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2006 年石炭技術会議
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【 特 別 講 演 Ⅰ 】 An Update of International CO2 Capture and Storage Initiatives
Dr. Kelly Thambimuthu
Chairman, IEA Greenhouse Gas R&D Programme and Chief Executive Officer, Center for Low Emission Technology
www.ieagreen.org.uk
Overview of the PresentationOverview of the Presentation
• The options in a carbon constrained world• What are CO2 capture and storage (CCS) technologies• Maturity of CCS technologies and power generation• Existing commercial-scale activity• Near-term opportunities• Proposed demonstrations• International clean coal roadmaps• Conclusions
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An Update of International An Update of International COCO22 Capture & Storage (CCS) InitiativesCapture & Storage (CCS) Initiatives
Presented at: J Coal Clean Coal Conference27th November, 2006, Tokyo, Japan
byDr. Kelly Thambimuthu,
ChairmanIEA Greenhouse Gas R&D Programme
andChief Executive Officer,
Centre for Low Emission Technology (cLET), Australia
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Fuels
Processes
Storage options
What is COWhat is CO22 capture & storage (CCS)capture & storage (CCS)
Source IPCC 2005
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Carbon Neutral Energy
Fossil Fuels
H2 Economy (?),De-carbonised electricity (?)
CO2 capture& storage
Nuclear fission& Fusion ?
Conservation, efficiencyand lower carbon fuels
Renewables
2004 to 2030 >53% increase; ~82% fossil fuel, ~12% renewables, ~6% nuclear
The options in a carbon constrained worldThe options in a carbon constrained world
Source cLET, Brisbane
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• Research phase means that the basic science is understood, but the technology is currently in the stage of conceptual design or testing at the laboratory or bench scale, and has not been demonstrated in a pilot plant.
• Demonstration phase means that the technology has been built and operated at the scale of a pilot plant, but further development is required before the technology is ready for the design and construction of a full-scale system.
• Economically feasible under specific conditions means that the technology is well understood and used in selected commercial applications, such as in case of a favourable tax regime or a niche market, processing at least 0.1 MtCO2/yr , with few (less than 5) replications of the technology.
• Mature market means that the technology is now in operation with multiple replications of the commercial-scale technology worldwide.
Source IPCC 2005
Maturity of CCS technologyMaturity of CCS technology
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The pathway for COThe pathway for CO22 capture & storage (CCS)capture & storage (CCS)
Fossil fuelsCO2 capture
UtilisationStorage
•Spent oil/gas fields•Saline reservoirs•Ocean
“Greener”Fossil Fuels(Enhanced oil andcoal seam methane recovery) SINK
SOURCE
Energy, Electricity or H2(with zeroing emissions)
•Chemicals•Fuel synthesis
Non fossilenergy
Source cLET, Brisbane
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Coal post combustion captureCoal post combustion capture
StorageCO2Separation
N2, H2O to atmosphere
CO2
Coalcombustion
Flue gases
PowerGeneration
Compression
• Conventional power plant
Other pollutants captured
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Technology maturity of CCS componentsTechnology maturity of CCS components
Research phase
Demonstrationphase
Economicallyfeasible under
specificconditions
Maturemarket
Ocean storage
Mineralcarbonation
Industrialutilization
Enhanced CoalBed Methane
Saline formations
Gas and oilfields
Enhanced OilRecovery
Transport
Post-combustion
Pre-combustion
Oxyfuelcombustion
Industrialseparation
Source IPCC 2005
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Coal Coal –– precombustionprecombustion capturecapture•Coal-fired power plant (IGCC)
CO2Separation
H2
CO2GasifierCoal
Shift Reactor
Compress/Storage
GTCC
Air SeparationUnit
O2 N2
Other pollutants captured
N2, H2O to atmosphere
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CoalCoal--oxyfueloxyfuel combustion combustion • Modified conventional plant
CO2 / H2O
Compress/Storage
CO2
Air SeparationUnit
O2
SeparationFossil fuelcombustion
PowerGeneration
Other pollutants removed
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Cost of CCS for electricity and hydrogen production Cost of CCS for electricity and hydrogen production
(-14)-49(-7)-319-4419-68Cost of CO2 avoided with EOR US$/t
5.2-12.940-7549-8137-70Cost of electricity or hydrogen with capture and EOR US$/MWhor US$/GJ
3-7514-5330-7138-91Cost of CO2 avoided with geosequestration, US$/t
7.6-14.455-9163-9943-77Cost of electricity or H2 with capture and geosequestrationUS$/MWh or US$/GJ
Hydrogen Plant
IGCCPulverisedcoal
Natural gas CC
Costs with geosequestration with and without enhanced oil recoverySource IPCC 2005
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Technology maturity Technology maturity -- capture in coal plantscapture in coal plants• Power generation with post combustion capture
• SC/USC pulverised coal power plants are reliable and proven• Scale up of solvent capture units/integration with power cycle is unproven.
• Power generation with pre-combustion capture• IGCC for coal (1 GWe) is near commercial and proving reliability, better
experience with 3 GWe of IGCC capacity on oil and petcoke. • Solvent capture units for CO2 available at scale, integration and power block
hydrogen utilisation issues
• Power generation with oxyfuel combustion• No proven experience of operation of pulverised coal power plants in an
oxyfuel combustion mode – the issue is “confidence building”• Large scale ASU’s for O2 production proven and reliable.• Some development issues with tail end CO2 purification
In need of demonstrations to support ‘learning by doing’ which can reduce costs by at least 20- 30% or more over the next decade
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Path to improved pulverised coal2015 on
S/C PCC~45%
Hg activities:characterisation
monitoringremoval methods
First commercial PCC-ZETsretrofits and new~36 - 37 %LHV
Advanced PCC based ZETs~44- 47 %LHV
Beyond 2020;USC >700C and 30MPa With higher efficiency?
Now 2005-10 2010-15Increasing efficiency, lower emissions, lower costs
SO2 activities:deeper removal
new systems
NOx activities:deeper removal
without SCR
Particulates removalmove to <10 mg/m3
CO2 capture activities:chemical scrubbing demo
CO2 capture activities:oxy-coal demo
Advanced USC PCC demonon-CO2 capture
Advanced USC PCC commercialnon-CO2 capture
New oxygen productionplants commercial
oxy-coal demo
Post combustion membrane
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The options for coal power plants with CCSThe options for coal power plants with CCSCentralised power and
industrial plantsDistributed energy & products
Heating or cooling
Coal Gasification
Distributed heat & power
Transport vehicles
Power Generation
Hydrogen
Electricity
CO2 to storage
CO2capture
Liquid Fuels
Chemicals
Chemical products
Industrial products
Combustion
Biomass for carbon offset
Source cLET, Brisbane
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Existing CCS CommercialExisting CCS Commercial--scale Projectsscale Projects
• There are 3 CCS projects operating at a commercial scale:• Sleipner, Norway• Weyburn, Canada• In Salah, Algeria
• Each project captures and stores approximately 1 million tonnes CO2/year
• This total of 3 million tonnes CO2/year is roughly equivalent to emissions from one 500MWe coal-fired power plant.
*‘Commercial’ as opposed to non-commercial demonstrations
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Path to improved coal-fired, IGCC2015 on
IGCCcommercial
scaledemos
~38-44 %LHV
Now 2005-10 2010-15Increasing efficiency, lower emissions, lower costs
Early full scale IGCC with CO2 capture
~32-35 %LHV
Advanced IGCClow emission plantsvarious technologies
multi-products~42 - 44 %LHV
Beyond 2020;stationary fuel cells
(IGFC)50 – 58 %LHV?
NOx activities:reduce emissions
CO2 capture activities:physical scrubbing demo
CO2 capture activities:Gas separation & reactor
membranesNew Oxygen production
plants commercial
Dry cleaning options:Particulates, Sulphur,
Nitrogen, trace elements
Commercial non-CO2Capture IGCC plants
HydrogenTurbines
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SnøhvitSleipner
Weyburn
In-Salah
CommercialCommercial--scale CCS Projectsscale CCS Projects
Images Courtesy of BP, Statoil, and PTRC THESE ARE NOT POWER GENERATION PROJECTS
START-UP 2007
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MonitoredMonitored COCO22 Stored UndergroundStored Underground
0
5
10
15
20
25
30
35
40
1995 1996 1997 1998 1999 2000 2001 2002 2003 2004 2005 2006 2007 2008 2009 2010
Year
Mill
ions
of t
onne
s of
CO
2
Sleipner (1996)
Weyburn (2000)
In Salah (2005)One 500MW coal-fired power station
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LowLow--cost COcost CO22 sourcessources
• Where it is removed from raw natural gas to meet pipeline specifications or for LNG production
• Synthesis gas clean-up e.g. in hydrogen production.
• Natural occurrences e.g. in Texas
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NearNear--term CCS Opportunities:term CCS Opportunities:• Are integrated with an existing infrastructure/project
• Have a convenient store for CO2
• The cost of CO2 is considerably less than the cost of capturing it at a power station
• Have some near term revenue benefit e.g. EOR
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Gorgon LNG plant with COGorgon LNG plant with CO22 capturecapture
Courtesy of Chevron
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Some proposed commercialSome proposed commercial--scale CCS projectsscale CCS projects
• Snøhvit (start-up 2007), Norway• Gorgon (operation start 2008-2010), Australia• Miller-Peterhead –DF1 (operation start 2009), UK• Carson - DF2 (operation start 2009), USA• Halten (operation start 2010), Norway
Total CO2 to be stored by the above: 12.5 million tonnes CO2 / year
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Key considerations for nearKey considerations for near--term CCS projectsterm CCS projects
• Applicable state/national/international incentives• Carbon taxes / emissions trading• 2 CCS projects have been submitted under the
Kyoto CDM (Clean Development Mechanism)• Revenues applicable to incremental oil/gas• Risk sharing• Finance sourcing/cost• Long-term liability issues
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Schematic of the Shell/Statoil Schematic of the Shell/Statoil –– HaltenHalten projectproject
Courtesy Shell-Statoil
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COCO22 Injection and Storage ActivitiesInjection and Storage Activities
Nagaoka
HokkaidoQinshui Basin
Snohvit
Sleipner
In Salah
KeyECBM projects
EOR projects
Gas production Fields
Saline aquifier
SibillaRECOPOLCO2 SINK
K-12B
Cerro Fortunoso
Frio
West Pearl QueenMountaineer
WeyburnPenn West
Alberta ECBM
Teapot DomeRangely
Burlington
4 New CO2-EOR Pilots in Canada
50 Acid Gas injection sites in North America
70 CO2-EOR projects in U.S.A.
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Power plant capture scalePower plant capture scale--up route & activitiesup route & activities
• Bench scale (simulated flue gas)• Post combustion pilots (on flue gas slip-stream)
• EU Castor – 25 tCO2/d, Denmark• MHI -10 tCO2/d, Nagasaki, Japan• ITC – 8 tCO2/d, Boundary Dam, 8 tpd
• Oxyfuel• Vatenfal, 30 MWth, lignite, Germany,
• Large demonstration – with integrated operation
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COCO22 capture facilitiescapture facilities
Mitsubishi Plant, Nagasaki
Sumitomo Chemicals
Indo Gulf Fertilizer Co.
Luzhou Natural Gas
Vattenfall
CASTOR
Snohvit
Sleipner
In Salah
Shady Point
Bellingham CogenDakota Gasification PlantBoundary Dam
IMC Global Inc.
Key
Warrior Run
Gasification synfuels plant
Major Pilot Plants
CO2 Separation from Natural Gas for CCS
Food-grade CO2/carbonation of brine/Urea (Post Combustion)
Mitsubishi, Malaysia
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Examples of Examples of proposedproposed CCS projects CCS projects withwith power generation: power generation: CoalCoal• RWE project, Germany
• 450 MW coal IGCC, pre-combustion capture• Saline reservoir storage of CO2, Start-up 2014
• Future Gen project, USA• 275 MW coal IGCC, pre-combustion capture• Saline reservoir storage of CO2, Start-up 2014
• HypoGen / Dynamis project, EU• Coal IGCC, pre-combustion capture, Proposed 2012
• Stanwell Zerogen, Australia• 100 MW Coal, IGCC, precombustion, Proposed 2010
• Sask Power project, Canada• 450 MW Lignite, EOR, oxyfuel, Start-up 2012
• RWE project, UK (Tilbury) – oxyfuel or post-combustion• International Power, Victoria, Australia
• Brown coal, 200MW (1.6 GW station) – post-combustion
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Proposed integrated CCS power projectsProposed integrated CCS power projects
Key
Pre-Combustion Capture
IGCC
Oxy-Fuel
Post-Combustion
DF1
DF2
HALTEN
RWERWESaskPower
FutureGen HypoGen
CentricaB.oN
Mongstrad
Gorgon Stanwell
Hazelwood
CallideLNG
CHNG
E.ON
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USA coal roadmap development principleUSA coal roadmap development principle• Short-term: keep existing fleet in service;
prepare for transition to near-zero-emission future
• SO2, NOx, Hg• Plant optimization and control• Reduced carbon intensity
• Long-term: add near-zero emission energy plants
• IGCCs to market • Advanced materials• Ultra-high efficiency hybrid systems• CO2 capture and storage
Rev. 071404
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2050
2020
2015
Pote
ntial
of U
tilisa
tion
on T
ime S
cale
2010
2005
Risk of R&Dhighlow medium
Vision
Steam PP η=50%Gas PP η>60%
Steam PP η=55%Gas pp η=65%
Hybrid-Power Plant
Zero-Emission
Power Plant
Capture with
Membranes
Oxyfuel-Demo
IGCCDemo
CO2-Wash
CO2-Reservoirs
CO2/H2-TurbineMaterials
Materials 700°C
Procedures ProtectionSystems
Materials800°C
Min. Leaks
Strategielinie: Effizienz Strategielinie:CO2-Capture/ Storage
2050
2020
2015
Pote
ntial
of U
tilisa
tion
on T
ime S
cale
2010
2005
Risk of R&Dhighlow medium
Vision
Steam PP η=50%Gas PP η>60%
Steam PP η=55%Gas pp η=65%
Hybrid-Power Plant
Zero-Emission
Power Plant
Capture with
Membranes
Oxyfuel-Demo
IGCCDemo
CO2-Wash
CO2-Reservoirs
CO2/H2-TurbineMaterials
Materials 700°C
Procedures ProtectionSystems
Materials800°C
Min. Leaks
Strategielinie: Effizienz Strategielinie:CO2-Capture/ Storage
German: COORETEC programmeGerman: COORETEC programme
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Australia Australia –– Coal 21 action planCoal 21 action plan
Pilot Implement
Demo Commercial
Pilot Demo
PilotEval Demo Commercial
Pilot Demo Commercial
2000 2005 2010 2015 2020 2025 2030
Lignite Drying
Black & Brown Coal IGCC with
CO2 Capture
Geological Storage of CO2
OxyfuelCombustion
Ultra-Clean Coal
Demo Commercial
Pilot Implement
Demo Commercial
Pilot Demo
PilotEval Demo Commercial
Pilot Demo Commercial
2000 2005 2010 2015 2020 2025 2030
Lignite Drying
Black & Brown Coal IGCC with
CO2 Capture
Geological Storage of CO2
OxyfuelCombustion
Ultra-Clean Coal
Demo Commercial
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ConclusionsConclusions
• CCS firmly on worldwide policy agenda• Demonstrations needed but costly• Significant CCS activity:
• Oil & Gas industry – driven by ‘near-term opportunities’
• Coal industry – driven by ‘clean coal’ visions• In need of incentives for deployment in the
electricity generation sector
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CarbonReduction
Time
`IncreasedEfficiency`Trajectory
`Zero Emissions`Trajectory
Near-term Mid-term Long-term
Zero emissions will need the most efficient plant
Key issue will be value of CO2
UK: CAT* roadmapUK: CAT* roadmap
*Carbon Abatement Technologies
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IEA GHG thanks you for your attentionIEA GHG thanks you for your attention
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氏 名 :Kelly Thambimuthu Chairman, IEA Greenhouse Gas R&D Programme 兼 Chief Executive Officer, Centre for Low Emission Technology 職 歴 1995- 化石燃料を起源とする温室効果ガス排出の大幅な削減を達成す
るための様々なオプションを評価しているIEA/OECDの主要グループ/
IEA Greenhouse Gas R&D Programme の議長 2004- 豪州ブリスベンCSIRO先進技術クイーンズランドセンター
(QCAT)に本拠を持つCenter for Low Emission Technologyのセンター
長。本センターはクイーンズランド州政府、CSIRO、ACARP、Stanwell、Tarong Energy及びクイーンズランド大学のジョイントベンチャー。
1982-2004 カナダCANMET Energy Technology Centerにおける研究者及び科学技
術管理者 2002-2005 気候変動緩和策として二酸化炭素回収・貯留に関するIPCC特別報告書に
おいて気候変動に関する政府間パネル(IPCC)委員会の編集委員及び主
執筆者 2004年 英国王立研究所で「Coal Science Lecture」を実施 2006年 持続的な石炭開発に関する賞である IEA Coal Industry
Advisory Board’s awardを受賞 学 歴 英国バーミンガム大学 学士号(化学工学) カナダマックギル大学 修士号(化学工学) 英国ケンブリッジ大学 博士号(化学工学)