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BIOENERGY WITH CO BIOENERGY WITH CO 2 REMOVAL AND REMOVAL AND DISPOSAL DISPOSAL - An approach to negative CO - An approach to negative CO 2 emissions in energy systems emissions in energy systems IEA Workshop Edinburgh, 12 th November 2001 Kenneth Möllersten Royal Institute of Technology Sweden

IEA Workshop Edinburgh, 12 th November 2001 Kenneth Möllersten

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BIOENERGY WITH CO 2 REMOVAL AND DISPOSAL - An approach to negative CO 2 emissions in energy systems. IEA Workshop Edinburgh, 12 th November 2001 Kenneth Möllersten Royal Institute of Technology Sweden. Today’s presentation. Basic concept Results from studied cases - PowerPoint PPT Presentation

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Page 1: IEA Workshop Edinburgh, 12 th  November 2001 Kenneth Möllersten

BIOENERGY WITH COBIOENERGY WITH CO22 REMOVAL AND REMOVAL AND DISPOSALDISPOSAL

- An approach to negative CO- An approach to negative CO22 emissions in emissions in energy systemsenergy systems

IEA Workshop

Edinburgh, 12th November 2001

Kenneth Möllersten

Royal Institute of TechnologySweden

Page 2: IEA Workshop Edinburgh, 12 th  November 2001 Kenneth Möllersten

Today’s presentation

• Basic concept

• Results from studied cases

• Ongoing research

• Policy-related issues

Page 3: IEA Workshop Edinburgh, 12 th  November 2001 Kenneth Möllersten

Conventional bioenergy

energyproducts

biofuels

ashes (minerals)

CO2

CO2

Page 4: IEA Workshop Edinburgh, 12 th  November 2001 Kenneth Möllersten
Page 5: IEA Workshop Edinburgh, 12 th  November 2001 Kenneth Möllersten

Bioenergy w CO2 removal and disposal

energy products

biofuels

ashes (minerals)

CO2

CO2 to underground storage

CO2

Page 6: IEA Workshop Edinburgh, 12 th  November 2001 Kenneth Möllersten

Principal methods for CO2 removal

Energyconversionprocess

CO2

removal

AirBio-fuel

Energy

Fluegas

CO2 Fluegas

Combustion CondenserO2

EnergyFluegas

CO2 H2OEnergyproducts

Airseparation

Air

Bio-fuel

CO2

CO2

removal

Energyconversionprocess

H2 orH2 and CO

CO2

Gasification

Air/O2 Biofuel Energy

CO shift(optional)

Fluegas

Energyproducts

Energyproducts

Page 7: IEA Workshop Edinburgh, 12 th  November 2001 Kenneth Möllersten

Specific CO2 emissions of power/CHP plants with CO2 removal (incl. compression to 100bar)

-3

-2,5

-2

-1,5

-1

-0,5

0

0,5

Coal-firedsteam power

plant

Coal IGCC NGCC Black liquorrecovery boiler

Black liquorIGCC

kgC

O2/

kWhe

Page 8: IEA Workshop Edinburgh, 12 th  November 2001 Kenneth Möllersten

CO2 removal costs (incl. compression to 100bar)

Option Cost (US$/t CO2)(10-15% annual capital charge)

Coal IGCC/CO shift/pre combustion removal

22-27

Coal Steam Power/flue gas removal

28-49

NGCC/flue gas removal

32-57

BL recovery boiler/flue gas removal

33

BLIGCC/pre combustion removal

18

+ around US$ 20-30 /t CO2 for transportation and disposal

Page 9: IEA Workshop Edinburgh, 12 th  November 2001 Kenneth Möllersten

CO2 consequences of alternative recovery boiler replacements in pulp mill

New recovery boiler Recovery boiler w CO2 removal

-200

0

200

400

600

800

1000

Power Total Power RemovedCO2

Penalty -transp &injection

Total

CO

2 r

ed

uc

tio

n (

kt

CO

2(y

)

Page 10: IEA Workshop Edinburgh, 12 th  November 2001 Kenneth Möllersten

CO2 consequences of alternative recovery boiler replacements in pulp mill

-200

0

200

400

600

800

1000

Power Total Power RemovedCO2

Penalty -transp &injection

Total

CO

2 r

ed

uc

tio

n (

kt

CO

2/y

)

BLIGCC BLIGCC w CO2 removal

Page 11: IEA Workshop Edinburgh, 12 th  November 2001 Kenneth Möllersten

Potential & cost-effectiveness of CO2 reductions in the Swedish pulp and paper sector

(Marginal power from coal power plants)

A: Electricity conservationB: Improved electrical efficiency in steam power systemsC: BLIGCCD: BLIGCC with CCSE: Black liquor gasification with CCS, methanol production and CCF: Conversion of lime kiln to biofuelsG: Cogeneration of wood-based methanol and heat in paper mills

F

400

200

0A

A

F

B

B

C

C

Cost of CO2 Reduction(US$/t CO2)

D

DE

EG

G

2 4 6 8

Capital valuation

Industrial

Societal

Potential CO2 reduction(Mt CO2/y)

Page 12: IEA Workshop Edinburgh, 12 th  November 2001 Kenneth Möllersten

Ongoing research

BlackLiquorGasifier

CO shiftCO2

removal

GTCC/EvGT/

FC

CO2

removal

GTCC/EvGT

rawgas

rawgas

CO2

CO2

CO2

heat

heat

power

power

Page 13: IEA Workshop Edinburgh, 12 th  November 2001 Kenneth Möllersten

Summary removal technologies & system considerations

Option CO2 reduction Additionalcost

Maturity

Flue gas High CO2 removalLower power

High MatureCo-firing wcoal

BIG- CC or fuel(MeOH, H2….)/Partial removal

Lower CO2 removalHigher electricalefficiency

Low BIG notmature

BIG- CC or fuel(MeOH,H2….)/CO shift

High CO2 removal?

? BIG, H2

turbinesnot mature

Page 14: IEA Workshop Edinburgh, 12 th  November 2001 Kenneth Möllersten

Is CO2 from biomass tradable?

• Ways to certify emission reduction credits

• ‘reducing anthropogenic emissions by sources’,or‘enhancing anthropogenic removals by sinks’?

Page 15: IEA Workshop Edinburgh, 12 th  November 2001 Kenneth Möllersten

Implementing bioenergy w CO2 removal & disposal

• CO2 disposal schemes are being developed by companies from the fossil-fuel sector. Will they “welcome” disposal of CO2 from biomass?

• Disposal of CO2 from biomass may require cooperation

– CO2 disposal projects are large-scale

– Pulp & paper producers are increasing their focus on core competencies, and less resources are available for energy management

– Bioenergy producers are small and independent

Page 16: IEA Workshop Edinburgh, 12 th  November 2001 Kenneth Möllersten

Research and development

• Introduce biomass energy into CO2 removal and disposal RD&D

• Large-scale biomass energy applications with CO2 removal and disposal

• Identify opportunities for synergies and phasing in biomass in CO2 disposal schemesFor example through:

– Co-firing coal and biomass w CO2 removal

– Introduction of biomass-based methane in natural gas networks

Integration of biomass energy and fossil-fuel energy RD&D is required: