Development of a fuel-flexible co-gasification technology
文献类型:期刊论文
作者 | Zhao, YH; Wen, H; Guo, ZC; Xu, ZH |
刊名 | CHINESE JOURNAL OF CHEMICAL ENGINEERING
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出版日期 | 2005-02-01 |
卷号 | 13期号:1页码:96-101 |
关键词 | co-gasification blast furnace gasifier aspen plus clean coal technology (CCT) |
ISSN号 | 1004-9541 |
其他题名 | Chin. J. Chem. Eng. |
中文摘要 | As one of promising clean coal technologies used to reduce pollutant emission and CO2 discharge, co-gasification has been extensively investigated. In this paper, a new co-gasification technology using coal and natural gas was developed. The distinct advantages of this technology are the excellent fuel flexibility and the availability to establish the gasifier by reconstructing the blast furnace or similar shaft furnace. Based on the concept of the new co-gasification technology, lab-scale experiments and modeling study were carried out. The obtained results indicate that gasification is undertaken at ideal thermodynamic environment where quasi-equilibrium could be reached without catalysts. The modeling results are in agreement with experimental data, demonstrating the validity of the model and that Aspen Plus is a useful tool for the analysis of the co-gasification process. Furthermore, the effect of major operation parameters, including oxygen flow rate and steam flow rate, on co-gasification process was investigated using the developed model. |
英文摘要 | As one of promising clean coal technologies used to reduce pollutant emission and CO2 discharge, co-gasification has been extensively investigated. In this paper, a new co-gasification technology using coal and natural gas was developed. The distinct advantages of this technology are the excellent fuel flexibility and the availability to establish the gasifier by reconstructing the blast furnace or similar shaft furnace. Based on the concept of the new co-gasification technology, lab-scale experiments and modeling study were carried out. The obtained results indicate that gasification is undertaken at ideal thermodynamic environment where quasi-equilibrium could be reached without catalysts. The modeling results are in agreement with experimental data, demonstrating the validity of the model and that Aspen Plus is a useful tool for the analysis of the co-gasification process. Furthermore, the effect of major operation parameters, including oxygen flow rate and steam flow rate, on co-gasification process was investigated using the developed model. |
WOS标题词 | Science & Technology ; Technology |
类目[WOS] | Engineering, Chemical |
研究领域[WOS] | Engineering |
关键词[WOS] | FLUIDIZED-BED ; BLAST-FURNACE ; BIOMASS ; PYROLYSIS ; GASIFIER ; PLASTICS ; WASTES |
收录类别 | SCI |
原文出处 | |
语种 | 英语 |
WOS记录号 | WOS:000227861600018 |
公开日期 | 2013-10-25 |
版本 | 出版稿 |
源URL | [http://ir.ipe.ac.cn/handle/122111/4143] ![]() |
专题 | 过程工程研究所_研究所(批量导入) |
作者单位 | Chinese Acad Sci, Inst Proc Engn, Beijing 100080, Peoples R China |
推荐引用方式 GB/T 7714 | Zhao, YH,Wen, H,Guo, ZC,et al. Development of a fuel-flexible co-gasification technology[J]. CHINESE JOURNAL OF CHEMICAL ENGINEERING,2005,13(1):96-101. |
APA | Zhao, YH,Wen, H,Guo, ZC,&Xu, ZH.(2005).Development of a fuel-flexible co-gasification technology.CHINESE JOURNAL OF CHEMICAL ENGINEERING,13(1),96-101. |
MLA | Zhao, YH,et al."Development of a fuel-flexible co-gasification technology".CHINESE JOURNAL OF CHEMICAL ENGINEERING 13.1(2005):96-101. |
入库方式: OAI收割
来源:过程工程研究所
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