merpro spe march 2006
TRANSCRIPT
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Topside Sand Handling Solutions
Tim Podger, Merpro
Second European Sand Management Forum
Aberdeen, March 2006
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Optimising separator performance
Enhancing downstream PWT systems
Protecting the integrity of produced water re-injection
systems
- through effective topside sand handling
Provide information from four case studies
Topside sand handling solutions
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Topside sand handling solutions
Merpro has developed a range of products for sand handling
Products incorporate Tore for sand/solids removal
They can be provided
as individual products for specific applications
or provided in combination to provide a complete topside
sand handling solution
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Tore - how it works
1 - Tangential feed
to swirl chamber
3 - Internal vessel pressure
forces slurry into discharge pipe
2 - Vortex generated fluidises solids
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Tore - what it does
Moves slurries of up to 40% solids by volume
1" Tore transports up to 4 tonnes of sand per hour
2" Tore transports up to 16 tonnes of sand per hour
Enables the removal of sand from vessels and the
transportation of slurries through pipelines
No moving parts = low maintenance
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Tore sand handling applications
Sand removal from separators
Sand cleaning
Sand transportation
De-sanding
Filtration
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ToreManifold
Removes sand from separators and vessels on-line
Sand removal from separators
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ToreManifold what it is
Tores manifolded within
base of vessel
Fluid introduced to Tores
Tore creates a vortex
which fluidises sand
Slurry exists through
discharge pipe
AIOC, Azerbaijan
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ToreManifold what it is
AIOC, Azerbaijan
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ToreManifold what it is
AIOC, Azerbaijan
BP Alaska, Prudhoe Bay
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ToreManifold demonstration
Click on the image to run the video clip
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Removal of sand from separators on-line
ToreManifold
Merpro acknowledges with thanks the permission of
Apache to present this case study
Case study 1 Apache Australia
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Produced sand inside production separator before
installation of Tore
Manifold
Case study 1 the problem
Apaches
Stag Platform,
Australia
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Case study 1 - results
Removes sand from separator on-line whenever required.
Apache activates them for half and hour every morningand evening
remove up to 10 tonnes sand per week
Eliminated unplanned shut downs to dig out sand previouspractice was 4 day shut downs to dig out every 3 months
In one year, eliminated 16 days of unplanned shut downs
Apache Stag, Australia
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Case study 1 - results
Eliminated associated shut down/dig out costs and HSEissues
Maintains vessel integrity
Enables separator to operate continuously at designefficiency, maintaining well fluid throughput at maximumlevels
Maximises revenue generation
Apache Stag, Australia
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Removal of sand from separators on-line
ToreManifold
Case study 2 Petronas Carigali
Merpro acknowledges with thanks the permission ofPetronas Carigali to present this case study
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Case study 2 the problem
Petronas Carigali Dulang B platform, Malaysia.
Shut downs every 6 months to dig out sand
Existing sand jetting system not working effectively due to
Jet nozzles and piping clogged
Drain line and valves eroded and clogged
Sand carry over to produced water system
Sand hardened and would not fluidise to flow through
drain nozzles No means to monitor how much sand left or removed
Petronas Carigali Dulang B,
Malaysia
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Case study 2 the solution
Tore
Manifold installed in HP separator Consists of 8 Tores in two banks of four
Configured in single line
2 inch inlet header for water; 2 inch outlet header for slurry Modifications to existing facilities minimised
Previous jetting system supports used to support Tore
Manifold
Petronas Carigali Dulang B,
Malaysia
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Case study 2 the solution
Operating data
Inlet pressure : 0.5 bar above vessel pressure
Outlet pressure : Free discharge to atmosphere
Inlet flow rate : 16m3/hour
Outlet flow rate : circa 16m3/hour
Inlet fluid : Treated water
Outlet fluid : Slurry (sand and water)
Petronas Carigali Dulang B,
Malaysia
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Case study 2 results
809 litres of sand collected in first month after
commissioning Annualised sand removal rate 9.7 kilolitres (15 tonnes)
Some loss of fine sand
Separator volume for oil and water separation is 92m3(based on normal 60% liquid level)
Accumulated sand would therefore result in loss of
residence time of 10.5%
More sand was removed by the B manifold closer to the
fluids inlet nozzle then the A manifold
Petronas Carigali Dulang B,
Malaysia
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Case study 2 results
Petronas Carigalis conclusions
Tore Manifold was easy to install, utilising existing vessel
nozzles
It is simple to operate with minimum controls No problems in utilisation at a practical level
It removes a significant volume of sand without causing any
operational or process interruptions
Petronas Carigali Dulang B,
Malaysia
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Case study 2 results
Petronas Carigalis conclusions ctd
Eliminated shut downs to dig out sand
Dulang B operations personnel have noticed better control
over the produced water discharge due to less sand level
interruption with the interface level reading
Petronas Carigali Dulang B,
Malaysia
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Case study 3 BP Schiehallion
Improving efficiency of produced water re-injection
systems through effective topside sand handling therole played by Tore
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Case study 3 BP Schiehallion
Merpro acknowledges with thanks the permission of the
Schiehallion partners to present this case study:
BP Exploration Operating Company Ltd
Shell UK Ltd Amerada Hess Ltd
Murphy Petroleum Ltd
OMV (UK) Ltd
Statoil Exploration (UK) Ltd
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Case study 3 the problem
Increasing produced water led to installation of PWRI
system as part of reservoir pressure support strategy
With increasing produced water came increasing sand
Smaller than expected particle size resulted in increasing
drop out from suspension later than expected in the processtrain
Resulted in elevated solids loading within the treated
produced water system
In 2004, 13 tonnes of solids were removed from key process
vessels
BP Schiehallion, UK
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Case study 3 the problem
Key factors that set solids loading limit for the PWRI system
well injectivity
erosion limits for pumps, pipework, well bore and
completion type
Despite pipework integrity and sand removal/disposalmethods in original design, increased solids loading within
the produced water stream had several adverse effects
including
filter blockage
accelerated pump erosion
BP Schiehallion, UK
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Case study 3 the problem
Within 4 months water seals and pump casings began to failwithin the water injection and produced water booster
pumps.
Wedge wire screen filters upstream of the water injection
pump blocked
Result the PWRI system was suspended one year after
commissioning
BP Schiehallion, UK
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Case study 3 the solution
Significant modifications made to the PWRI system - Tore
important element in this
Erosion and mechanical improvements
sand erosion probes fitted to each production riser
pumps changed out for high solids pumps
desanding cyclone replaced wire screens
BP Schiehallion, UK
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Case study 3 the solution
Sand removal and entrainment minimisation
sand jetting system in the slug catcher and first stage
separator - replaced with ToreManifold
ToreManifold installed in the degasser to remove the
finer grained sand settling out in the vessel to minimisere-entrainment into the produced water system
nucleonic profiler for oil/water/sand interface
measurement fitted to improve level control in the firststage separator
BP Schiehallion, UK
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Case study 3 lessons learned
Detailed understanding of sand production issues
sand particle size distribution
sand quantities
sand drop out points within the process
Equipment Specification
sand removal and sand handling equipment
pumps suitable for solids loading
Review the correct point in the process to remove sand fromproduced water
BP Schiehallion, UK
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Case study 4 Statoil Gullfaks C
Eliminating sand carry over problems into
produced water outlet through effective topside
sand handling
Merpro acknowledges with thanks the permission ofStatoil to present this case study
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Case study 4 the problem
Existing sparging system causing excessive sand in the
produced water outlet
Production restricted by additional jetting water introducedinto the separator
Statoil, Gullfaks C, Norway
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Case study 4 the solution
ToreManifold installed in production and produced water
separators
Statoil, Gullfaks C, Norway
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Case study 4 results
80 kgs of sand removed every 2 days from each separator
Fluidising effect of each Tore is localised
eliminated jetting system induced problems of solids in
the produced water outlet, giving improved operational
stability Feed water requirement reduced to 32m3/hour compared to
previous 100m3/hour
upstream and downstream equipment can be smaller
Statoil, Gullfaks C, Norway
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Case study 4 results
Since Tores cause minimal turbulence at the liquid
interface, and the feed water and slurry discharge rates arebalanced, the separator interface level remains unaltered
allows separation of liquids to continue unaffected while
solids are removed
Enabled Statoil to increase well fluid throughput by up to
30% - increasing oil production and revenues
Supports field life extension
Statoil, Gullfaks C, Norway
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Tore
Manifold atannual shut downinspection after oneyear of operation
No erosion inpipework or in vessel
Statoil describedvessel as clear ofsand
Case Study 4 results
Statoil Gullfaks C, Norway
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Conclusions
Operator experience with ToreManifold has demonstrated it
is an effective means of removing sand from separators
provides significant financial and operating benefits
eliminates unplanned shut downs to dig out produced sand removes sand on-line, enabling separators to operate at
design capacity on a continuous basis, maximising
revenues
protects downstream equipment from erosion e.g. PWRI
systems
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Thank you for your attention
Questions?