alanrosewall patersoncooke 151111032140 lva1 app6891
TRANSCRIPT
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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