dps group overview

DPS Overview

DPS Group

Overview

Process system integrators

Multi-disciplined engineering team

Innovative technical solutions

Project execution excellence

Recent clients include:

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

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

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

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

Typical Que$tor Output

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

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

Plus lots of other acronyms

Other Deepwater Platform Options

Control Buoy Subsea to Shore (subsea processing) Ormen Lange

+ Subsea to Platform

Compliant Towers

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

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

Lightweight

Jacket

Steel Braced

Monotower

Conductor

Supported

Self-Installed

Platform

Light Weight Structure Options

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:


4-Leg Jacket

4 wells

Test Separator

Production/Test/Gas lift Manifold

WP-2:


4-Leg Jacket

2 wells

Test Separator

Production/Test/Gas lift Manifold

Utilities

Temporary Shelter

Basic / FEED Case Study

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.

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PROJECT MANAGEMENT/ ENGINEERING

TOPSIDES MODULES

100,000 bpd

FEED Case Study

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

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

Project: Cendor Phase II FEED

Location: Offshore Terengganu

Client: Petrofac (Malaysia PM304) Limited

1. Wellhead Platform 1 (WHP-1)-Max Production: 40,000BLPD



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

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

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)

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

FPSO before upgrade FPSO after upgrade

Berantai FPSO upgrade

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

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TOPSIDES MODULES

80,000 bpd 16 mmscfd


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

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

Interface Engineering

FEED

Detail

Delivery

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


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

everything in pink is a change

OSX-1 FPSO

Significant Upgrade Project

OSX-1 FPSO

PDMS modelling through to completion

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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TOPSIDES MODULES



CRUDE STABILISATION

FLARE KNOCK OUT

FLARE KNOCK OUT MODULE

WATER INJECTION

CRUDE

STABILISATION &

PRODUCED WATER

TREATMENT

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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TOPSIDES MODULES


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: 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

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TOPSIDES MODULES



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

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TOPSIDES MODULES

2007 East

Fortune 30,000 bpd 35 mmscfd


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



BW. Carmen Upgrade

Ithaca Athena

North Sea


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


Detail Design of Wellhead Platform for

Newfield West Belumut Field

Jacket Engineering

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

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

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

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

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

DPS Group

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)

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

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

Extensive Testing of Solids Evacuation Valves in DPS Test Rig.

Solids Evacuation from HydroLoc

HydroLoc

30GPM unit on test in

our R&D facility in Utah

30GPM unit on shale

gas project in Colorado

Results on Frac Water Flow Back

HydroLoc Extensive Performance Trials

5gpm HydroLoc on

Performance Trials in

DPS UK Flow Loop

Typical HydroLoc P&ID

Interface Level Control

In the Hydroloc

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)

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

Cyclone Design

Well Fluids

Gas

Oil

Water

Where do we Manage Solids in Process?

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

Upstream of Production Separator

Well Fluids

Gas

Oil

Water

Solids

Prevent solids entering production separator

Solids actively removed

Multi phase cyclone design

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

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

Cleaning Solids Offshore?

Clean Solids Discharge

Solids from Production

Clean Produced Water

Oily Water

Solids

Accumulation

Vessel Jet Pump

Cleaning

Cyclone

CyFlo

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

Solids Management Technology

Options

DPS provides a total solids

management solution

Offline Sand Removal

Online Sand Removal

Atmospheric Transfer

Solids Cleaning

Deoiling Hydrocyclones - Evolution

High Flow

Low Differential Pressure

Combined Desanding and

Deoiling

The Right Hydrocyclone for the

Right Duty

Combined Desander and HFD

Inlet

Water Outlet Solids Outlet

Oily Reject

Desanders HFD

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

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

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

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

Gas

Oil

HFD + Degassing Self Cleaning Filter

Recycle

Water

Media

Cleaning

DSCF

Productio

n

Separator

HFD

Hydrocyclon

e

Gas

Electrostatic Coalescers

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

Specialist Packages Knarr FPSO

DEBUTANISER TOWER

+ CONDENSATE

DEHYDRATION

MODULE GLYCOL REGEN PACKAGE

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

Feed Hopper

Cold End Feed

Pyro Chamber & Screw

Oxidiser & Start-

up burner

Gasifier

Hot Gas Outlet

Ash Drum

W2E Principle of Operation

W2E Video

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)

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

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

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)

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

Space Including Access

Length = 12m

Width = 6.5mm

Height = 4.5mm

Weight = 20Te

Size and Weight

dps group overview

Documents

art review activity

maximum topsides field

minimum topsides option

medium topsides option

art review que

te field

project management activity

hydraulic modelling