Mid Sweden University

miun.sePublications
Change search
CiteExportLink to record
Permanent link

Direct link
Cite
Citation style
  • apa
  • ieee
  • modern-language-association-8th-edition
  • vancouver
  • Other style
More styles
Language
  • de-DE
  • en-GB
  • en-US
  • fi-FI
  • nn-NO
  • nn-NB
  • sv-SE
  • Other locale
More languages
Output format
  • html
  • text
  • asciidoc
  • rtf
TAR/CH4 REFORMING BY CATALYTICALLY ACTIVE MATERIALS IN A BIOMASS DUAL FLUIDISED BED GASIFIER 
Mid Sweden University, Faculty of Science, Technology and Media, Department of Natural Sciences, Engineering and Mathematics. (Bioenergy - gasification)
Mid Sweden University, Faculty of Science, Technology and Media, Department of Natural Sciences, Engineering and Mathematics. (Bioenergy - gasification)
Mid Sweden University, Faculty of Science, Technology and Media, Department of Natural Sciences, Engineering and Mathematics. (Bioenergy - gasification)
2010 (English)In: The second International Symposium on Gasification and Its Application (ISGA 2010), December 5-8, Fukuoka, Japan, 2010Conference paper, Published paper (Refereed)
Abstract [en]

This paper presents a study on the effects of catalytically active materials, before tests in the 150 kW allothermal biomass gasifier at Mid Sweden University (MIUN). The gasifier has been built up in 2008 for research on synthetic fuel production, and is a combination of a circulating fluidised bed (CFB) riser as combustor and a fluidised bed (FB) as steam gasifier. The MIUN gasifier has a unique design suitable for in-built tar/methane (CH4) catalytic reforming. The lifetime of the catalyst can be prolonged using a dual fluidised bed gasifier (DFBG) with continuously internal regeneration of the catalyst. The catalytic effects of 1) basic condition with silica sand (no catalytic activity), 2) commercial catalyst, 3) development metal-catalyst (high surface area support), and 4) olivine catalyst will be evaluated by comparing tar/CH4 content in the syngas from the gasifier operated under different conditions. Silica sand and commercial catalyst can be considered as extremes for comparing the activity of the chosen conditions.

Place, publisher, year, edition, pages
2010.
Keywords [en]
Biomass Gasification, Syngas Cleaning, Tar Catalytic Reduction, Dual Fluidised Bed
National Category
Chemical Engineering
Identifiers
URN: urn:nbn:se:miun:diva-12542OAI: oai:DiVA.org:miun-12542DiVA, id: diva2:376700
Conference
The second International Symposium on Gasification and Its Application (ISGA 2010), December 5-8, Fukuoka, Japan
Projects
Development of BTL (Biomass To Liquid) Towards Small-scale Automotive-fuel plantsAvailable from: 2010-12-13 Created: 2010-12-13 Last updated: 2025-09-25Bibliographically approved

Open Access in DiVA

No full text in DiVA

Authority records

Göransson, KristinaSöderlind, UlfZhang, Wennan

Search in DiVA

By author/editor
Göransson, KristinaSöderlind, UlfZhang, Wennan
By organisation
Department of Natural Sciences, Engineering and Mathematics
Chemical Engineering

Search outside of DiVA

GoogleGoogle Scholar

urn-nbn

Altmetric score

urn-nbn
Total: 1209 hits
CiteExportLink to record
Permanent link

Direct link
Cite
Citation style
  • apa
  • ieee
  • modern-language-association-8th-edition
  • vancouver
  • Other style
More styles
Language
  • de-DE
  • en-GB
  • en-US
  • fi-FI
  • nn-NO
  • nn-NB
  • sv-SE
  • Other locale
More languages
Output format
  • html
  • text
  • asciidoc
  • rtf