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Institute of Chemical Engineering page 1 Achema 2012 Chemical Process Engineering Working group Gasification & Gas Cleaning [email protected]

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Institute of Chemical Engineering page 1Achema 2012

Chemical Process Engineering

Working group Gasification & Gas Cleaning

[email protected]

Institute of Chemical Engineering page 2Achema 2012

Chemical Process Engineering

Working group Gasification & Gas Cleaning

Content

• Working group Gasification and Gas Cleaning

• Dual fluidised bed gasification fundamentals

• Design development

• Industrial application

• Catalytic tar removal

• Contacts

Institute of Chemical Engineering page 3Achema 2012

Chemical Process Engineering

The GGC team focuses on projects from the energy technology sector with a

specification on gasification technologies as well as catalytic tar removal from

producer gas originating from thermo-chemical hydrocarbon conversion

processes.

Mission: Development of fuel flexible, high efficient gasification technologies for

the production of high quality syngas.

Research topics:

• Dual fluidized bed steam gasification of biomass, coal, waste materials

• Producer gas adaptation by catalytically active bed material

• Catalytic reforming of hydrocarbons in secondary fixed bed units

• Development of a new gasification process based on the dual fluidized bed process

• Pressurized gasification

Working group Gasification & Gas Cleaning

Institute of Chemical Engineering page 4Achema 2012

Chemical Process Engineering

Biomass Steam Gasification

Syngas

Electricity

Fuels

Heating/ Cooling

Thermal Gasification, Biomass

combined heat and power plant

in Guessing, Austria

Institute of Chemical Engineering page 5Achema 2012

Chemical Process Engineering

DFB Gasification – Principle of the process I

Steam Air

Biomass

Gasification

(~ 850 °C)

Combustion

(~ 920 °C)

Producer Gas

(CH4, CO, H2, CO2, H2O)Flue gas

Circulation

(bed material,

char coal)

Heat

Fuel to

combustion

Institute of Chemical Engineering page 6Achema 2012

Chemical Process Engineering

DFB Gasification – Principle of the process I

Steam Air

Biomass

Circulation

(bed material,

char coal)

Heat

Fuel to

combustion

CaCO3

CaO

Producer gas

(H2-rich)

Flue gas

(+CO2)

Gasification

+absorption

600…700°C 850…900°C

Combustion

+desorption

Dual fluidised bed steam gasification of solid biomass coupled with CO2 capture

CaO + CO2 ↔ CaCO3

Institute of Chemical Engineering page 7Achema 2012

Chemical Process Engineering

DFB Gasification – Principle of the process II

Typical producer gas composition

Component Unit Conventional process SER process*

H2 vol.-%db 36 … 42 55 … 70

CO vol.-%db 19 … 24 5 … 11

CO2 vol.-%db 20 … 25 7 … 20

CH4 vol.-%db 9 … 12 8 … 13

C2H4 vol.-%db 2.0 … 2.6 1.4 … 1.8

C2H6 vol.-%db 1.3 … 1.8 0.3 … 0.6

C3-Fract. vol.-%db 0.3 … 0.6 0.3 … 1.0

Tar g/Nm³db 4 … 8 0.3 … 0.9

Dust g/Nm³db 10 … 20 20 … 50

H2O vol.-% 30 … 45 50 … 60

Fuel wood pellets wood pellets

Bed material Olivine Calcite

* SER: Sorption enhanced reforming

Institute of Chemical Engineering page 8Achema 2012

Chemical Process Engineering

Design development I

1993-1996, „FICFB* gasifier“

* Fast Internally Circulating Fluidized Bed

Institute of Chemical Engineering page 9Achema 2012

Chemical Process Engineering

Design development II

1999-2003 2004-now

Institute of Chemical Engineering page 10Achema 2012

Chemical Process Engineering

Investigations on a novel

fluidized bed concept

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Advanced DUAL FLUID gasifier

Institute of Chemical Engineering page 11Achema 2012

Chemical Process Engineering

Details of the countercurrent gasification reactor

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Advanced DUAL FLUID gasifier

Institute of Chemical Engineering page 12Achema 2012

Chemical Process Engineering

Industrial application

Güssing, Austria

in operation since 2002

8.0 MWth, 2.0 Mwel

gas engine

Oberwart, Austria

in operation since 2008

8.5 MWth, 2.8 Mwel

gas engine, organic rankie cycle (ORC)

Plants under commissioning: Villach, Austria - 15 MWth, 3.7 Mwel, gas engine

Klagenfurt, Austria - 25 MWth, 5.5 Mwel, gas engine, ORC

Ulm, Germany - 15 MWth, 5.3 Mwel, gas engine, ORC

Plants in planning: Gothenborg, Sweden - 30 MWth, 20 Mwel, Synthetic

Natural Gas (SNG) production of 67%

Institute of Chemical Engineering page 13Achema 2012

Chemical Process Engineering

Catalytic tar removal

Photographer Hans Ringhofer

Test rig

• 2 stage reformer

• 4 & 4 honeycomb catalysts

• 100 Nm³/h

• ~ 900°C

• Atmospheric pressure

Aims:

• Long term tests of catalytic gas cleaning with

real product gas from an industrial DFB-steam

gasifier (Güssing)

• To find selective catalysts for reforming

hydrocarbons - except Methane => BioSNG

• To find selective catalysts for reforming

hydrocarbons - especially Methane => Fischer-

Tropsch

• To find best process parameters regarding

lifetime and reforming potential of the catalysts.

Institute of Chemical Engineering page 14Achema 2012

Chemical Process Engineering

Further information

Links:

http://www.vt.tuwien.ac.at

http://www.vt.tuwien.ac.at/chemische_verfahrenstechnik_und_wirbelschichttechnik/gasification_and_gas_cleaning/

Contact:

Univ.Prof. Dr. Hermann HOFBAUER

Email: [email protected]

Tel.: +43 1 58801 166300