Pump Sizing Calculation

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NAE DEEP OFFSHORE PROJECT

ETAN FPSO

EQUIPMENT SIZING / VALIDATION REPORT

CD-FE

01

01/04/2014

Issued for Review

Date

Description

Validity Revision Status Number Revision Index

Company logo and business name

K.Ekwuluo

R.Ogunyemi

Contractor Prepared

Contractor Verified

Project name NAE DEEP OFFSHORE PROJECT

exploration & production Contractor logo and business name

M.Omotoso Contractor Approved

Company Checked

Company Approved

Company Document ID Job N. Contractor Document ID

XXX-IES-P-DOC-001 BW OFFSHORE

INTERNATIONAL ENERGY SERVICES LTD.

Facility and Sub Facility Name

Contract N. Scale

ETAN FPSO

n.a.

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EQUIPMENT SIZING / VALIDATION REPORT Software: Microsoft Word

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TABLE OF CONTENTS LIST OF TABLES ........................................................................................................................................... 5 LIST OF APPENDICES .................................................................................................................................. 5 LIST OF ABBREVIATIONS ........................................................................................................................... 6 1.0

INTRODUCTION.................................................................................................................................. 7

1.1

PROJECT OVERVIEW........................................................................................................................ 7

2.0

OBJECTIVES ...................................................................................................................................... 8

3.0

PUMP SIZING ...................................................................................................................................... 9

3.1

PUMP SIZING CRITERIA .................................................................................................................... 9

3.2

FLUID PROPERTIES ........................................................................................................................ 10

3.3

ASSUMPTIONS ................................................................................................................................ 11

3.3.1 PRODUCED WATER TRANSFER PUMP ......................................................................................... 11 3.3.2 WATER INJECTION BOOSTER PUMPS .......................................................................................... 11 3.3.3 WATER INJECTION PUMPS ............................................................................................................ 11 3.4

CALCULATION PROCEDURE .......................................................................................................... 12

4.0

RESULTS / EVALUATION ................................................................................................................ 13

5.0

CONCLUSION ................................................................................................................................... 14

6.0

REFERENCES: ................................................................................................................................. 15

APPENDICES .............................................................................................................................................. 16

This document is property of Eni S.p.A. Exploration & Production Division. It shall neither be shown to Third Parties not used for purposes other than those for which it has been sent.

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LIST OF TABLES Table 1

Equipment Index

Table 2

Liquid line sizing for pump suction & discharge

Table 3

Fluid Properties

Table 4

Summary of Results

LIST OF APPENDICES Appendix I

Produced water pump sizing calculation

Appendix II

Water Injection Pumps Sizing Calculation

Appendix III

Heat & Material Balance For Maximum Oil & Gas (Start-up)

Appendix IV

Heat & Material Balance For Maximum Water Case

This document is property of Eni S.p.A. Exploration & Production Division. It shall neither be shown to Third Parties not used for purposes other than those for which it has been sent.

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Sheet of Sheets 6 / 24 Validity Status

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exploration & production

LIST OF ABBREVIATIONS

Abbreviations

Meaning

bara

Bar absolute

barg

Bar guage

bpd

Barrels per day

FEED

Front End Engineering Design

FPSO

Floating, Production, Storage & Offloading

HMB

Heat & Material Balance

hp IESL Kg/m3 kW NAE

Horse power International Energy Services Limited Kilogram per cubic metre kiloWatts Nigerian Agip Exploration Ltd

NPSHA

Net Positive Suction Head Available

NPSHR

Net Positive Suction Head Required

P&ID psi SNEPCo

Piping & Instrumentation Diagram Pound per square inch Shell Nigeria Exploration & Production Company

This document is property of Eni S.p.A. Exploration & Production Division. It shall neither be shown to Third Parties not used for purposes other than those for which it has been sent.

Contractor Document ID

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1.0

INTRODUCTION

1.1

Project Overview

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Nigerian Agip Exploration Limited (NAE) and Shell Nigeria Exploration and Production Company (SNEPCo) are in the process of developing NAE Deep Offshore Block located approximately 150kilometers offshore Nigeria. In particular, the block is a 1,958 km2 block license located in the deepwater eastern portion of the Niger Delta in Nigeria, with water depths ranging from 1,200 to 2,400 m. The current development scenario involves production from subsea wells located in water depths around 1,750 - 1800 meters. The wells would be conveyed to a moored ship-shaped FPSO. The FPSO would be utilised for: a. Stabilisation, dehydration, storage and export of crude oil product, b. Dehydration, compression and export of gas, c. Separation and treatment of produced water, d. Seawater treatment; e. Produced water and Seawater injection for Reservoir pressure maintenance f. Power generation for FPSO marine, accommodation and process loads, g. Gas lift at riser base at an appropriate pressure The block (Fig. 1) comprises two discoveries, Zabazaba and Etan, which are separated by a significant seafloor canyon. The field is in about 1,950 m water depth and the distance between Zabazaba and Etan is about 30/40 km.

Figure 1: Block Location

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BW Offshore has therefore employed the services of IESL to carry out the Front End Engineering Design (FEED) for the new Water injection and Produced Water Treatment modules/systems. This document shows the process equipment sizing calculations carried out on the Produced Water Treatment and New Water Injection modules. 2.0

OBJECTIVES

The purpose of this document is to provide the sizing calculations for the both the Produced Water and Water Injection Pumps. Table 1: Equipment Index No.

Description

Tag

Quantity

P&ID Number(s)

1

Produced Water Transfer Pump

44PA101A/B/C (3x50%)

3

4295-IES-P-XB-44005.001

2

Water Injection Booster Pumps

29PA101 A/B/C (3x50%)

3

4295-IES-P-XB-29004.001

3

Water Injection Pump

29PA102 A / B

2

4295-IES-P-XB-29005.001

This document is property of Eni S.p.A. Exploration & Production Division. It shall neither be shown to Third Parties not used for purposes other than those for which it has been sent.

Company Document ID

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XXX-IES-P-DOC-001 exploration & production

3.0

PUMP SIZING

3.1

Pump Sizing Criteria

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The Water injection and injection booster pumps were sized in accordance with API RP 14E (Ref 8) and the Eni exploration & production design criteria reference document for process minimum requirement (Ref 9). The following criteria form the basis for the pump sizing as per API 14E (Ref 8): • Velocity in the suction pipe shall be between 2 - 3 ft/s (Table 2.3). • Velocity in the discharge pipe shall be between 6 – 9 ft/s (Table 2.3). • Pump should be sized to provide adequate head required and to ensure that the NPSHA exceeds the NPSHR (Ref 8) so that essentially no vapor will be flashed from the liquid as it enters the pump casing or cylinder. Similarly, Table 2 below shows the design criteria as specified in the Eni exploration & production design criteria. Table 2: Liquid line sizing for pump suction & discharge ∆P(bar) / 100m

SERVICE

Normal (Note 1)

Maximum (Note 1)

Maximum Velocity (m/s)

0.05

0.8

1.0

0.1

1.5

0.11

1.8

0.35

2.0

0.35

3.0

Pump Suction • Liquid @ bubble point or with dissolved gas ( ≥ 4”) • Liquid at bubble point or with dissolved gas ( 4”-8”)

0.07 0.07

• Liquid at bubble point or with dissolved gas ( ≥ 8”)

• Sub-cooled Liquid ( < 8”) • Sub-cooled Liquid ( ≥ 8”)

0.25 0.25

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Table 2: Liquid line sizing for pump suction & discharge (Cont’d) ∆P(bar) / 100m

SERVICE

Normal (Note 1)

Maximum (Note 1)

Maximum Velocity (m/s)

0.05

0.8

1.0

Pump Discharge • Lines ( < 4”)

• Lines ( ≥ 8”)

0.07

0.1

1.5

Note 1: For all calculations, reference was made to the normal value. 3.2

Fluid Properties The fluid properties for the Produced Water Transfer Pumps was taken from the Maximum Water Simulation case, while the fluid properties for the Water Injection Booster pumps and Water Injection pumps were taken from the Maximum Oil & Gas (Start-up) Simulation case. The table below shows the fluid properties from the respective Heat and Material Balance (HMB) Tables (Ref 4 & 5) which were used for the sizing. Table 3: Fluid Properties No.

Description

Tag

Flowrate (m3/h)

Flowrate (bpd)

Density (Kg/m3)

1

Produced water transfer pump

44PA101A/B/C (3x50%)

198.72

30,000

994.4

2

Water injection booster pumps

29PA101 A/B/C (3x50%)

132.40

20,000

1006

3

Water injection pump

29PA102 A / B (2 x 100%)

264.80

40,000

1006

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3.3

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ASSUMPTIONS Assumptions were made on individual pump sizing which await the actual values from the isometric drawing. Below are the series of assumptions. 3.3.1

Produced water transfer pump



Suction pipe length 10m



Suction static head 8m considering the vessel height.



Total K-factor (based on valves & fittings on the suction line) 6.89



Discharge pipe length based on 100ft (30.48m)



Discharge static head 10m



Total K-factor (based on valves & fittings on the discharge line) 2.89

3.3.2

Water Injection booster pumps



Suction pipe length 10m



Suction static head 8m



Total K-factor (based on valves & fittings on the suction line) 1.33



Discharge pipe length 10m



Discharge static head 10m



Total K-factor (based on valves & fittings on the discharge line) 4.74



A discharge pressure of 11 barg was used.

3.3.3

Water Injection pumps



Suction pipe length 10m



Suction static head 8m



Total K-factor (based on valves & fittings on the suction line) 0.637



Discharge pipe length 20m



Discharge static head 10m



Total K-factor (based on valves & fittings on the discharge line) 2.38

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3.4

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CALCULATION PROCEDURE The following methodology was used in performing the pump sizing / NPSH calculation a. Pipe Data & Fluid properties was gathered b. The absolute total pressure at pump suction was calculated. c.

The absolute total pressure at pump discharge was calculated.

d. The Differential head of the pumps was determined. e. The pump hydraulic power was determined. f.

The pump actual horse power was determined.

g. The Net Positive Suction Head Available (NPSHA) was calculated. Appendix I & II shows the detailed pump sizing calculation of the Produced Water transfer pumps, Water Injection Booster Pumps and Water Injection Pumps.

This document is property of Eni S.p.A. Exploration & Production Division. It shall neither be shown to Third Parties not used for purposes other than those for which it has been sent.

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4.0 RESULTS / EVALUATION A summary of the calculation result is giving in the table below.

Table 4: Summary of Results Produced Water Transfer Pump (44PA101A/B/C)

Water Injection Booster Pump (29PA101A/B/C)

Water Injection Pump (29PA102A/B)

Differential Head (m)

28.668

84.068

1407.640

Flowrate (bpd)

32,998*

20,000

40,000

Hydraulic Power (hp)

22.73

40.85

1371.19

Estimated Horsepower (kW)

19.51

35.60

1165.01

NPSHa (m)

37.84

48.02

128.99

Pump Efficiency

85.64

83.72

86.31

Suction

0.02

0.025

0.025

Discharge

0.18

0.294

0.237

Suction

0.84

0.7

0.8

Discharge

2.06

2.0

2.2

Pump Parameters

∆P / 100m (bar)

Velocity (m/s)

The pressure drop per length (∆P / 100m) values were obtained from the Process Calculation Report (Ref 10) which captured all process lines inclusive of all pump suction and discharge lines. *A flow margin of 10% was added to the produced water pumps.

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5.0 CONCLUSION The results obtained from the pump sizing calculation as shown in Table 4, indicates that the pump suction and discharge lines for the Produced Water transfer pumps, Water Injection Booster Pumps and the Water Injection pumps adequately meet the specified criteria in section 3.1. Appendix I & II show the detailed sizing calculation spreadsheets of the Produced and sea water pump sizing respectively.

This document is property of Eni S.p.A. Exploration & Production Division. It shall neither be shown to Third Parties not used for purposes other than those for which it has been sent.

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6.0 REFERENCES: 1.

Basis of Design Etan Development - 325300BGRB12000.

2.

Process Design Philosophy - 4295-BWO-P-FD-00001.

3.

Produced water transfer Pumps P&ID – 4295-IESL-P-XB-44005.001.

4.

Heat & Material Balance for Maximum Oil & Gas (Start-up).

5.

Heat & Material Balance for Maximum Water Case.

6.

Water injection booster pumps P&ID - 4295-IES-P-XB-29004.001.

7.

Water injection pumps P&ID – 4295-IES-P-XB-29005.001.

8.

API 14E – Recommended Practice for Design & Installation of Offshore Petroleum Production Platform Piping Systems (Section 2.3b).

9.

Eni Exploration & Production Design Criteria (10009.HTP.PRC.PRG) – Process Minimum Requirement

10.

Process Calculation Report (XXX-IES-P-DOC-002)

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APPENDICES

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APPENDIX I Produced water pump sizing calculation

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APPENDIX II Water Injection Pumps Sizing Calculation

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APPENDIX III Heat & Material Balance For Maximum Oil & Gas (Start-up)

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APPENDIX IV Heat & Material Balance For Maximum Water Case

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