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    Slurry Pipelines Conference 2015, Khouribga to Jorf Lasfar Pipeline , Slide 1

    www.PatersonCooke.com

    The Design and Engineering of the 187 km Khouribga to

    Jorf Lasfar Phosphate Slurry Pipeline Alan Rosewall, Paterson & Cooke, Perth

    Slurry Pipelines and Flow Equipment Conference 2015

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    Slurry Pipelines Conference 2015, Khouribga to Jorf Lasfar Pipeline , Slide 2

    Introduction

    Morocco now has one of the largest ore slurry pipeline

    systems in the world The main delivery pipeline is 187 km long and transports

    4400t/h of phosphate ore

    The system has become an integral part of the OCP value

    chain and their expansion plans

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    Slurry Pipelines Conference 2015, Khouribga to Jorf Lasfar Pipeline , Slide 3

    Introduction

    Client: OCP

    Client representative: JESA

    EPC Contractor: Tekfen Construction

    Design engineers: Paterson & Cooke and Tekfen

    Engineering

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    Slurry Pipelines Conference 2015, Khouribga to Jorf Lasfar Pipeline , Slide 4

    Construction Statistics

    50 000 tons of pipeline steel

    1.7 million man days

     At the peak of construction - 1800 people and 800

    construction machines were employed

    This paper provides a system overview and highlights some

    of the challenges

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    Slurry Pipelines Conference 2015, Khouribga to Jorf Lasfar Pipeline , Slide 5

    Location

    Diameter Nominal Length

    Daoui Feeder DN450 22 km

    MEA Feeder – low grade DN400 1.8 km

    MEA Feeder – high

    grade

    DN300 1.8 km

    Halassa Feeder DN500 15 km

    Ouled Fares Feeder

    (future)

    DN500 10 km

    Mainline MEA to Jorf DN900 187 km

    Total 227 km (10 km

    future)

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    Slurry Pipelines Conference 2015, Khouribga to Jorf Lasfar Pipeline , Slide 6

    System Description

    • 14.9 km pipeline

    • 1500 t/h• 2 trains of 5 pumps

    each

    • 1.8 km pipeline

    • 700 & 1400 t/h

    • Utilises thickener

    underflow pumps

    • 22.2 km pipeline

    • 1400 t/h

    • 2 trains of 4 pumps

    each

    • Variable choke

    station

    • 187 km

    pipeline• 4400 t/h

    • 2 trains of 6

    pumps each

    • Valve Station

    • Pressure

    Monitoring

    Stations

    • Variablechoke station

    • 8 Storage

    Tanks

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    Slurry Pipelines Conference 2015, Khouribga to Jorf Lasfar Pipeline , Slide 7

    Feeder Pipelines – Daoui

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    Slurry Pipelines Conference 2015, Khouribga to Jorf Lasfar Pipeline , Slide 8

    Feeder Pipelines – El Halassa

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    Slurry Pipelines Conference 2015, Khouribga to Jorf Lasfar Pipeline , Slide 9

    Feeder Pipelines – MEA

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    Slurry Pipelines Conference 2015, Khouribga to Jorf Lasfar Pipeline , Slide 10

    Feeder Pipelines

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    Slurry Pipelines Conference 2015, Khouribga to Jorf Lasfar Pipeline , Slide 11

    Main Pipeline Route

    Key Statistics

    187 km long

    Head station

    elevation: 650m Maximum

    elevation: 770m

    Discharge

    elevation: 100m Maximum slope:

    12%

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    Slurry Pipelines Conference 2015, Khouribga to Jorf Lasfar Pipeline , Slide 12

    Control of Main Pipeline

    Control of the pipelinemust ensure

    No slack f low on the

    predominantly

    downhill route profile

    High enough velocityto avoid solids

    deposition on pipe

    invert

    Turbulent rather than

    laminar flow Flow rate and

    pressure within the

    design limits

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    Slurry Pipelines Conference 2015, Khouribga to Jorf Lasfar Pipeline , Slide 13

    Control of Main Pipeline

    The system mustaccommodate a

    wide range of

    operating

    conditions whilesatisfying the

    design criteria

    The figure shows

    the relationshipbetween

    volumetric and

    solids throughput

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    Slurry Pipelines Conference 2015, Khouribga to Jorf Lasfar Pipeline , Slide 14

    Control of Main Pipeline

    Trained operatorsguided by a visual

    grade line display

    of the system

    They select flow

    rate and chokingwithin limits

    System

    automatically

    controls to flow rate

    by adjusting speedsof pumps 1,2,5,6

    and stopping or

    starting pumps 3, 4.

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    Slurry Pipelines Conference 2015, Khouribga to Jorf Lasfar Pipeline , Slide 15

    Control of Main Pipeline

    The valve stationis required to

    divide static head

    during shut-down.

    Pressure

    monitoringstations monitor

    intermediate

    conditions along

    the pipeline.

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    Slurry Pipelines Conference 2015, Khouribga to Jorf Lasfar Pipeline , Slide 16

    Control of Main Pipeline

    Instruments used for control and monitoring of the overlandpipeline:

    • Tank level transmitter and level switches

    • Pressure transmitters

    • Flow meters

    • Density meters

    • BPL Analysers

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    Slurry Pipelines Conference 2015, Khouribga to Jorf Lasfar Pipeline , Slide 17

    Control of Main Pipeline

    Batch Tracking:• Different grades of phosphate ore are mined, processed in

    the wash plants and fed into storage tanks dedicated to

    the pipeline.

    • The control system tracks these batches and is able toautomatically control valves in order to directed these into

    specific tanks.

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    Slurry Pipelines Conference 2015, Khouribga to Jorf Lasfar Pipeline , Slide 18

    Equipment – Piping

    Overland piping dimensional standard according to API 5L

    Main line has API 5L X70 material

    Feeders have API 5L Grade B material

    Flanges are ASME B16.5 and B16.47 Series A with ASTM

     A105 and ASTM A694 F70 material

    Overland pipelines are internally lined with HDPE

    Slurry station pipelines are lined with Polyurethane or

    rubber 

    Water pipeline are internally lined with Epoxy

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    Slurry Pipelines Conference 2015, Khouribga to Jorf Lasfar Pipeline , Slide 19

    Equipment – Piping

    The test loop is used to monitor

    the pipeline hydraulic losses

    before the slurry enters the

    main pipeline. The

    requirements made design and

    manufacture a challenge:

    • Matches the mainline ID

    • Smooth joints despite being

    made up of several

    relatively tight radius bends

    • HDPE liner sections were

    custom made for eachspool and have a finely

    grooved surface finish

    creating smooth join

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    Slurry Pipelines Conference 2015, Khouribga to Jorf Lasfar Pipeline , Slide 20

    Equipment – Piping

    High pressure PU-lined pipe spools for pump and

    choke stations• Cast into straights, bends and tees using unique, removable patterns

    • Special rubber lined steel gaskets with inward facing “ears” contain

    the pressure while allowing a smooth transition between spools

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    Slurry Pipelines Conference 2015, Khouribga to Jorf Lasfar Pipeline , Slide 21

    Equipment – Main Pumps

    Six operating and six standby

    1850 kW motors with air-cooledgearboxes

    Separate, wear resistant volute

    liners

    Pressure limits of 6200 kPa

    Variable speed drives give a

    large head range from 10m to

    50m for slurry and 80m on water 

    Separate gland seal water

    plunger pump for each slurry

    pump

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    Slurry Pipelines Conference 2015, Khouribga to Jorf Lasfar Pipeline , Slide 22

    Equipment – Terminal Choke Station

    Choke station designed for 10MPa

    Four loops each with two ceramic orifice plates

    Bursting

    disk take-off 

    Fixed

    chokes

    Variable choke

    bypass

    Slurry feedline

    Choke

    loops

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    Slurry Pipelines Conference 2015, Khouribga to Jorf Lasfar Pipeline , Slide 23

    Equipment – Terminal Choke Station

    The orifice plates are different sizes and by

    combining various combinations, the control systemprovides a wide range of choking

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    Slurry Pipelines Conference 2015, Khouribga to Jorf Lasfar Pipeline , Slide 24

    Equipment – Terminal Choke Station

    The effect of choking on the hydraulic grade line

    High flow Low flow

    Choke

    head

    Choke

    head

    Pumping

    head

    Pumping

    head

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    Slurry Pipelines Conference 2015, Khouribga to Jorf Lasfar Pipeline , Slide 25

    Equipment – Tanks

    Each tank is 20m x 20m 250 kW agitators

    Head Station: 4 tanks(2 groups of 2 tanks each)

    Terminal Station: 8 tanks(3 groups of either 2 or 3

    tanks each)

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    Slurry Pipelines Conference 2015, Khouribga to Jorf Lasfar Pipeline , Slide 26

    Hydrostatic Testing

    Pipeline must be pressure tested to 1.1 the design pressure

    for not less than 4 hours (ASME B31.4) With multiple elevation changes, pipeline must be divided

    into sections for testing

    Plan was devised to

    • Minimize number of test sections

    •  Allow filling from Oum er Rbia River 

    • Minimize water discharge

    •  Allow test and filling equipment to be removed after

    testing

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    Slurry Pipelines Conference 2015, Khouribga to Jorf Lasfar Pipeline , Slide 27

    Hydrostatic Testing

    Test Planshowing testsections, transferpoints and testheads

    Transfer point

    between

    sections 2 and 3

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    Slurry Pipelines Conference 2015, Khouribga to Jorf Lasfar Pipeline , Slide 28

    Conclusion

    The sheer size and complexity of the OCP Khouribga to Jorf 

    Lasfar phosphate slurry pipeline presented a number of uniqueengineering challenges, all of which were overcome. The

    system has since been commissioned and it provides OCP

    with a highly efficient transport system which is an essential

    component of their value chain.

    Pipeline

    ROW