dps group overview
DESCRIPTION
sheet showing fps files lolTRANSCRIPT
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DPS Overview
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DPS Group
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Overview
Process system integrators
Multi-disciplined engineering team
Innovative technical solutions
Project execution excellence
Recent clients include:
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Core Skills
Field Development Plans
Basic/Conceptual Engineering
FEED & Detailed Designs
Process System Design, Supply & Support
Process Package/Module Study
Construction and Commissioning Supervision
FPSO and Floating Production Expertise
MOPU
Well Head Platform Design
CPPs
Brownfield Engineering
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Portfolio of latest design and process tools including:
HYSYS
TASC
FLARENET
AutoCAD Full
Navisworks
PDMS
MicroStation
STAAD.Pro
PV Elite
SACS
Caesar II
UniSim
Design Tools
Que$tor
SmartPlant PID
SmartPlant Review
Intools
PDS
PipeFlo
ProEngineer
PipeSim
FlareSim
PipeNet
In addition to many in-
house bespoke sizing
software
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FPSO
Process topsides
Integration
Conversion
Fixed Platforms
Jackets
Topsides
WHPs
CPPs
MOPU
Jack up conversion
Semisubmersible
Non-ship shaped
Brownfield
Offshore upgrades
FPSO recertification
Concept to FEED to Detail Design
Total Offshore Capability
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Independent & Tailored Service
QUE$TOR Utilisation
Benchmarked Solution
Competitive Rates
Marginal Field & Lower Flow Rate Specialists
Deliverables
Review of available options (floating v fixed)
State of art review
High value options
Concept Selection
CAPEX/OPEX
Basic Engineering and Field Development Studies
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Typical Que$tor Output
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Study Basis
Option
Review
Definition of
Preferred Option
Final Report
State of the Art Review
QUE$TOR Data
Client Data DPS Data
Export Options
Market / DPS Data
Flow Assurance
Phase 1
Activity 1 Project Management
Activity 2 Study Basis Definition
Activity 3 Definition of new build development options
Activity 5 State of the Art review
Activity 6 Coarse screening of development options
Phase 2
Activity 1 Project Management
Activity 4 Re-use of existing facilities
Activity 5 State of the Art review
Activity 7 Fine screening of development options
Activity 8 Hydraulic Modelling
Activity 9 Final Report
State of the Art Review
Typical Concept Screening Activities
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TLP (148m (Hutton) to 1,500m)
FPSO (up to and beyond 3,000m)
Spar (500m up to and beyond 3,000m)
Semi-submersible (75m (Argyll) up
to and beyond 3,000m)
Deepwater Platform Options
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Plus lots of other acronyms
Other Deepwater Platform Options
Control Buoy Subsea to Shore (subsea processing) Ormen Lange
+ Subsea to Platform
Compliant Towers
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Basic Evaluation Criteria All Concepts
Field Life
Remoteness of field location/location of infrastructure
Reservoir structure
Number of wells / drilling centres
Dry Tree or Wet Tree
Drilling or work over capability
Production Capacity
Total Topsides weight
Motion Characteristics
Riser Technologies
Installation Method
Constructability and lead time
Concept maturity
Field Operators experience of concept
CAPEX
OPEX
Abandonment Costs
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OPTION 1
Minimum Topsides
OPTION 2
Medium Topsides
OPTION 3
Maximum Topsides
Field Located Facilities 6 well slots (5 + 1 spare) Production & test manifold Topsides MPM for well tests Topsides pig launcher (remote operation) Topsides UTU Topsides crane (5te capacity) Small power (batteries) NavAids
Dry 110te Operating 130te
Field Located Facilities 6 well slots (5 + 1 spare) Production & test manifold Topsides MPM for well tests Topsides pig launcher (remote operation) HPU Topsides UTU Topsides crane (5te capacity) Solids removal unit (retrofit) Helideck Small power (batteries) Free Water Knock Out (at host)
Dry 180te Operating 210te
Field Located Facilities 6 well slots (5 + 1 spare) Production & test manifold Topsides MPM for well tests Topsides pig launcher (remote operation) HPU Topsides UTU Topsides crane (30-40te capacity) Solids removal unit Helideck Personnel shelter & emergency lifecraft FW pump Small power (batteries) Free Water Knock Out (at host)
Dry 600te Operating 760te Work-over equipment included 100te (CTU dry)
Topsides Definition
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Lightweight
Jacket
Steel Braced
Monotower
Conductor
Supported
Self-Installed
Platform
Light Weight Structure Options
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Project: Lerek Field Development
Location: Offshore Terengganu
Client: Newfield Peninsula Malaysia Inc
Central Processing Platform
Production :45000 BLPD
4-Leg Jacket
Production Separator
Heat Exchanger
Produced Water Treatment
Free water knock out
Export Pumping
Water Inject
Power Gen (GTG)
Flare System
LQ (30 People)
Utilities
Pipelines
WP-1:
Production :30000 BLPD
4-Leg Jacket
4 wells
Test Separator
Production/Test/Gas lift Manifold
WP-2:
Production :15000 BLPD
4-Leg Jacket
2 wells
Test Separator
Production/Test/Gas lift Manifold
Utilities
Temporary Shelter
Basic / FEED Case Study
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Project: Fry Field Development
Location: Offshore Norway
Client: Larsen Oil & Gas
Front end design study to provide process topsides
and interfacing solution for jack-up destined for the
North Sea.
Process footprint was critical so module
design and layout was important.
Cost estimate included in final solution.
2007 Froy
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PROJECT MANAGEMENT/ ENGINEERING
TOPSIDES MODULES
100,000 bpd
FEED Case Study
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Project: Dulang Field Development
Client: PetroMalaysia Sdn Bhd
Provision of Engineering Services for Conceptual
Engineering of Dulang Full Field Development
Three new wellhead platforms (DL-DX. DL-AX & DL-E)
One new processing platform (DL-BX).
Completed all engineering to pass Petronas MR4
development gate
Concept / FEED Case Study
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Project: Kambuna Field Development, Indonesia
Client: Serica Energy
Provision of Concept selection to review offshore vs
onshore process requirements to meet the onshore pipe
gas specifcation.
Client had originally selected a FPSO, but our study
worked showed that a wet gas pipeline with onshore
treatment was the most economic solution and this was
carried through to detail design and project completion.
Basic Engineering Case Study
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Project: Cendor Phase II FEED
Location: Offshore Terengganu
Client: Petrofac (Malaysia PM304) Limited
1. Wellhead Platform 1 (WHP-1)-Max Production: 40,000BLPD
2. Wellhead Platform 2 (WHP-2)-Max Production: 56,000BLPD
3. Wellhead Platform 3 (WHP-3)-Max Production: 56,000BLPD
4. FPSO -Max Production:80,000BLPD (marine, mooring and
topsides)
5. Removal of existing MOPU
6. Infield Pipelines
7. Submarine Cables Between CPP & WHP-3
8. Pipelines to ANDR-A
Basic / FEED Case Study
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FPSO: D1 Field
Location: West Coast India
Client: ONGC
Project Management Consultant for specifications
of appropriate FPSO for D1 marginal field
Includes assistance preparing ITT through to
vessel commissioning
FPSO conversion rather than new build for fast
track project
FPSO Consultancy
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DPS- Recent FPSO Topsides Projects
2012/2013 Dana Western Isles North Sea
Detailed Engineering Of Topsides (New Build)
2010/2012 OSX-1 Brazil (Heavy Oil)
Detailed Engineering Of Topsides (Upgrade)
2011/2012 Petrofac Berantai Malaysia
Detailed Engineering Of Topsides (Upgrade)
2009/2011 EMAS Lewek Vietnam
Detailed Engineering Of Topsides (Conversion)
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FPSO: Berantai
Location: Malaysia
Client: Keppel / Petrofac / Petronas
Upgrade of the East Fortune FPSO to make it
suitable for Berantai Field in Malaysia
Includes 9 new modules and significant
upgrading
FPSO Topsides Case Study
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FPSO before upgrade FPSO after upgrade
Berantai FPSO upgrade
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FPSO: Cascade & Chinook
/ BW Pioneer
Location: Gulf of Mexico
Client: BW Offshore
First FPSO for Gulf of Mexico production scheduled 2011
Storage capacity - 600,000 barrels of oil
FPSO installed in a water depth of 2,600 metres
Disconnectable during storms
2008 Cascade & Chinook
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PROJECT MANAGEMENT/ ENGINEERING
TOPSIDES MODULES
80,000 bpd 16 mmscfd
FPSO Topsides Case Study
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EPC detailed design and supply of the
- M10 (Main Production) &
- M30 (Flare Knock-Out) modules
Topsides process interface engineering
Design of process pipe rack
Flare system design
Cascade & Chinook DPS Scope
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Module 3D Software used FPSO Autodesk Inventor CSU Module Intergraph PDS Flare Module Intergraph PDS Pipe Rack Aveva PDMS M60 A&B Gas Compression CADWorx M61 TEG Module Bentley Autoplant
5 x 3D Software Packages
Clash Checking
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Interface Engineering
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FEED
Detail
Delivery
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P30: Compression Module
(20.7x21x13.4m)
P40: Metering Skid
(10x4.25x2m)
P50 : Water Injection Module
(18x10.8x13.4m)
Z10: Blast
Wall H10:
Helideck
L10: Living
Quarter
O10: Office
Block
U10: EIT
Block
U40 : Power Generation
Area
P20: Separation Module
(20.7x18.6x13.4m)
F10: Flare Boom
P10: Pigging & Manifold Module
(13x7.7x7.4m)
TEG Skid
Western Isles FEED Verification
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FPSO Topsides Case Study
FPSO: OSX-1 FPSO
Location: Brazil
Client: Keppel / BW Offshore
Upgrade of the new-build Nexus 1 FPSO
to make it suitable for the OSX Waimea
heavy oil field (API 17.6) offshore Brazil
Involves 7 new modules including
Inlet Manifold
Crude Heating
Water Injection
Fuel Gas Compression
Power Module
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everything in pink is a change
OSX-1 FPSO
Significant Upgrade Project
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OSX-1 FPSO
PDMS modelling through to completion
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FPSO: Chim Sao Dua
Location: Vietnam
Client: EMAS / Premier Oil
Topsides Detailed Engineering for CSU,
Injection Water Treatment and Flare Modules
Also responsible for entire process topsides
piping interface engineering
Successful through design competition
2009 Chim Sao
Dua
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Gas
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Gas
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PROJECT MANAGEMENT/ ENGINEERING
TOPSIDES MODULES
80,000 bpd 50 mmscfd
FPSO Topsides Case Study
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CRUDE STABILISATION
FLARE KNOCK OUT
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FLARE KNOCK OUT MODULE
WATER INJECTION
CRUDE
STABILISATION &
PRODUCED WATER
TREATMENT
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FPSO: Ruby FPSO formally Ruby
Princess
Location: Vietnam
Client: MISC / MMHE
DPS to design and supply the complete process
topsides
FPSO will replace the FPSO Ruby Princess,
and have the ability to process 30,000 bopd
2008 Ruby 45,000 bpd 29 mmscfd
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CSU
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TOPSIDES MODULES
FPSO Topsides Case Study
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FPSO: Nexus FPSO
Location: (Norway) now Brazil (OSX)
Client: Samsung Heavy Industries
DPS responsible for the design of separator (60,000
bopd) and glycol dehydration packages (~100
MMSCFD unit including TEG Contactor, and Glycol
Regeneration unit) part of Nexus FPSO project destined for North Sea
Partnership with Whasung Industries Company Ltd
(Korea) who are responsible for fabrication
Now OSX-1 (DPS undertaking upgrade)
FPSO Topsides Case Study
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FPSO: Oyo
Location: Nigeria
Client: Bumi Armada
DPS scope initially involved the FEED elements
of the entire process topsides design and
integration
Extended to include detailed designn
2008 Oyo
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PROJECT MANAGEMENT/ ENGINEERING
TOPSIDES MODULES
45,000 bpd 60 mmscfd
FPSO Topsides Case Study
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FPSO: East Fortune
Location: Singapore
Client: Nortechs FPSO / Songa
Generic FPSO
Following on from the execution of conceptual
and FEED studies, execution of EPC. Vessel
fabrication China, module fabrication and vessel
conversion in Singapore
DPS involved in looking at suitability for various
feilds Basi
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Heating/C
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TOPSIDES MODULES
2007 East
Fortune 30,000 bpd 35 mmscfd
FPSO Topsides Case Study
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FPSO: Bunga Kertas
Location: Malaysia
Client: MSE (Now MMHE)
Built in Malaysia, a first for MSE, DPS provided
the engineering for MSEs first EPC contract.
Responsible for all detailed engineering design
activities, including CSU; Produced Water,
Gas Compression & Utility packages;
Structural design through to the full
topsides integrated control systems.
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TOPSIDES MODULES
2004 Bunga Kertas
30,000 bpd 40 mmscfd
FPSO Topsides Case Study
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BW. Carmen Upgrade
Ithaca Athena
North Sea
FPSO Topsides Case Study
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Name: D-111 (Dolphin)
Location: Angola (West Morsa)
Client: Angola Drilling Contractors / Sonangol
Full EPC for conversion of jack-up drilling rig into
production facility for marginal field offshore Angola
20,000 bpd oil production
Remote Un-manned Wellheads
33km export pipeline to FPSO
Produced by 10 Electric Submersible Pumps
FPSO Topsides Case Study
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Detail Design of Wellhead Platform for
Newfield West Belumut Field
Jacket Engineering
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Name: Khurmala Dome Field Development
Location: Northern Iraq
Client: Kar-AvrAsya / SCOP
Major total Greenfield development - 3 separate sites
100,000 bopd of oil & 100 mmscfd of gas
Engineering design and provision of
domain expertise in all engineer aspects
In-country construction and creation of jobs
Onshore Engineering
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Name: Bangora Expansion
Location: Bangladesh
Client: Tullow Oil
Receipt & review of Basic Engineering docs with site
visit to understand facilities concept, layout and
verify as-built information
Detailed Engineering Schedule and associated CTR's
Preparation, submittal, review & final approval of Detailed
Engineering deliverables list
Weekly & monthly reports against agreed schedule and the
associated CTR's
Onshore Engineering
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Name: Bangora IIC Development HDPC
Location: Bangladesh
Client: Tullow Oil
Receipt & review Phase IIA of detailed design documents and
drawings
Review of vendors document & drawing of the HDPC package
Detailed civil & structural engineering & review of the HDPC
package
Detailed Engineering Schedule and associated CTR's
Preparation, submittal, review & final approval of Detailed
Engineering deliverables list
Onshore Engineering
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Client: Texaco and Mariner Expro
Field: Mariner, UKCS
Scope: Extended Well Test (EWT) package
API: 14.5
Client: Texaco
Field: Captain, UKCS
Scope: EWT work including pre-separation
hydrocyclones, deoiling hydrocyclones and offshore
trials test work
API: 20.5
Client: Santa Fe Snyder
Field: Carauna Field FPSO, Offshore Brazil
Scope: Design of 5,000bpd crude oil and produced
water treatment process topsides module,
including centrifuge and coalescer.
API: 19
Client: Chevron
Field: Bressay Field, UKCS
Scope: Review the process facilities required to complete
an EWT vessel.
API: 11
Client: TK Petrojarl/Petrobras
Field: Siri Field, Brazil
Scope: Electrostatic coalescer
API: 12.8
Heavy Oil Experience
Client: OSX
Field: Wamea Field, Brazil
Scope: Topsides Detailed Design
Conversion for Heavy Oil
API: 17.6
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HP Ref.
HM
AGRU
DEHYDRATION
AND
MERCURY
REMOVAL
LNG
FUEL GAS
FEED GAS
CONDENSATE TO CRUDE PROCESSING
COOLING
WATER
COOLING
WATER
COOLING
WATER
LP Ref.
COOLING
WATER
M
M
GT
FUEL GAS
LNG
MiniLNG (Associated Gas)
Onshore / Offshore
Liquefaction Process
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DPS Group
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Dedicated development facilities
Increasing patent portfolio
Focus in innovation and creativity
Separation and filtration specialists
Oil / water flow loop
Online reporting and data management
Available for oil companies to outsource
R&D Facilities
R&D Centres in
Portishead (UK) and
Utah (USA)
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Multiphase separation system
Enhanced gravity separator with 5 phase capability:
i. Liquid heavy phase
ii. Liquid light phase
iii. Solids slurry sub-micron particles iv. Rag / emulsion layer
v. Gas
Flexible operation ability to deal with 100% oil 100% water with no change of internals
Shale gas (frac water flow back),
Heavy oil dehydration
PWT (the difficult streams)
Bilge water treatment
HydroLoc The Versatile Centrifuge
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HydroLoc Internal Arrangement
Fluid Inlet
Solids Discharge
NRV
Solids Collection
Funnel
Gas Volume
Annulus
Water Outlet
Oil Outlet
Gas Outlet
Emulsion/ Rag
Layer Outlet
Internal Jetting
Nozzles
Solids Collection
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Extensive Testing of Solids Evacuation Valves in DPS Test Rig.
Solids Evacuation from HydroLoc
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HydroLoc
30GPM unit on test in
our R&D facility in Utah
30GPM unit on shale
gas project in Colorado
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Results on Frac Water Flow Back
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HydroLoc Extensive Performance Trials
5gpm HydroLoc on
Performance Trials in
DPS UK Flow Loop
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Typical HydroLoc P&ID
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Interface Level Control
In the Hydroloc
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The skid dimensions = 8ft x 8ft x 8ft (2.44m x 2.44m x
2.44m)
Plant air at 150psi (10.3 bar) through a line
Electricity supply 480V 100A 3 phase 60 Hz Number 2
wire
Inlet process connection is 1 male camlock
Water outlet, oil outlet and solids outlet are 1 female camlock connections
A standard Nitrogen cylinder and spare cylinder are
required
H-5 Pilot Plant (Haz. Area Rated)
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Online solids management no shutdowns
Zoned removal and disposal of solids
No moving parts or wear high availability
Slurry density preset for optimal process
performance
Sand Cleaning for discharge overboard
Solids Management CyFlo
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Cyclone Design
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Well Fluids
Gas
Oil
Water
Where do we Manage Solids in Process?
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Upstream of Choke
Well Fluids
Gas
Oil
Water
Solids
Installed Subsea or Surface
Prevent erosion in piping/risers
Prevent erosion in choke
Cyclone
Vessel
Fluids
Inlet
Fluids
Outlet
Isolation
Valves,
Integral
DB&B
Solids
Discharge
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Upstream of Production Separator
Well Fluids
Gas
Oil
Water
Solids
Prevent solids entering production separator
Solids actively removed
Multi phase cyclone design
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Removal from Production Separator
Well Fluids
Gas
Oil
Water
Separator designed to retain solids
Solids removed on-line with no impact of separation performance
So
lids
Water
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Downstream of Production Separator
Well Fluids
Gas
Oil
Water
Solids
Solids removed from produced water stream
Simpler single phase cyclone design
Separator designed to carry solids in water outlet
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Cleaning Solids Offshore?
Clean Solids Discharge
Solids from Production
Clean Produced Water
Oily Water
Solids
Accumulation
Vessel Jet Pump
Cleaning
Cyclone
CyFlo
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Case Study P57 FPSO (Petrobras) Design of Sand Wash
Package and Supply of Internals
5 off 316 Manifolds - 20 CyFlo Units
Crude Degassers & Test Separator
Cascade & Chinook FPSO
7 off Duplex Manifolds - 28 CyFlo Units
1st US Gulf of Mexico FPSO
Cascade & Chinook BW / PAI
4 CyFlo Manifolds for Vietnam - 16 CyFlo Units
for Production Separators
Ruby FPSO Premier Vietnam
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Solids Management Technology
Options
DPS provides a total solids
management solution
Offline Sand Removal
Online Sand Removal
Atmospheric Transfer
Solids Cleaning
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Deoiling Hydrocyclones - Evolution
High Flow
Low Differential Pressure
Combined Desanding and
Deoiling
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The Right Hydrocyclone for the
Right Duty
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Combined Desander and HFD
Inlet
Water Outlet Solids Outlet
Oily Reject
Desanders HFD
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Grade efficiency of 20
microns (de-sander)
Reference - typical example of solids distribution from oil producing wells Sand Management Network presentation (Aberdeen)
Combining de-sanding and de-oiling with a grade efficiency circa d95 20 microns gives the following benefits:
o 95% solids removed (by volume)
o Coalesce oil droplets, increasing grade efficiency of de-oiling hydrocyclone stage
o Combine de-sanding and de-oiling in same cyclone
Efficiency of Separation
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Water Polishing for Discharge
As water discharge limits have reduced from 40ppm to
15ppm or less then tertiary
treatment is required
Compact Flotation has been favoured
DPS offer alternative Degassing Self Cleaning
Filter (DSCF)
Based on High Flux Media Filtration
Combines Degassing so no need for separate degasser
upstream
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DSCF Principle of Operation
1. Inlet Degassing
Uses Cyclonic inlet
optimised with CFD
2. Three Band Media Filter
1. Fine Media
2. Coarse Media
3. Media Support
3. Active Media Wash
System
All media bands can be
washed independently and
actively using CyFlo and
Cyclone
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Gas
Oil
Water
Standard Water
Treatment Scheme
Degasser after primary separators and hydrocyclones
Use of floatation flocculant
2 stage floatation achieves 15ppm oil in water
Reject
Compact
Floatation
Degassin
g Vessel
Gas
Oil Productio
n
Separator
Hydrocyclon
e
Reject
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Gas
Oil
HFD + Degassing Self Cleaning Filter
Recycle
Water
Media
Cleaning
DSCF
Productio
n
Separator
HFD
Hydrocyclon
e
Gas
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Electrostatic Coalescers
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Glycol Dehydration Packages
Project: Knarr FPSO
Location: Norwegian North Sea
Client: SHI / TK / BG
Project: Ruby FPSO
Location: Vietnam
Client: Emas / Premier
Project: Khalda
Location: Onshore Egypt
Client: Petrofac
Project: OSX FPSO
Location: Offshore Brazil
Client: SHI / OSX
Project: Oyo FPSO
Location: Offshore Nigeria
Client: Bumi Armada
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Specialist Packages Knarr FPSO
DEBUTANISER TOWER
+ CONDENSATE
DEHYDRATION
MODULE GLYCOL REGEN PACKAGE
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Compact onsite waste to energy technology
Up to 250kg/hr processing offers economic and environmental benefits
First continuous system to market
Uses Pyrolysis Technology
Meets WID requirement in Europe
Fully Patented
Proven in with Military
ST150 Small Scale W2E
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Feed Hopper
Cold End Feed
Pyro Chamber & Screw
Oxidiser & Start-
up burner
Gasifier
Hot Gas Outlet
Ash Drum
W2E Principle of Operation
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W2E Video
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Commissioned 2001
First in UK to pre-qualify for Renewable Obligation Certificate (ROCs) and awarded an Integrated Pollution Prevention and Control (IPPC)
Tested successfully on Municipal Solid Waste (MSW), Refuse Derived Fuel (RDF), tannery waste, abbatoir waste, tyres, car frag, sewerage and oil sludges.
Power produced, steam used for adjacent sterilisation plant as commercial improvement
Run commercially on clinical / pharma waste since 2001. Treated over 50K tonnes of clinical wastes.
Waste Incineration Directive (WID) compliant throughout operational history
Case Study Avonmouth (Bristol)
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HMS Ocean Testing, Operation and Upgading:
2 years of extensive testing was undertaken by Qinetiq and the MoD on a technical demonstrator in Portsmouth
Processed a wide range of waste streams from food waste to oil sludges
Very high availability throughout normal operation
Average 7% char residue
Queen Elizabeth Class Aircraft Carrier 4 off skid mounted ST150s for the UK Royal Navy
Destined for Queen Elizabeth Class Aircraft Carrier
1,000tpa mixed waste
Case Study UK Navy
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Waste Site- Leeds
Operating on real waste at accredited waste
facility
Completed comprehensive
processing of wide
range of wastes to
establish throughputs
and waste mixes
Completed 24/7 endurance running tests
Trained waste site operators in use
Improved design as consequence of tests
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ENQUIRY N: EXXXXXX
CUSTOMER: TBD
1 - FEED SYSTEM
THROUGHPUT (MAX PER ST150) 196 Kg/h
CALORIFIC VALUE (WET) 27 MJ/kg
MOISTURE (MAX) 15 %
MASS FRACTION C (APPROX) 45 %
MASS FRACTION H (APPROX) 15 %
2 - ASH COMPOSITION
VOLUME REDUCTION >90 %
TOTAL ORGANIC CONTENT (TOC)
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Waste properties paper plastic textiles wood food waste yard waste Carbon rich Hydrogen
CV (MJ/kg) 16 33 18.7 17 4 6 22 22
moisture (%) 8 2 10 15 70 50 0 0
mass fraction C % 45.4 60 46.2 48.3 41.7 49.2 99 0.1
mass fraction H2 % 6.1 8.3 6.5 6 5.8 5.8 0.1 99
The following assumes just C and H content of the waste
molar fraction C 0.55 0.55 0.54 0.57 0.55 0.59 0.99 0.00
molar fraction H (atomic) 0.45 0.45 0.46 0.43 0.45 0.41 0.01 1.00
Calculations
Combustion air input (kg/s) 0.1694 0.1694 0.1694 0.1694 0.1694 0.1694 0.1694 0.1694
Oxygen input (assume some excess O2 in exhaust) (kg/s) 0.0254 0.0254 0.0254 0.0254 0.0254 0.0254 0.0254 0.0254
moles of oxygen (kmols/s) 0.0016 0.0016 0.0016 0.0016 0.0016 0.0016 0.0016 0.0016
moles of oxygen per mole of fuel (-) 0.6652 0.6598 0.6567 0.6797 0.6588 0.6893 0.9955 0.2501
moles of fuel used (kmol/s) 0.0024 0.0024 0.0024 0.0023 0.0024 0.0023 0.0016 0.0064
moles of carbon used 0.0013 0.0013 0.0013 0.0013 0.0013 0.0013 0.0016 0.0000
moles of hydrogen used (atomic) 0.0011 0.0011 0.0011 0.0010 0.0011 0.0010 0.0000 0.0063
weight of carbon (kg/s) 0.0159 0.0158 0.0157 0.0161 0.0158 0.0162 0.0190 0.0000
weight of hydrogen (kg/s) 0.0011 0.0011 0.0011 0.0010 0.0011 0.0010 0.0000 0.0063
Energy from carbon (MW) 0.5188 0.5162 0.5147 0.5254 0.5157 0.5297 0.6224 0.0004
Energy from hydrogen (MW) 0.1279 0.1310 0.1329 0.1198 0.1316 0.1146 0.0012 0.7620
Total energy (MW) 0.6467 0.6473 0.6476 0.6452 0.6474 0.6443 0.6236 0.7624
Throughput of waste based on CV analysis (kg/s) 0.0404 0.0196 0.0346 0.0380 0.1618 0.1074 0.0283 0.0347
MAXIMUM Throughput of waste (kg/hr) 145.50 70.61 124.67 136.63 582.63 386.55 102.04 124.76
water flowrate (kg/s) 0.003 0.000 0.003 0.006 0.113 0.054 0 0
heat required for water (kW) 161.671 19.614 173.153 284.647 5664.442 2684.388 0 0
Assumed losses on system (kW) 200 201 202 203 204 205 206 206
Heat into ash assuming CP of 1 an dT of 800 (kW) 18.790 2.188 14.226 16.709 115.978 72.178 7.440 22.634
Net heat (kW) 266.22 424.45 258.21 140.84 -5337.05 -2317.31 410.11 533.77
Total weight of air, C and H (kg/s) 0.19 0.19 0.19 0.19 0.19 0.19 0.19 0.18
Temperature in oxidiser (C) 1448 2298 1406 775 -28626 -12399 2196 3056
Waste CV Values - Typical
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Space Including Access
Length = 12m
Width = 6.5mm
Height = 4.5mm
Weight = 20Te
Size and Weight