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dc.contributor.authorZhang, Shu
dc.contributor.authorLuo, Y.
dc.contributor.authorLi, Chun-Zhu
dc.contributor.authorWang, Y.
dc.date.accessioned2017-01-30T12:08:14Z
dc.date.available2017-01-30T12:08:14Z
dc.date.created2015-10-29T04:09:37Z
dc.date.issued2015
dc.identifier.citationZhang, S. and Luo, Y. and Li, C. and Wang, Y. 2015. Changes in char reactivity due to char-oxygen and char-steam reactions using victorian brown coal in a fixed-bed reactor. Chinese Journal of Chemical Engineering. 23 (1): pp. 321-325.
dc.identifier.urihttp://hdl.handle.net/20.500.11937/18505
dc.identifier.doi10.1016/j.cjche.2014.09.044
dc.description.abstract

This study was to examine the influence of reactions of char–O2 and char–steam on the char reactivity evolution. A newly-designed fixed-bed reactor was used to conduct gasification experiments using Victorian brown coal at 800 °C. The chars prepared from the gasification experiments were then collected and subjected to reactivity characterisation (ex-situ reactivity) using TGA (thermogravimetric analyser) in air. The results indicate that the char reactivity from TGA was generally high when the char experienced intensive gasification reactions in 0.3% O2 in the fixed-bed reactor. The addition of steam into the gasification not only enhanced the char conversion significantly but also reduced the char reactivity dramatically. The curve shapes of the char reactivity with involvement of steam were very different from that with O2 gasification, implying the importance of gasifying agents to char properties.

dc.publisherChemical Industry Press
dc.titleChanges in char reactivity due to char-oxygen and char-steam reactions using victorian brown coal in a fixed-bed reactor
dc.typeJournal Article
dcterms.source.volume23
dcterms.source.number1
dcterms.source.startPage321
dcterms.source.endPage325
dcterms.source.issn1004-9541
dcterms.source.titleChinese Journal of Chemical Engineering
curtin.departmentFuels and Energy Technology Institute
curtin.accessStatusFulltext not available


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