CCPilot100+ Test Results and Operating Experience - IEAGHG

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CCPilot100+ Test Results and Operating Experience Experience K Damen, F D Fitzgerald, R A Gardiner and S A Hume IEAGHG PCCC2 2 nd Post Combustion Capture Conference Bergen, Norway 17-20 September 2013

Transcript of CCPilot100+ Test Results and Operating Experience - IEAGHG

Page 1: CCPilot100+ Test Results and Operating Experience - IEAGHG

CCPilot100+ Test Results and Operating ExperienceExperience

K Damen, F D Fitzgerald, R A Gardiner and S A Hume

IEAGHG PCCC22nd Post Combustion Capture ConferenceBergen, Norway17-20 September 2013p

Page 2: CCPilot100+ Test Results and Operating Experience - IEAGHG

Contents

Doosan Power Systems Overview

Doosan Carbon Capture TechnologiesDoosan Carbon Capture Technologies

Test Facilities and Demonstration Projects

Ferrybridge CCPilot100+

Next Steps

Development Roadmap to Scaling-Up

Summary

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Our Products and Services

Doosan Power Systems

Doosan SkodaPowerDoosan Lentjes and Doosan Babcock

Boiler & Air

Doosan Skoda Waste to Energy

Boiler & Air Pollution Control Service TurbogeneratorsWaste to Energy

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Doosan Carbon Capture Technologies

25 years of experience in carbon capture

Oxyfuel

160KWt at Doosan ERTF

ERTF OxyfuelConversion

40MWt OxyCoalTM

Burner at Doosan CCTF

Full Power Plant Demo Expected100-250MW

Forecast to be fully commercialised by 2020

ERTF

1996 2009 20202012/1420081996 2009 20202012/142008

Post Combustion Capture (PCC)

University of R i

Boundary Dam PCC d t d t

Doosan invest into HTC Purenergy taking 15% &

l i

ERTF converted to PCC Test Facility

Antelope V ll FEED L S lRegina

development of PCC

donated to University for research

UoR’s ITC completed

exclusive rights to PCC technology

Valley FEED & Ferrybridge Demo

Large Scale Power Plantwith CCS

Commercial CCS Market

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2008 2009/10 2012/16 2016/20171987 20032000 2008 2009/10 2012/16 2016/20171987 20032000

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Test Facilities and Demonstration Projects

P f d d id f f l d diff l fi i

Facilities and technology create a winning edge

UoR’s Boundary Dam 4 t/dayITC 1 t/day

Performance demonstrated on wide range of fuels and different plant configurations

s of

dem

o

UoR s Boundary Dam, 4 t/day Commissioned in 1987 Dedicated to post-combustion

capture since 2000 Captures CO2 from flue gas

ITC, 1 t/day Opened in 2003 Flue gas from natural gas

combustion Includes equipment to

20+

year

s Captu es CO2 o ue gasemitted from lignite-fired boiler

Upgraded in 2007 to evaluate advanced process with RS-2

c udes equ p e t tostudy corrosion, material selection, solvent degradation and kinetics

le

ERTF, 1 t/day Commissioned in 2010 Ability to test wide range

f l d th f l

Ferrybridge, 100 t/day Largest post carbon capture

demonstration plant in the UK Long term testing and

dust

ry s

ca of coals and other fuels High degree of flexibility

and accuracy to test wide range of solvents and other modifications

Long-term testing and validation of process and solvent performance

Evaluate transient conditions and process control

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Extensive monitoring planned

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Ferrybridge CCPilot100+

PCC demonstration plant using DPS’ technology.

100 t/day slip stream from a 500MWeunit on SSE’s Ferrybridge Power Station, making it the largest PCC , g gdemonstration in the UK.

Two year test programme, fast-tracked build operating March 2012tracked build, operating March 2012.

Funded by all the project partners.

Lessons learned to be incorporated into future designs.

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CCPilot100+ Project Location

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Pictures courtesy Google Earth

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CCPilot100+ Test Programme Key Parameters

The test campaigns comprise a combination of parametric testing and exposure testing in order to;

– Assess the durability of the solvent,

– Permit process optimisation,Permit process optimisation,

– Provide data on plant design and scale-up.

Key Parameters

CO2 capture rate and product compositions. Steam consumption at reboiler. Amine and degradation product atmospheric emissions.

y

Absorber column efficiency.– Column CO2 composition and temperature profiling.

Power and water consumption under differing operating regimes. Optimisation of thermal integration. Solvent testing and formulation for efficiency and durability. Performance of construction materials including polymers. Comparison of performance with other pilot plant for scale-up.

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CCPilot100+ Test Measurements and Instrumentation

On site laboratory – off-line liquid analysis Solvent

Liquid Analysis

– Amine Concentration– Conductivity– Density– pHp– Heat Stable Salts (HSS) Concentration– Bound Amine

Water (Ion Chromatography)Cooling Water– Cooling Water

– Waste Water

Development of on-line liquid analysis Solvent

– Solvent Concentration – CO2 Loading

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CCPilot100+ Test Measurements and Instrumentation

Gas and solvent flow rates, temperatures and pressures.

Process Conditions and Gas Analysis

On-Line Gas Analysis– FT-IR – Extractive multi-point heated sampling system– Ammonia Tuneable Diode Laser – Cross-duct, non-extractive

O Mi F l C ll E t ti ld li– ppm Oxygen Micro-Fuel Cell – Extractive, cold sampling system

Manual Gas Analysis– FGD Polisher PerformanceFGD Polisher Performance– PCC Based Emissions

• Solvent Carryover• Degradation Products

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CCPilot100+ Current Status

Commissioned to run on MEA.

Plant handed over to SSE Operations Group March 22nd 2012.

1000+ hours of running time recorded with 30%w/w MEA with water. – Detailed analysis of results on-going.

900 hours of running time recorded to date on RS2TM. – Performance Optimisation and Solvent Degradation

Testing on-going.

UK Environment Agency and SSE interface– positive dialogue.– supportive of emissions measurement & control to pp

develop standards during the test programme.

100+t/day CO2 capture achieved at 90% capture efficiency.

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CCPilot100+ : MEA Baseline Results

MEA preliminary results show good agreement with publically available test datap y g g p y– typical quoted values of 3.6 to 3.9 GJ/t CO2

Solvent Regeneration Energy vs CO2 Capture Rate

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CCPilot100+ : RS2 Baseline Results

Preliminary results show a decrease in solvent regeneration energy when compared to MEA baseline performancePreliminary results show a decrease in solvent regeneration energy when compared to MEA baseline performance.

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NOT TO SCALE

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CCPilot100+ Operating Experience

Good working relationships developed with– SSE Ferrybridge Station and CCPilot100+ staff.– Environment Agency.– Main process plant item suppliers.– C&I equipment suppliers.– Analytical instrument suppliers.

Commissioning Commissioning– Development of analytical techniques.– On-line solvent analysis instrumentation.– Confirmation of plant operational envelope.

Testing and Operation– Selection of manual gas analysis contractor.– Liaison with Environment Agency.– Assessment of control system - cycling of plant through y y g p g

start-up, shut-down and other transient conditions.– Operation of plant at minimum turndown and increased

throughput for full BoP assessment.– Process monitoring - solvent behaviour and process

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optimisation.

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Next Steps

Complete RS-2™ testing Q4 2013Complete RS 2 testing Q4 2013

Process Modelling Validation– Development of modelling techniques for scale-up

Detailed Data AnalysisDetailed Data Analysis– Assessment of measurement accuracies– Assessment of BoP for scale-up

Advanced PCC materials testing– Corrosion resistant alloys, polymer resins and

anti-corrosion coatings.

Solvent Reclaimer Operation– Analysis of solvent degradation productsAnalysis of solvent degradation products

On-line liquid and gas analysis throughout test programme.

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Knowledge Transfer

Commitment to maximising the scientific benefit of the CCPilot100+ project

Knowledge Dissemination and Information Sharing - ONGOING

Complementary R&D Projects at partner Universities ONGOING

Commitment to maximising the scientific benefit of the CCPilot100+ project

Complementary R&D Projects at partner Universities - ONGOING

– Use of operational results to support areas of CCS related research.

Continuing Professional Development - COMPLETED

– Day visits.

– Industrial Awareness Module.

– CCPilot100+ one month site secondments.CCPilot100 one month site secondments.

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Commercialisation

DPS Development Roadmap to Scaling-Up

Large demonstration

Commercialisationfull scale plant

10,000 t/day CO2 ≈ 500MWe

15,000 t/day CO2 ≈ 800MWe

Slipstream100 t/d CO 5MW

project(s) slipstream

~3000 t/day CO2 ≈ 150MWe

15,000 t/day CO2 800MWe

Emissions reduction test facilities

100 t/day CO2 ≈ 5MWeFerrybridge

1 t/day to 4 t/day CO2

Where we are now

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In Summary

Successful achievement of 100+ t/day of CO2 captured at 90% efficiency.

Solvent regeneration energy for 30%w/w MEA in agreement with literature values.

RS2TM performance and solvent degradation testing on-going.

Provision of invaluable knowledge for incorporation into the full commercial deployment of PCC technology.

Development of robust procedures, operating guarantees and p p , p g gcompetitive performance.

Improving the technology offering through capital and operational cost reduction.

Working closely with utilities and environmental agencies to develop measurement and control standards to further bolster confidence in post-combustion capture.

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Contact Details

Rebecca GardinerSenior Engineer Product DevelopmentE [email protected]

Doosan Power Systems LimitedPorterfield Road

Dr David FitzgeraldPrincipal Engineer Product DevelopmentE [email protected]

Porterfield RoadRenfrewPA4 8DJUnited Kingdom

Mark BryantDirector Carbon CaptureE [email protected]

T +44 (0)141 886 4141

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Thank youThank youThank youDisclaimer:The contents in this presentation are for information purposes only

Thank you

and are not intended to be used or relied upon by the reader and are provided on the condition that you 'use it at your own risk'. Doosan Power Systems Limited does not accept any responsibility for any consequences of the use of such information.

All rights are reserved and you may not disseminate, quote or copy this presentation—written by Doosan Power Systems Limited—without its written consent.its written consent.