Steam co-gasification of coal and biomass - Synergy in reactivity of fuel blends chars

被引:68
作者
Howaniec, Natalia [1 ]
Smolinski, Adam [1 ]
机构
[1] Cent Min Inst, Dept Energy Saving & Air Protect, PL-40166 Katowice, Poland
关键词
Gasification; Co-gasification; Reactivity; Hydrogen; Synergy; FLUIDIZED-BED; EASTERN-EUROPE; RANK COALS; PYROLYSIS; PRESSURE; COPYROLYSIS; TEMPERATURE; ELECTRICITY; POTENTIALS; MISCANTHUS;
D O I
10.1016/j.ijhydene.2013.10.019
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070305 [高分子化学与物理];
摘要
Development of clean coal technologies is the answer to increasing energy demand and environmental concerns related to conventional coal processing technologies. The technologies of fossil fuel gasification are technically proven and commercially available. Attempts of utilization of waste materials and renewable energy resources in gasification-based energy generation systems has been made, but wide application of such systems is still hindered by issues inherently combined with the characteristics of the materials. These include discontinuous supplies of a fuel of limited resources and varying composition resulting in poor economy of small-scale systems and operating problems related to tars formation and corrosion, especially when biomass utilization is considered. In the light of the above co-gasification seems to offer several advantages through mitigation of undesired effects of both carbon-intensive utilization of coal and low efficient and troublesome operation of biomass/waste-fed gasification systems. The experimental results presented in the paper address the issues of determination of potential synergy effects resulting from the utilization of fuel blends composed of materials of various physical and chemical characteristics, which are still insufficiently discussed in the literature, especially when hydrogen-rich gas production in co-gasification is concerned. The results of reactivity tests of fuel blends of coal and energy crops biomass in the process of steam co-gasification in a laboratory scale fixed bed reactor at 700, 800 and 900 degrees C are given proving the synergy effect in co-gasification reflected in increased reactivity of fuel blends when compared to coal and biomass chars reactivity under similar process conditions. Copyright (c) 2013, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:16152 / 16160
页数:9
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