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Biomass steam-reforming in a low throughput fluidized bed reactor

Research output: Contribution to conference - Without ISBN/ISSN Conference paperpeer-review

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Biomass steam-reforming in a low throughput fluidized bed reactor. / Aiouache, Farid; Kitagawa, Kuniyuki.

2004. 6179-6186 Paper presented at 2004 AIChE Annual Meeting, Austin, TX, United States.

Research output: Contribution to conference - Without ISBN/ISSN Conference paperpeer-review

Harvard

Aiouache, F & Kitagawa, K 2004, 'Biomass steam-reforming in a low throughput fluidized bed reactor', Paper presented at 2004 AIChE Annual Meeting, Austin, TX, United States, 7/11/04 - 12/11/04 pp. 6179-6186. <https://folk.ntnu.no/skoge/prost/proceedings/aiche-2004/pdffiles/papers/333b.pdf>

APA

Aiouache, F., & Kitagawa, K. (2004). Biomass steam-reforming in a low throughput fluidized bed reactor. 6179-6186. Paper presented at 2004 AIChE Annual Meeting, Austin, TX, United States. https://folk.ntnu.no/skoge/prost/proceedings/aiche-2004/pdffiles/papers/333b.pdf

Vancouver

Aiouache F, Kitagawa K. Biomass steam-reforming in a low throughput fluidized bed reactor. 2004. Paper presented at 2004 AIChE Annual Meeting, Austin, TX, United States.

Author

Aiouache, Farid ; Kitagawa, Kuniyuki. / Biomass steam-reforming in a low throughput fluidized bed reactor. Paper presented at 2004 AIChE Annual Meeting, Austin, TX, United States.8 p.

Bibtex

@conference{4a6b5f4b18ab4f8f869461c70525b1b5,
title = "Biomass steam-reforming in a low throughput fluidized bed reactor",
abstract = "This work presents the results from biomass gasification tests in a low throughput fluidized bed membrane reactor (FBMR) and compares them with two-phase model predictions. The operating temperature was decreased to 550°C, while an equimolar steam/cellulose ratio was used. The profiles of kinetics limitation and biomass conversion were analysed when a palladium (Pd) membrane for hydrogen separation was used. The produced gases were analysed by gas chromatography, while steam composition and temperature profiles were retrieved by near-infrared imaging (NIRI) technique. As a single membrane tube did not show high permeability rates, the changes in conversions and temperatures profiles were not significant when a Pd membrane was incorporated. The experimental design and procedure allowed us to visualize low radial dispersions in the FBMR.",
author = "Farid Aiouache and Kuniyuki Kitagawa",
year = "2004",
month = dec,
day = "1",
language = "English",
pages = "6179--6186",
note = "2004 AIChE Annual Meeting ; Conference date: 07-11-2004 Through 12-11-2004",

}

RIS

TY - CONF

T1 - Biomass steam-reforming in a low throughput fluidized bed reactor

AU - Aiouache, Farid

AU - Kitagawa, Kuniyuki

PY - 2004/12/1

Y1 - 2004/12/1

N2 - This work presents the results from biomass gasification tests in a low throughput fluidized bed membrane reactor (FBMR) and compares them with two-phase model predictions. The operating temperature was decreased to 550°C, while an equimolar steam/cellulose ratio was used. The profiles of kinetics limitation and biomass conversion were analysed when a palladium (Pd) membrane for hydrogen separation was used. The produced gases were analysed by gas chromatography, while steam composition and temperature profiles were retrieved by near-infrared imaging (NIRI) technique. As a single membrane tube did not show high permeability rates, the changes in conversions and temperatures profiles were not significant when a Pd membrane was incorporated. The experimental design and procedure allowed us to visualize low radial dispersions in the FBMR.

AB - This work presents the results from biomass gasification tests in a low throughput fluidized bed membrane reactor (FBMR) and compares them with two-phase model predictions. The operating temperature was decreased to 550°C, while an equimolar steam/cellulose ratio was used. The profiles of kinetics limitation and biomass conversion were analysed when a palladium (Pd) membrane for hydrogen separation was used. The produced gases were analysed by gas chromatography, while steam composition and temperature profiles were retrieved by near-infrared imaging (NIRI) technique. As a single membrane tube did not show high permeability rates, the changes in conversions and temperatures profiles were not significant when a Pd membrane was incorporated. The experimental design and procedure allowed us to visualize low radial dispersions in the FBMR.

M3 - Conference paper

AN - SCOPUS:22544437582

SP - 6179

EP - 6186

T2 - 2004 AIChE Annual Meeting

Y2 - 7 November 2004 through 12 November 2004

ER -