TAR/CH4 REFORMING BY CATALYTICALLY ACTIVE MATERIALS IN A BIOMASS DUAL FLUIDISED BED GASIFIER
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 plants2010-12-132010-12-132025-09-25Bibliographically approved