications

By Yasmin Bhuj, CCI USA

Background

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

become increasingly popular concepts in recent years. Their main

advantage is the ability to operate without the need or a specic

export inrastructure. Crude can be exported by shuttle tanker.

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

FPSOs suit low Gas Oil Ratios (GOR) elds especially. Other

advantages include:

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

Can oten be leased instead o bought, hence makingvery small elds 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 elds as

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

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

lack o drilling/ workover acilities (although there are proposals

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

to hire them rom companies such as Oceaneering or Bluewater

Economic Philosophy

Companies operating FPSOs generically aim to achieve the

ollowing1

Rapid Deployment: target or 12 months between contract

award and sail away rom the conversion yard

Fast track production rom new discoveries to accelerate

generation o revenues and increase reliability and

availability o production data or the ull eld

development

Turret mooring to allow tandem as well as calm buoy

o-loading

Cost Eectiveness: by high degree o vendor and operator

involvement in the early projects, and repeat ordering or

subsequent copy jobs

Standardization: By the generation o generic design

philosophies and specications or equipment, control &

saeguarding systems, etc. All these specications

can be tailored or a special project by separate unctional

specications and general conditions and data

specications.

Ater the successul start up o FPSO Kuito and FPSO Espadarteby the end o 1999, Single Buoy Moorings Inc. (SBM) and IHC

Gusto Engineering BV recognized the need to standardize FPSO

designs and incorporate lessons learned rom previous projects.

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

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

An FSPO is essentially a ship shape foating production vessel

(oten built rom a converted oil tanker). The vessel is moored in

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

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

allowing the vessel to weather vane, in harsher waters.

Process acilities can be anything rom just a 3 phase separator

train with gas to fare to ull export process systems with ull

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

has a lot o deck space!

FPSO are very fexible; theyve been used in thousands o meters

o water oshore Brazil to a ew meters o water oshore Nigeria;

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

and throughputs can vary rom a couple o thousand bbl/d to

hundreds o thousands bbl/d. Storage can also range rom a ew

thousand barrels to over a million barrels.


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

to cope with a wide range o eld properties, and water depths

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

or relocation between elds during its lietime.

Conversion o the existing tanker or FPSO service lie was based

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

renewals. Design and construction o new topside acilities was

intended or a minimum o 15 years lie.

General Set-up Considerations

Vessel Conversion

The primary selection criteria or a vessel conversion are:

Good Hull Condition

Minimum Steel Renewal

Traceable History

Lay Out Suitable or Conversion, i.e

noadditionalbulkheadsrequired,

possibilitytoextendaccommodation

Boiler,SteamTurbines,Off-loadingPumpssuitablefor

reurbishment

The reurbishment may comprise the removal o:

All deck and cargo piping,

Accommodation interior,

Asbestos,

Superfuous equipment

Topsides Lay Out

Reer to the generic diagram1 on the top o page 4. The topsides

lay out is based on the ollowing philosophy:

A central pipe rack supports a travelling crane and providescentral walkway

Modules mounted 4 meters above main deck, on modulesupports 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 o risers is the

key parameter which denes the diameter and size o the turret.

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

sea-bed. Any turret thereore has a xed part (moored to the

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

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

chain, anchor and winch designs are especially dependant onriser weight and loads resulting rom current, wind, etc. There are

many designs o 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 acilities, sick bay and bridge are located in the

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

provided or installation o uture acilities.

Process

Crude Oil Separation

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

production acilities may comprise a single train, which eatures

three stages o separation and stabilization. Ater bulk separation

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

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

dehydrated to specication using an electrostatic coalescer.

Produced water is fashed at near atmospheric pressure and

stored in the slop tanks or gravity settling and i required

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

water is disposed o overboard. Crude oil is stored temporarilyand produced water is disposed o overboard ater nal treatment

in the slop tanks.

Wash water is injected downstream o the LP Separator to reduce

the salt content o the crude within specications. Wash water

is desalinated seawater, using reverse osmosis as desalination

method.


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5/23


Chemical Injection

Extensive provisions or chemical injection include methanol,

pour points depressant, corrosion inhibitor, oam inhibitor,

demulsier, scale inhibitor, etc. A dedicated chemical injection

module is provided or water injection purposes.

Nitrogen

A nitrogen generator is provided to increase availability o largequantities o nitrogen oshore West Arica.

Fuel Gas and marine gas oil (MGO) System

Fuel gas is normally extracted immediately downstream o the

TEG Contactor, upstream o the nal compression stage. Despite

the low dewpoint o the gas ater dehydration at 140 bar /45 C,

20 C superheat is continuously maintained or protection o

turbomachinery and ease o operation.

In addition each FPSO will have its own particular eatures

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

below or a specic example.

Gas Compression, Treatment and Disposal

Reservoir pressure is maintained by gas injection, thus

minimizing faring. All gas in excess o uel gas is available or

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

injection header.

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

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

common shat, centriugal compressors are driven by industrial

type gas turbines, iso-rated at 13.4 MW.

The 1x 100% capacity Flash Gas Compressor receives gas

rom the IP and LP- Separator. The two stage, oil ree 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 or each compressor but

eature 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 orce is

provided by seawater and low pressure steam rom the vessel

system.

Power Generation

Electrical Power is provided by two, 100% capacity industrial

type gas turbines, 6.5 MW iso-rated. Emergency and EssentialPower Generators are provided in the engine room and below

the helideck.


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Case Study

Terra Nova FPSO2

The Terra Nova eld is being developed using a Floating

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

a ship-shaped production platorm with integrated oil storage

rom which oil is o-loaded to a shuttle tanker.

One o the largest Floating Production Storage and O-loading

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

45.5 metres wide (about the size o three ootball elds laid

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

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

accommodate up to 80 personnel.

The wellheads and production maniolds are placed in glory

holes excavations in the sea foor that protect the equipment

rom scouring icebergs.

Production System

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

drilling platorm such as the one below.

A network o more than 40 kilometers o fexible fowline is usedto convey hydrocarbons to and rom the wells. Produced gases

are separated rom the oil and re-injected into the reservoir or

possible uture extraction.

The connection between the FPSO and the subsea fowlines is

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

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

oil and fuids that fow to and rom the FPSO and reservoir. The

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

disconnect and leave the area in an emergency situation like the

approach o an iceberg. Crude oil is o-loaded rom the FPSO

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

Design, construction and installation o the FPSO, subsea

components and pre-production wells were carried out by a

consortium o companies comprising Petro-Canada, AGRA

Brown & Root, Hallibuton Energy Services, FMC Oshore

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

and Doris ConPro Ltd


7/23


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 o 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 o

Natuna Island, roughly 200 kilometers northeast

o Singapore, and is one o the most sophisticated

production acilities in the world. The vessel produces

approximately 7,800 standard barrels per day o

butane and 14,700 standard barrels per day o propane

plus 430 million standard cubic eet o gas and

100,000 barrels o oil.

CCI supplied seven anti-surge control valves or the

FPSO vessels LPG unit. These valves are considered

the most critical control valves on the FPSO because

they protect over $20 million worth o compressors.

Stringent specication requirements demanded

that CCI implement specialized design and control

measures, and the valves were custom designed or

each application. For example, while carbon steel is

a typical material or these types o valves, CCI used

duplex stainless steel or the FPSO valves since this

extra-hard material is the best substance available or

preventing corrosion in the valve body and bonnet.

Corrosion is a signicant concern on the FPSO unit

because both the highly acidic fuid 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 shuto, made possible by the pneumatic

actuator providing thrust o over 500 pounds per

linear inch. Preventing leakage and boosting overall

eciency, this tight shuto translates directly into

operational cost savings or the FPSO. Another special

eature o the valves supplied by CCI is their ast 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


8/23


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

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

stages, the valves eature CCIs unique DRAG technology or

superior velocity and noise control to eliminate vibration and

the possibility o mechanical ailure.

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 Lit Maniold Control

HP Compressor Suction Pump

Dehydrator Train

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

to supply 23 control valves to Exxon Mobils Erha FPSO vessel.

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

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

are or high-pressure applications and range rom 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 o the rst stretches o deepwater acreage

oered by the Angolan Government. The development

consortium is operated by ExxonMobil's subsidiary, Esso

Exploration Angola, which has a 40% stake in the eld. 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 o 3,300 t to 3,400 t. The project

will include the combination o a surace wellhead platorm and

subsea wells tied back to an FPSO vessel3.


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Endnotes

1 EPS Project A: FPSO Falcon, Design Challenges and Successul

Start-up o the rst Generic FPSO design, Andries Mastenbroek

and Mattieu Ubas o HIC Gusto Engineering

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

12/06/2004

3 http://www.oshore-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


10/23


CONTROL VALVE DATA SHEETProject Belanak FPSO Development Tag # T23FV 3165A/B

Customer Halliburton Far East Pte. Ltd Item # 01/02

Ult. Client Conoco Indonesia Qty. 2

Inq. TIC-36 Rev. Date 04-JUN-02 Model 100D

Prop. 010623-003040 Rev. Date 25-Jun-02 D-SHT Rev. 4 Dwg # 200679-1

P.O. CNCO-BELK-PTIC36 Application LP compressor A/B Surge Control1 Fluid Gas - Customer Dened Crit Press psi A Crit Temp deg F

Units 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 1800

6 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


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CONTROL VALVE DATA SHEETProject ERHA FPSO-EPC1 Tag # 1-LV-66108-1

Customer SAIPEM SA Item # 10

Ult. Client ESSO E & P NIGERIA Qty. 1

Inq. T122010-PRT-11.01-044 Rev. Date Model 10OGD

Prop. 030124-152154 Rev. Date D-SHT Rev. 4 Dwg # 200903-4

P.O. Application Dehydrater Train 1 / 2

1 Fluid TEG Crit Press 20.46 Bar A Crit Temp - deg C

Units @ 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 70.1 160.0

6 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


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CONTROL VALVE DATA SHEETProject ERHA FPSO-EPC1 Tag # 1-PV-54200-1 / 2

Buyer Saipem SA Item # 16

Owner Esso E & P Nigeria Qty. 2

Inq. T122010-PRT-11.01-044 Rev. 0 Date Model 100 D

Prop. 030124-152154 Rev. 0 Date 12 Feb 2003 D-SHT Rev. 2 Dwg # 200903-16

P.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 48.0 313.8

6 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




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 Piston

17 Pipe Out 10in (250mm) Sch 160 42 Mfr / Model CCI / Standard

18 Pipe Matl In Carbon Steel Out Carbon Steel 43 Failure Mode Fail Open

19 Type Angle Size 6 X6inches 44 Supply Type Compressed Air20 Design P In 314.0 Out 314.0 Bar G 45 Supply (Min) 5.5 Bar G

21 Design T In 0.00/121.0 Out 0.00/121.0 deg C 46 Supply (Max) 7.0 Bar G

22 Rating(s) In 2500 Std PN 420 Out2500 Std PN 420 47 Stem Orientation Vertical Up

23 Material A350-LF2/ A350-LF2 48 Manual Override Top Mounted Side Access

24 Connect In RTJ Flange 49

25 Connect Out RTJ Flange 50 Positioner Type Smart Positioner w/ Hart Protocol

26 Flow Dir. Flow to Close (OTP) 51 Mfr / Model Fisher / DVC 6000

27 Bonnet Type Bolted 52 Input Signal 4 to 20 mA

28 Bonnet Seal Standard 53 Increasing Signal To Close the Valve

29 Packing Type Standard 54 Cam Characteristic Linear

30 Packing Matl Teon 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 Specication

37 Plug Matl 316 SS 62 Seat Leakage ANSI/FCI Class V

38 Seat Matl 316 SS 63 Open Time(s) < 12 sec

39 Guide Matl 316 SS 64 Close Time(s) < 12 sec

40 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 s

66 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 ow direction will be ow to close.

71 To prevent ow 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


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CONTROL VALVE DATA SHEETProject ERHA FPSO-ECP1 Tag # 1-PV-65300-1

Owner SAIPEM S.A. Item # 8

Buyer ESSCO E&P NIGERIA Qty. 1

Inq. T122010-PRT-11.01-044 Rev. 0 Date Model 100D

Prop. 030124-152154 Rev. 0 Date 12Feb2003 D-SHT Rev. 4 Dwg # 200903-8

P.O. t122010/opi/prt/11.10 Application Gas Injection Flowline To Drill Center 3/4

1 Fluid Gas - Customer Dened Crit Press Bar G Crit Temp deg C

Units 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 97.65 458

6 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



15 Pipe Matl In Carbon Steel Out Carbon Steel 40 Failure Mode Fail close

16 Type Angle Size 18 X18inches 41 Supply Type Compressed Air17 Design P In 458.0 Out 458.0 Bar G 42 Supply (Min) 5.5 Barg

18 Design T In -45.0/82.0 Out -45.0/82.0 deg C 43 Supply (Max) 7.0 Barg

19 Rating(s) In API 10000 Std Out API 10000 Std 44 Stem Orientation Vertical Up

20 Material AISI 4130/ 4130 45 Manual Override N/A

21 Connect In API 10000 Hub (TECHLOK) 46

22 Connect Out API 10000 Hub (TECHLOK) 47 Positioner Type Smart Positioner W/ Hart Protocol

23 Flow Dir. Flow to Open (UTP) 48 Mfr / Model Fisher/ DVC 6000

24 Bonnet Type Bolted 49 Input Signal 4-20 mA

25 Bonnet Seal Standard 50 Increasing Signal To Open The Valve


27 Packing Matl Teon with Graphoil Ring 52

28 Trim Type Drag, Multi-Path, Multi-Stage 53 Filter (Filter Reg) Norgren B73G

29 Trim Size 12.0 inches Rated Cv 1960 54 Limit/Torque Switch NA

30 Trim Char. Bi-Linear 55 Position Feedback N/A



33 Stem Matl INC 718 58 Elect Housing STD EExd IIA T3, IP 56

34 Plug Matl 316 SS 59Seat Leakage ASME/FCI Class IV35 Seat Matl 316 SS 60 Open Time(s)


14/23


CONTROL VALVE DATA SHEETProject Erha FPSO-EPC1 Tag # 1-FV-65403-1

Owner Saipem SA Item # 17

Buyer Esso E & P Nigeria Qty. 1

Inq. T122010-PRT-11.01-044 Rev. 1 Date Model 100 D

Prop. 030124-152154 Rev. 1 Date 5 Sept 03 D-SHT Rev. 8 Dwg # 200903-9

P.O. Application Gas Lift Manifold Control


Units 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


8 Compressibility .742 .742 .742


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 Diaphragm

14 Pipe Out 4in (100mm) Sch XXS 39 Mfr / Model CCI / Standard

15 Pipe Matl In Carbon Steel Out Carbon Steel 40 Failure Mode Fail Close

16 Type Globe Size 2 X2inches 41 Supply Type Compressed Air17 Design P In 200.0 Out 200.0 Bar G 42 Supply (Min) 5.5 Bar G

18 Design T In 0/200 Out 0/200 deg C 43 Supply (Max) 7.0 Bar G

19 Rating(s) In 2500 Out 2500 44 Stem Orientation Vertical Up

20 Material A350-LF2/ A350-LF2 45 Manual Override N/A

21 Connect In RTJ Flange 46

22 Connect Out RTJ Flange 47 Positioner Type Smart HART

23 Flow Dir. Flow to Open (UTP) 48 Mfr / Model Fisher / DVC 6000 Series


25 Bonnet Seal Gasket 50 Increasing Signal To Open the Valve


27 Packing Matl Grafoil 52

28 Trim Type Drag, Multi-Path, Multi-Stage 53 Filter (Filter Reg) Fisher 67CFR

29 Trim Size 1 Inch Rated Cv 5 54 Limit/Torque Switch N/A

30 Trim Char. Equal Percentage 55 Position Feedback N/A



33 Stem Matl Inconel 718 58 Elect Housing STD Per Specication

34 Plug Matl Inconel 718 59Seat Leakage ASME/FCI Class IV35 Seat Matl 316 SS 60 Open Time(s) < 4 sec

36 Guide Matl Inconel 718 61 Close Time(s) < 4 sec

37 62 Approx. Weight 350 kgs




65 The uid Kinetic Energy (Velocity Head) exiting the trim will not exceed 70 psi (4.8 Bar).

66 To maximize the noise attenuating benets, ow direction will be ow to open.

67 All noise levels shown above are based on no thermal or acoustic padding on the downstream pipe.




71 Control valve sizing is based on ISA S75.01, Flow Equations For Sizing Control Valves.

72 73 74 75


15/23


CONTROL VALVE DATA SHEETProject ERHA FPSO-EPC1 Tag # 1-PV-65100-1B

Customer Saipem SA Item # 12

Ult. Client Esso E & P Nigeria Qty. 1

Inq. T122010-PRT-11.01-044 Rev. 0 Date Model 100D


P.O. Application HP Compressor Master Controller


Units @ Max Flow @ Norm Flow @ Min Flow Shut Off


3 Inlet Pressure (P1) Bar G 381.3 380.5 381.3

4 Outlet Pressure (P2) Bar G 36.0 28.1 36.0


6 Inlet Temp. (T1) deg C 65.0 65.0 65.0




10 Required Flow Cv 27.6 24.3 8.3

11 Travel % ~79% ~69% ~24%

12 SPL dBA 80.5 82.2 75.0




16 Type Z-Globe Size 5-1/8 X5-1/8inches 41 Supply Type Compressed Air17 Design P In 458.0 Out 458.0 Bar G 42 Supply (Min) 5.5 Bar G

18 Design T In -45/200 Out -45/200 deg C 43 Supply (Max) 7.0 Bar G


20 Material AISI 4130 / 4130 45 Manual Override N/A

21 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 6000


25 Bonnet Seal Standard 50 Increasing Signal To Open the Valve








33 Stem Matl Inconel 718 58 Elect Housing STD EExd IIA T3, IP 56

34 Plug Matl Inconel 718 59Seat Leakage ANSI/FCI Class IV35 Seat Matl 316L SS 60 Open Time(s) < 20 sec


37 62 Approx. Weight 1140 KG (2500 lbs)



64 65 To eliminate uncontrolled pressure letdown problems, a number of discrete pressure reduction stages are provided.

66 The uid Kinetic Energy (Velocity Head) exiting the trim will not exceed 70 psi (4.8 Bar).

67 To maximize the noise attenuating benets, ow direction will be ow to open.

68 All noise levels shown above are based on no thermal or acoustic padding on the downstream pipe.



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


16/23


CONTROL VALVE DATA SHEETProject ERHA FPSO-EPC1 Tag # 1-LV-54200-1A, B, C, D

Customer Saipem SA Item # 1/2/3/4

Ult. Client Esso E & P Nigeria Qty. 4

Inq. T122010-PRT-11.01-044 Rev. 0 Date Model 100 C


P.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 1.0 313.8

7 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 Piston

17 Pipe Out 24in (600mm) Sch XS 42 Mfr / Model CCI / Standard


19 Type Angle Size 20.0 X20.0in 44 Supply Type Compressed Air20 Design P In 314.0 Out 314.0 Bar G 45 Supply (Min) 5.5 Bar G

21 Design T In 121 Out 121 deg C 46 Supply (Max) 7.0 Bar G


23 Material AISI 4130 / 4130 48 Manual Override Yes, Top Mounted/Side Access

24 Connect In API 5000 Hub (TECHLOK H20IN152) 49

25 Connect Out API 5000 Hub (TECHLOK H20IN152) 50 Positioner Type Smart Positioner w/ Hart Protocol

26 Flow Dir. Flow to Close (OTP) 51 Mfr / Model Fisher / DVC 6000





31 Trim Type Cage Guided 56 Filter (Filter Reg) Fisher 67CFR



34 Number of Pressure Reducing Stages Cage Guided 59 I - P Transducer N/A


36 Stem Matl 316 SS 61 Elect Housing STD EExd IIA T3, IP 56

37 Plug Matl 316 SS 62 Seat Leakage ANSI/FCI Class IV


39 Guide Matl 17-4 PH Cond. 1150M 64 Close Time(s) < 40 sec

40 Wetted parts per NACE STD MR-01-75. 65 Approx. Weight 5400 kg (11800 lbs)



67 Valve design to API 6A, latest edition.


69 Wetted parts per NACE STD MR-01-75.

70 71 72 73 74 75


17/23


CONTROL VALVE DATA SHEETProject ERHA FPSO-EPC1 Tag # 1-LV-65128-1




Prop. 030124-152154 Rev. Date D-SHT Rev. 5 Dwg # 200903-3

P.O. Application 3rd Stage HP Comp Suct Scrub 1 & 2

1 Fluid Water Condensate Crit Press 226.5 Bar A Crit Temp - deg C

Units @ Max. Flow @ Norm. Flow Shut Off

2 Mass Flow Rate kg/hr 995.0 995.0




6 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


18/23


CONTROL VALVE DATA SHEETProject ERHA FPSO-EPC1 Tag # 1-PV-67635-6

Buyer Saipem SA Item # 21

Owner Esso E & P Nigeria Qty. 1

Inq. T122010-PRT-11.01-044 Rev. Date Model 100D

Prop. 030124-152154 Rev. 11 Date 21-Aug-03 D-SHT Rev. 2 Dwg # 200903-17

P.O. Application Methanol Header Pressure Control

1 Fluid Liquid Crit Press Bar A Crit Temp deg C

Units @ Max Flow @ Min Flow Shut-Off

2 Mass Flow Rate kg/hr 53788 21515




6 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


11 Travel

12 SPL dBA 75.0 75.0

13 Pipe In 4in (100mm) Sch XXS 38 Actuator Type Pneumatic Double Acting Piston

14 Pipe Out 4in (100mm) Sch XXS 39 Mfr / Model CCI / SC/V 200


16 Type Globe Size 3 X3inches 41 Supply Type Compressed Air17 Design P In 458.0 Out 458.0 Bar G 42 Supply (Min) 5.5 Bar G

18 Design T In 0.00/49.0 Out 0.00/49.0 deg C 43 Supply (Max) 7.0 Bar G

19 Rating(s) In API 10000 Out API 10000 44 Stem Orientation Vertical Up

20 Material AISI 4130/4130 45 Manual Override N/A

21 Connect In Hub Techlok 3IN23ST 46

22 Connect Out Hub Techlok 3IN23ST 47 Positioner Type Smart Positioner w/ Hart Protocol

23 Flow Dir. Flow to Close (OTP) 48 Mfr / Model Fisher / DVC 6000 Series


25 Bonnet Seal Gasket 50 Increasing Signal To Open the Valve



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


31 Number of Pressure Reducing Stages 10 Stages 56 I - P Transducer N/A


33 Stem Matl Inconel 718 58 Elect Housing STD IP56

34 Plug Matl Inconel 718 59Seat Leakage ASME/FCI Class IV35 Seat Matl Inconel 718 60 Open Time(s)


19/23


CONTROL VALVE DATA SHEETProject ERHA FPSO-EPC1 Tag # 1-PV-67635-2




Prop. 030124-152154 Rev. Date 22-MAR-04 D-SHT Rev. 5 Dwg # 200903-6

P.O. Application Methanol Injection Pump Discharge

1 Fluid Methanol Crit Press 80.0 Bar A Crit Temp - deg C

Units @ Max. Flow @Norm Flow @Min. Flow Shut Off


3 Inlet Pressure (P1) Bar G 105 415 415

4 Outlet Pressure (P2) Bar G 1.5 1.5 .5


6 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


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 Piston

14 Pipe Out 6in (150mm) Sch STD 39 Mfr / Model CCI / 113in2


16 Type Angle Size 2-1/16 X2-1/16 41 Supply Type Compressed Air17 Design P In 458.0 Out 458.0 Bar G 42 Supply (Min) 5.5 Bar G

18 Design T In 49.0 Out 49.0 deg C 43 Supply (Max) 7.0 Bar G

19 Rating(s) In API 10000 Out API 10000 44 Stem Orientation Vertical Up

20 Material AISI 4130 / 4130 45 Manual Override N/A

21 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 Protocol

23 Flow Dir. Flow to Close (OTP) 48 Mfr / Model Fischer / DVC6000






29 Trim Size 1.5 inches Rated Cv 6.8 54 Limit/Torque Switch N/A


31 Number of Pressure Reducing Stages Min. 22 Stages 56 I - P Transducer N/A


33 Stem Matl Inconel 718 58 Elect Housing STD EExd IIA T3, IP 56

34 Plug Matl Inconel 718 59Seat Leakage ANSI/FCI Class IV35 Seat Matl 316L SS 60 Open Time(s) < 10 sec


37 62 Approx. Weight 800kg (363lbs) lbs









70 Control valve sizing is based on ISA S75.01, Flow Equations Sizing Control Valves.

71 72 73 74 75


20/23


CONTROL VALVE DATA SHEETProject Kizomba B FPSO Tag # B1-HV-56206-14

Buyer Fluor / Hyundai Item # 1

Owner Esso Exploration Angola (Exxon Mobile) Qty. 4

Inq. Rev. Date 18Dec03 Model 100D

Prop. Rev. Date D-SHT Rev. Dwg # 200971-1

P.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 99590

3 Gas Mass Flow Rate kg/hr 31470 6817.0



6 Differential (P) Bar 34.9 1.6

7 Inlet Temperature deg C 50.0 50.0

8 Liquid Vapor Press Bar G 52.0 18.1

9 Liquid Density kg/m3 868.0 878.0

10 Molecular Weight 18.61 19.38

11 Ratio of Spec. Heat 1.22 1.24

12 Compressibility 0.9 0.96


14 Travel 78% 95%

15 SPL dBA < 80 < 80

16 Pipe In OD 10.75 THK 1.052 inches 41 Actuator Type Pneumatic Double Acting Piston

17 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 Close via Springs

19 Type Angle Size 6 X6inches 44 Supply Type Compressed Air20 Design P In 215.0 Out 215.0 Bar G 45 Supply (Min) 5.5 Bar G

21 Design T In -29 to 138 Out -29 to 138 deg C 46 Supply (Max) 8.5 Bar G


23 Material LF2/LF2 48 Manual Override N/A

24 Connect In RTJ 6 in, 1500# 49

25 Connect Out RTJ 6 in, 1500# 50 Positioner Type Smart positioner w/ Hart Protocol

26 Flow Dir. Flow to Close (OTP) 51 Mfr / Model Fisher / 6000DVC See Note 74

27 Bonnet Type Bolted 52 Input Signal 4 - 20 mA

28 Bonnet Seal Metal Seal 53 Increasing Signal To Open the Valve





33 Trim Char. Linear 58 Position Feedback 4 - 20 mA Fisher 4211 See Note 75

34 Number of Pressure Reducing Stages 4 Stages 59 I - P Transducer N/A


36 Stem Matl Inconel 718 61 Elect Housing STD EExd. CL.1,DIV.2,GR.C&D

37 Plug Matl 316 SS with Wallex 55 Overlay 62 Seat Leakage ASME/FCI Class IV

38 Seat Matl 316 SS with Wallex 55 Overlay 63 Open Time(s) < 30 sec





67 The uid Kinetic Energy (Veleocity Head) exiting the trim will not exceed 70 psi (4.8 bar).



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 uid area, Diskstack Tortuous path inlet passage 6MM X 6MM

72 Valve capacity shall not exceed Cv=317.

73 Cv = 124 at 50% stroke, equivalent to a 2 orice.

74 Positioner tag number is B1-HY-56206-14A75 Position feedback tag number is B1-ZT-56206-14


21/23


CONTROL VALVE DATA SHEETProject Kizomba B FPSO Tag # B1-HV-56207-1

Buyer Fluor / Hyundai Item # 2

Owner Esso Exploration Angola (Exxon Mobile) Qty. 1

Inq. Rev. Date 18Dec03 Model 100D

Prop. Rev. Date D-SHT Rev. Dwg # 200971-2

P.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 Piston

17 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 Springs

19 Type Angle Size 8 X8inches 44 Supply Type Compressed Air20 Design P In 215 Out 215 Bar G 45 Supply (Min) 8.5 Bar G

21 Design T In -29 to 132 Out -29 to 132 deg C 46 Supply (Max) 5.5 Bar G


23 Material A350 -LF2 / A350-LF2 48 Manual Override N/A

24 Connect In RTJ, 8 1500# 49

25 Connect Out RTJ, 8 1500# 50 Positioner Type Smart positioner w/ Hart Protocol

26 Flow Dir. Flow to Close (OTP) 51 Mfr / Model Fisher / 6000 DVC see note 73

27 Bonnet Type Bolted 52 Input Signal 4 - 20 mA







34 Number of Pressure Reducing Stages Min 2 Stages 59 I - P Transducer N/A


36 Stem Matl Inconel 718 61 Elect Housing STD Exd, Cl.1, Div.2, Gr C&D

37 Plug Matl 316 SS With Wallex Overlay 62 Seat Leakage ASME/FCI Class IV

38 Seat Matl 316 SS With Wallex Overlay 63 Open Time(s) < 30 sec





67 The uid Kinetic Energy (Veleocity Head) exiting the trim will not exceed 70 psi (4.8 bar).



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 uid area, Diskstack Tortuous path inlet passage 6MM X 6MM

72 Valve capacity shall not exceed Cv=600

73 Positioner tag number is B1-HY-56207-1

74 75


22/23


CON TRO L VALVE DATA SHE ETProject AGBAMI FPSO, Nigeria Tag # FV-6137

Buyer HHI Item # 3

Owner CHEVRON TEXACO Qty. 1

Inq. Rev. Date Model 100D

Prop. 030919-14711-5 Rev. Date 26Feb2004 D-SHT Rev. 0 Dwg # LI 3 FV-6137

P.O. Application Seawater Injection Pump No.1 Discharge

1 Fluid Sea Water Crit Press 221.2 Bar A Crit Temp 374.2 deg C

Units Max.Flow Norm.Flow Min.Flow Shut-Off

2 Liquid Vol Flow m3/hr 384.3 272.5 22.63 Inlet Pressure (P1) Bar G 344.7 344.7 344.7



6 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


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 Piston

14 Pipe Out 6in (150mm) Sch XXS 39 Mfr / Model CCI / Standard

15 Pipe Matl In Carbon Steel Out Carbon Steel 40 Failure Mode Fail Open via Springs

16 Type Angle Size 6 X6inches 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 G

19 Rating(s) In API 6500# Out API 6500# 44 Stem Orientation Vertical Up

20 Material AISI 4130 (60 KSI Min.) 45 Manual Override Yes

21 Connect In Hub [To be dened] 46

22 Connect Out Hub [To be dened] 47 Positioner Type Smart Positioner, Hart Protocol

23 Flow Dir. Flow to Close (OTP) 48 Mfr / Model Fisher / DVC 6000 Series



26 Packing Type Standard 51 Cam Characteristic N/A


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/A33 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 IV


36 Guide Matl 316 SS 61 Close Time(s) < 30 sec









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


23/23

CON TRO L VALVE DATA SHE ETProject Agbami FPSo, Nigeria Tag # PV-4402A

Buyer HHI Item # 54

Owner Chevron Texaco Qty. 1

Inq. Rev. Date Model 100D

Prop. 030919-14711-5 Rev. Date 26Feb2004 D-SHT Rev. Dwg #

P.O. Application INJ COMP SUCT HDR TO HP FLARE

1 Fluid Gas - Customer Dened Crit Press psi A Crit Temp deg C

Units Max Norm Min Shut-Off

2 Gas Vol Flow Rate Nm3/hr 410011 137080 138873 Inlet Pressure (P1) Bar G 22.7 22.7 22.7



6 Inlet Temp. (T1) deg C 53.65 53.65 49.44




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 Piston


15 Pipe Matl In Carbon Steel Out Carbon Steel 40 Failure Mode Fail Close Via Volume Tank

16 Type Globe Size 14 X14inches 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 G

19 Rating(s) In 300 Std PN 50 Out 300 Std PN 50 44 Stem Orientation Vertical Up

20 Material A105 or WCB/A105 45 Manual Override Yes, Top Mounted/Side Access

21 Connect In RF Flange 46 N/A

22 Connect Out RF Flange 47 Positioner Type Smart Positioner

23 Flow Dir. Flow to Open (UTP) 48 Mfr / Model Fisher / DVC 6000 Series



26 Packing Type Standard 51 Cam Characteristic N/A


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/A33 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 VI

35 Seat Matl 410 SS HT 60 Open Time(s)

788-tp-fpso-applications.pdf

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