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Search: L773:1226 086X OR L773:1876 794X OR L773:0888 5885 OR L773:1520 5045 > (2010-2014) > Use of Nickel Oxide...

Use of Nickel Oxide as a Catalyst for Tar Elimination in a Chemical-Looping Reforming Reactor Operated with Biomass Producer Gas

Berguerand, Nicolas, 1978 (author)
Chalmers tekniska högskola,Chalmers University of Technology
Lind, Fredrik, 1978 (author)
Chalmers tekniska högskola,Chalmers University of Technology
Israelsson, Mikael, 1985 (author)
Chalmers tekniska högskola,Chalmers University of Technology
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Seemann, Martin, 1975 (author)
Chalmers tekniska högskola,Chalmers University of Technology
Serge, Biollaz (author)
Paul Scherrer Institut
Thunman, Henrik, 1970 (author)
Chalmers tekniska högskola,Chalmers University of Technology
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 (creator_code:org_t)
2012-12-14
2012
English.
In: Industrial & Engineering Chemistry Research. - : American Chemical Society (ACS). - 1520-5045 .- 0888-5885. ; 51:51, s. 16610-16616
  • Journal article (peer-reviewed)
Abstract Subject headings
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  • A secondary tar-cleaning process based on Chemical-Looping Reforming (CLR) was investigated for upgrading biomass producer gas, derived from the Chalmers University of Technology 2-4 MW indirect gasifier. The experiments were conducted in a bench-scale CLR reactor using a manufactured nickel oxide (NiO) catalyst. Although Ni is a well-documented and efficient steam-reforming catalyst, it is susceptible to rapid deactivation under tar-rich conditions. The aim of this study was to explore the advantages of CLR as a gas-cleaning application, a process which offers continuous regeneration of the carbon deposits on catalysts. The tar-reforming performance of this Ni material and its influence on the gas composition and in particular its potential to increase the H2/CO ratio, were studied. The system was tested at reforming temperatures that ranged from 700°C to 880°C and at oxygen concentrations of 1.0% and 2.2% in the inlet feed to regenerator section. The results confirm the strong ability of the catalyst to reform tars. Higher process temperatures clearly promoted tar conversion, with 96% overall conversion at 880°C (99% if benzene is excluded), as compared with 45% conversion at 700°C. The hydrogen production was favored when temperature was raised. Though, a maximum ratio H2/CO of 2.2 was observed at 750°C. Finally, no time-on-stream deactivation of the catalyst in the CLR was observed during the test, which lasted almost 7 hours.

Subject headings

TEKNIK OCH TEKNOLOGIER  -- Maskinteknik (hsv//swe)
ENGINEERING AND TECHNOLOGY  -- Mechanical Engineering (hsv//eng)
TEKNIK OCH TEKNOLOGIER  -- Kemiteknik (hsv//swe)
ENGINEERING AND TECHNOLOGY  -- Chemical Engineering (hsv//eng)
NATURVETENSKAP  -- Kemi (hsv//swe)
NATURAL SCIENCES  -- Chemical Sciences (hsv//eng)

Keyword

Tars
Chemical-Looping Reforming
Catalytic Gas Cleaning
Circulating Fluidized Beds
Biomass Gas Upgrading
Nickel Oxide Catalyst

Publication and Content Type

art (subject category)
ref (subject category)

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