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Resent Activities of CCTResent Activities of CCT · 2014. 4. 25. · Shift CO2 Capture Technology...

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Resent Activities of CCT Resent Activities of CCT 23th April, 2013 at Edinburgh University Dr. Yasuhiro Yamauchi Environment Department Contents 1. About NEDO 2.1 Importance of Clean Coal Technology 2.2 NEDO’s CCT Development Strategy 3. Improvement of Coal-fired Power Generation Efficiency 4. Dissemination of High-efficiency CCT 5. Feasibility Study on CCS in Japan
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Page 1: Resent Activities of CCTResent Activities of CCT · 2014. 4. 25. · Shift CO2 Capture Technology IGCC Gas clean-up facilities CO2 Capture Technology o n CO Steam Ai Coal Air reactor

Resent Activities of CCTResent Activities of CCT 23th April, 2013 at Edinburgh University

Dr. Yasuhiro Yamauchi

Environment Department

Contents

1. About NEDO

2.1 Importance of Clean Coal Technology2.2 NEDO’s CCT Development Strategyp gy

3. Improvement of Coal-fired Power Generation Efficiency

4. Dissemination of High-efficiency CCT

5. Feasibility Study on CCS in Japan

Page 2: Resent Activities of CCTResent Activities of CCT · 2014. 4. 25. · Shift CO2 Capture Technology IGCC Gas clean-up facilities CO2 Capture Technology o n CO Steam Ai Coal Air reactor

– NEDO, an incorporated administrative agency under METI, promotes R&D as well as the dissemination of industrial, energy and environmental technologies.

Japanese Government, Ministry of Economy, Trade and Industry (METI)

Coordination withpolicymaking authorities

Budget

NEDO Budget: Approx. USD$ 1.3 billion Number of personnel: Approx. 900

I d tA d iPublic research

Finance

IndustryAcademia laboratories

Global primary energy demand by Global power generation by p y gy ysource

p g ysource

18000

20000

9000

10000

Mto

e

Mto

e

12000

14000

16000 Other renewables

Bio energy

Hydro6000

7000

8000

6000

8000

10000Hydro

Nuclear

Gas 3000

4000

5000

0

2000

4000 Oil

Coal

0

1000

2000

27% 25% 46% 38%

Source: World Energy Outlook 2002, 2004, 2007–2012

Page 3: Resent Activities of CCTResent Activities of CCT · 2014. 4. 25. · Shift CO2 Capture Technology IGCC Gas clean-up facilities CO2 Capture Technology o n CO Steam Ai Coal Air reactor

1.2

10%

1.1 trillion kWhApprox 1 trillion kWh

‘Setsuden’ refers to Japan’s energy conservation movement

110%

35%

Renewable energyOil

Approx. 1 trillion kWh

0 6

0.8

63%

35%

Fossil fuels

LNG

Oil

0.4

0.6

65%

Coal

LNG

0.2

65%

Nuclear

Coal

0

2010 2030

Coal

Source: Options for Energy and the Environment (outline) (The Energy and Environment Council Decision on June 29, 2012) July 2012 National Policy Unit

• New Energy Policy will be established based on the coalition government formed between the Liberal Democratic Party (LDP) andgovernment formed between the Liberal Democratic Party (LDP) and Komeito Party.

• The Japanese government will take all possible measures to stabilize energy supply and demand to meet the needs of its citizens and prevent any interruptions in economic activities. In this respect, it will establish a “Responsible Energy Policy.”

• Japan’s “Zero-nuclear Energy Policy”—aimed at halting the operations of all nuclear power plants by the 2030s and established by the previous administration—needs to be reviewed The LDP’s manifestoprevious administration—needs to be reviewed. The LDP s manifesto during the House of Representatives election in December 2012 states that it will establish a sustainable long-term best energy mix within ten yearsyears.

• Japan will establish a responsible energy policy in accordance with these principles.

Source: Japan’s Coal Policy, March 26,2013, Coal Division, Natural Resources and Fuel Department, ANRE,METI

Page 4: Resent Activities of CCTResent Activities of CCT · 2014. 4. 25. · Shift CO2 Capture Technology IGCC Gas clean-up facilities CO2 Capture Technology o n CO Steam Ai Coal Air reactor

1.Technology for Sustainable Use of Coal

State-of-the-art gasification technology accelerates the establishment of coal-based low carbon societies “Smart Coal”

Hydrogen energy

H2 (chemical materials fuel cell hydrogen

FertilizerIGFCHydrogen energy

supply chain

Electricity

EAGLE project H2 (chemical materials, fuel cell, hydrogen fuel)

G f lHydrogen production

Synthetic gasReduction FT synthesis, etc.Clean fuel

Gas fuel-Substitute natural

gas (SNG)

Steel

CO+H₂

イメージを表示できません。メモリ不足のためにイメージを開くことができないか、イメージが破損している可能性があります。コンピュータを再起動して再度ファイルを開いてください。それでも赤い x が表示される場合は、イメージを削除して挿入してください。 Liquid fuel

Reduced iron

Gasification

Clean fuel-DME,

-Gasoline,-Diesel oil, etc.

イメージを表示できません。メモリ不足のためにイメージを開くことができないか、イメージが破損している可能性があります。コンピュータを再起動して再度ファイルを開いてください。それでも赤い x が表示される場合は、イメージを削除して挿入してください。

Upgrading,drying

n

CCS – (EOR)CO2

Coal Brown coal, low rank coalBiomass OilOxyfuel Workshop on Dec. 4th, 2012 at NETL Pittsburgh

NEDO h l d h i th d l t f IGCC d IGFC hi hNEDO has placed an emphasis on the development of IGCC and IGFC which utilize gasification as a core technology in order to improve power generation efficiency,

・ Integrated Coal Gasification Combined Cycle (IGCC)・ Integrated Coal Gasification Fuel Cell Combined Cycle (IGFC)・ Advanced Ultra-super Critical Steam Condition (A-USC)

Page 5: Resent Activities of CCTResent Activities of CCT · 2014. 4. 25. · Shift CO2 Capture Technology IGCC Gas clean-up facilities CO2 Capture Technology o n CO Steam Ai Coal Air reactor

Coal Energy Application for Gas, Liquid & Electricity(EAGLE)

G ifi

Photograph of EAGLE Pilot Plant (150 tons/day)Photograph of EAGLE Pilot Plant (150 tons/day)

Gasifier(1 0 /d )

Air separation facilities

Gas purifier (150 tons/day)

facilitiesIncinerator

Sulfur recoveryfacilitiesCO2 separation facilities

(Chemical Absorption

NN

Gas turbine house (8 MW)

(Chemical Absorption technology)

■Stage 1 (2002 - 2006) Oxygen-blown entrained-flow gasifier was developed.■Stage 1 (2002 2006) Oxygen blown entrained flow gasifier was developed.Gas cleanup technology was established.

■Stage 2 (2007 - 2009) CO2 capture technology (chemical absorption) was developed. Coal type diversification (high ash fusion temperature coal) was carried out. Trace elements behavior was investigated.

■Stage 3 (2010 - 2013) Development of CO2 capture technology (physical absorption)Survey of innovative CO2 capture technology

EAGLE Stage 3: Survey of innovation CO2 capture technology

- Development of CO2 capture technology (physical absorption) -

A survey on innovative CO2 capture technology is being carried out in order to develop optimal CCS technology to be used in combination with higher pressure systems in next generation IGCC The EAGLE pilot plant is being utilized to conduct an oxygen blowngeneration IGCC. The EAGLE pilot plant is being utilized to conduct an oxygen-blown entrained-flow gasifier, CCS test using mainly physical absorption technology.

GasifierCO₂

absorberShift

Reactor→①→

(Desulfurizer)

→②→

(Desulfurizer)

→Gasturbine

CO2 separation facilities (physical absorption,

newly installed)

CO2 separation facilities (chemical absorption)

CO Shift R t

CO₂Ab b

( ) ( )

Reactor Absorber

Sour shift(location of

Desulfurizer: ②)

Physical absorption

Stage 3Currently

testingDesulfurizer: ②)

Sweet shift(location of

Desulfurizer: ①)

Chemical absorption

testing

Stage 2Reference test

Desulfurizer: ①)

Page 6: Resent Activities of CCTResent Activities of CCT · 2014. 4. 25. · Shift CO2 Capture Technology IGCC Gas clean-up facilities CO2 Capture Technology o n CO Steam Ai Coal Air reactor

EAGLE Stage 3: Survey of innovation CO2 capture technology

- Results of EAGLE Pilot Plant -

Gasifier Syngas Cooler

Fine DesulfurizerCoal Gasification

Cold Gas Cleanup

Coal

y g

Char Filter

MDEAStripper Limestone

Scrubber

N2 N2

CharSlag

Waste Heat

WaterScrubber

MDEAAbsorber

GGHGypsum

WaterScrubber

PhysicalCO2 Capture

Ch i l

SourShift

Sweet

(Under Construction)

O2

GComp GT

HRSG

Air

Air FeedCompressor

RectifyingC l

Air

Incinerator

Recovery BoilerChemicalCO2 Capture

SweetShift

G

(not installed)

ST

Compressor Column

Gas TurbineAir Separation UnitStack

Ref: H. Suzuki, The Clearwater Clean Coal Conference, Florida U.A., 2012 06 05

EAGLE Stage 3: Survey of innovation CO2 capture technology

- Results of Chemical absorption Development -

Steam

Coal

N2

COH2

Sweet Shift Reactors

CO2 Capture (Steam Regen.)

H2 Rich Gas CO2

N2

O2 CO2

H2

Absorber Stripper

Reboiler

CO + H2O ⇒ CO2 + H2 + 41kJ/mol

3

CO2 Capture (Heated Flash Regen.)

H2 Rich Gas CO2

Syngas Feed Rate: 1,000 Nm3/h

CO2 Recovery Rate: 24 t/d

Flash DrumAbsorber

Basic data on solvent regeneration energy of the heated flash mode-under condition of more then 80%Case#

1Steam

Regeneration

2Steam

Regeneration

3Heated FlashRegeneration

4Heated Flash mode(Actual) under condition of more then 80%

CO2 recovery rate, 1.0~1.3GJ/t-CO2 were obtained as the parametric testing results.

They indicated that energy

Regeneration(Base Case)

Regeneration(Improved)

Regeneration mode(Actual)

Solvent Circulation Ratio (L/G) 6.8kg/kg 6.7kg/kg 12.5kg/kg

Reboiler Steam Ratio (G/L) 140kg/m3 90kg/m3 -

Flash Drum Temperature - - 75℃ 67℃

consumption is improved by 10-30% when compared with last year’s results.

Heat Required for Regeneration

2.99GJ/t-CO2 1.93GJ/t-CO2 1.39GJ/t-CO2 1.0-1.3GJ/t-CO2

CO2 Recovery Ratio 91.8% 91.4% 85.3% >80%28% cut 23% cut

Page 7: Resent Activities of CCTResent Activities of CCT · 2014. 4. 25. · Shift CO2 Capture Technology IGCC Gas clean-up facilities CO2 Capture Technology o n CO Steam Ai Coal Air reactor

EAGLE Stage 3: Survey of innovation CO2 capture technology

- Results of F.S. of Actual Chemical absorption System -

Dry Low-NOx Gas Turbine Combustor for IGCC (Demonstrated at EAGLE)

Page 8: Resent Activities of CCTResent Activities of CCT · 2014. 4. 25. · Shift CO2 Capture Technology IGCC Gas clean-up facilities CO2 Capture Technology o n CO Steam Ai Coal Air reactor

Shift CO2 Capture Technology

CO2 Capture TechnologyIGCC Gas clean-up facilities

on CO

SteamAi

CoalAir

reactorTechnology

CO2, H2

Gas

ific

atio

Syngas (CO, H2)CO2

SteamAir

separation unit

Oxygen Gas AirGasifier

G

Combustor

H2 rich gas

Oxygen

Steamturbine

turbine Generator

Stack

Fuel Cell

H2

Compressor

HRSG (heat recovery steam generator)

Fuel cell

To CO₂ transportation・Construction period: 2012–2016

Osaki CoolGen ProjectLocation: Osaki, Hiroshima; Capacity: 167 MW

and storage processes(out of scope for OsakiProject)

・First stage: IGCC verification tests will start from March 2017・Second stage: Demonstration of CO₂ capture technology・Third stage: Demonstration of IGFC with CO₂ capture technology

Oosaki Cool Gen (OCG) Project

gRendering of OCG facilities

Coal Gasification

Now constriction is started

Page 9: Resent Activities of CCTResent Activities of CCT · 2014. 4. 25. · Shift CO2 Capture Technology IGCC Gas clean-up facilities CO2 Capture Technology o n CO Steam Ai Coal Air reactor

Nakoso IGCC Demonstration Plant Becomes First IGCC Commercial Plant in Japan (Nakoso Unit 10)

• To acquire data for designing a demonstration plant, a 200 t/d IGCC pilot plant was put into operation from 1986–1996 under the management of NEDO.

• After the pilot plant project, the demonstration plant, which can produce 250 MW of electricity, was constructed in Nakoso of Fukushima prefecture and operations started in 2007. p p

• Two thousand hours of continuous operations were achieved during the first year of the project in 2008, and cumulative operations of 19,600 hours were attained as of March, 2013.

• After all test objectives were achieved, the demonstration plant became the first IGCC commercial plant in Japan, Nakoso Unit 10th on April 1, 2013. p p

Updating Nakoso 250MW IGCC Demonstration Project

Target and Achievement

Targets Results Status of Achievement

Future plan

S f d 250MW 250MW A hi dSafe and Stable Operation

250MW 250MW Achieved -

Long Term continuousOperation

>2000hr 2238hr Achieved -

Net Thermal Efficiency >42% (LHV basis) 42.9% Achieved -

Carbon Conversion Rate >99.9% >99.9% Achieved -

Environmental Performance

SOx <8ppmNOx <5ppm

1.0ppm3.4ppm

Achieved -

Dust <4mg/m3N <0.1mg/m3N

Coals Bituminous (B)Sub-bituminous (SB)

Chinese (B)Russian (B)USA (2SB) Indonesian (B,2SB)

Achieved Increase in coalTypes

Indonesian (B,2SB)Colombian (B)Canadian (B)

Start-up Time <18hr 15hr Achieved -

Minimum Load 50% 36% Achieved -

Load Change Rate 3%/min 3%/min Achieved -

Durability &Reliability &

Maintainability

Evaluate during5000hr test

5013hr in one year,No serious damage

Same as conventional PCF

Maintenanceinterval Evaluation,Higher availabilityy

Economy estimation Less than or equalto PCF power generation cost

Construction cost and operation cost was estimated.

Could becompatiblewith PCF

Maintenance costEvaluation etc.

Page 10: Resent Activities of CCTResent Activities of CCT · 2014. 4. 25. · Shift CO2 Capture Technology IGCC Gas clean-up facilities CO2 Capture Technology o n CO Steam Ai Coal Air reactor

As Japan has achieved the world’s highest efficiency levels for coal-fired thermal power generation technology, project feasibility studies are currently being conducted on high-efficiency CCT, such as USC and IGCC in order to disseminate CCT technologies worldwide and reduce global CO2 emissions.

41

43

[%]

G

Japan Feasibility studies are currently being carried out on the following

35

37

39

cy (G

ross

, LHV

)

ChinaAustralia

Germany

USA

carried out on the following technologies:

・ USC, USC + CCS

・ IGCC, IGCC + CCS

27

29

31

33

Ther

mal

Effic

ienc

India

,

・ Coal gasification (SNG, H2, clean synthetic fuel, etc.)

・ Upgrading or drying of low rank coal

25

27

'90

'91

'92

'93

'94

'95

'96

'97

'98

'99

2000 '01

'02

'03

'04

'05

'06

'07

T

Japan Germany U.S.A. Australia China India

Year

・ Operational know-how (combustion simulation, etc.)

International comparison of fossil fuel power generation efficiency (ECOFYS) (2010)

Resultsesu ts

・Project formation

・Potential for CO2

reductions

AdoptionApplication FS implementation Next step is implemented by private sector through

Screening

Report FS results to

JBIC loans, etc

Explanation of project to

Technology investigation

Screeningby

outside experts and

NEDO

counterpart country

Collection of information for

follow-up

counterpart country

commission(advice for

project development)

Project management・meeting・monthly process Provide information

f F ibilitfor Feasibility Studies on

Bilateral Offset Credit Mechanism

Evaluation

Page 11: Resent Activities of CCTResent Activities of CCT · 2014. 4. 25. · Shift CO2 Capture Technology IGCC Gas clean-up facilities CO2 Capture Technology o n CO Steam Ai Coal Air reactor

▲ 2011 project formation research

▲ 2012 project formation research

★ 2011: Advanced operation know-how using coal-fired boiler simulation in China★ 2011: IGCC project in Lang Fang, China★ 2012: Advanced operation know-how using low rank coal-fired boiler simulation in China 2012 project formation research

★ 2011: Clean synthetic fuel using coal project in Mongolia

★2011 2012: High efficiency coal power★2011-2012: High-efficiency coal power plant (USC) in Poland

★ 2012: High-efficiency coal power plant (USC) in Bosnia and Herzegovina

★ 2012: HECA IGCC project (additional FS) in the U.S.

▲▲▲

★ 2011: High-efficiency coal power plant

▲▲

▲▲▲▲

★ g y p p(USC) and CCS in Bulgaria

▲▲

★ 2012: Upgraded brown coal (UBC) and high-efficiency coal power plant (USC) in India

★ 2012: CCS and turbine renewable project

★ 2011: IGCC project in Indonesia★ 2011: Substitute coking coal project using low rank coal in Indonesia★ 2012 L k l / t t b d i t

★ 2011-2012: Hydrogen energy supply chain using Victorian brown coal in Australia

▲ ▲★ 2012: Co-firing domestic anthracite and imported coal at a high-efficiency coal power plant in Vietnam

★ 2012: CCS and turbine renewable projectin Taiwan

★ 2012: Low rank coal power/steam tube drying system★ 2012: Circulation fluidized bed power plant in Indonesia

brown coal in Australia★ 2012: Oxy-fuel combustion power plant (USC) in Australia

1. Scope of Work

Mitsubishi Heavy Industries is currently carrying out front-end engineering design activities (FEED) as part of the Hydrogen Energy California project (HECA). Additional research to support the HECA project is being conducted in order to improve the economic feasibility of the project by raising the blending ratio ofimprove the economic feasibility of the project by raising the blending ratio of pet coke through a gasification test. The potential for GHG emissions reductions is also being evaluated through this research.

J 2012 M h 20132. Duration

3. Entrusted Company

June 2012–March 2013

Mitsubishi Heavy Industries

Coal

Gasifier SGC

Steam

CO₂

Gasifier

Pulverizer

Hoppe Char

Syngas

Electricity

AGR

GTCCPower plant

Hopper

Slag hopper

Char

ChemicalsChemical process

Acid gas

Removal

22

Page 12: Resent Activities of CCTResent Activities of CCT · 2014. 4. 25. · Shift CO2 Capture Technology IGCC Gas clean-up facilities CO2 Capture Technology o n CO Steam Ai Coal Air reactor

FS results on 500 MW class USC + CCS plant

Coolingtowertower

CO2 captureand compressor

USC plantESP

FGD

The results of the FS showed that one high-efficiency USC unit of 500 MW class would be more effective as efficiency would increase by 6% (32%→38%) and y y % ( % %)construction costs would be the same compared to construction costs for two subcritical 225 MW units.

• NEDO’s CCT Development Strategy is as follows:

① Improvement of Coal-fired Power Generation Efficiency

② Feasibility Study on CCS in Japany y

③ Dissemination of High-efficiency CCT

・ We are currently conducting the project feasibility on high-efficiency CCT, such as USC and IGCC in order to disseminate CCT technologies worldwide and reduce global CO2 emissions.g g

Page 13: Resent Activities of CCTResent Activities of CCT · 2014. 4. 25. · Shift CO2 Capture Technology IGCC Gas clean-up facilities CO2 Capture Technology o n CO Steam Ai Coal Air reactor

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