Simulation and Analysis of Chemical Looping Processes to Produce Hydrogen with Various Coal-Fuel Sources
碩士 === 國立臺灣科技大學 === 化學工程系 === 103 === By following Zeng et al. (2012)’s work, the process of CDCL is simulated by Aspen Plus® with R-Gibbs module for the fuel reactor, air reactor, and hydrogen generator. And the type of moving-bed reactor is also selected in this paper. The objective of this pa...
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ndltd-TW-103NTUS53421042019-05-15T22:17:45Z http://ndltd.ncl.edu.tw/handle/n2q3uk Simulation and Analysis of Chemical Looping Processes to Produce Hydrogen with Various Coal-Fuel Sources 不同煤炭燃料於化學迴路產氫製程之模擬與分析研究 Tzu-Yuan Huang 黃資元 碩士 國立臺灣科技大學 化學工程系 103 By following Zeng et al. (2012)’s work, the process of CDCL is simulated by Aspen Plus® with R-Gibbs module for the fuel reactor, air reactor, and hydrogen generator. And the type of moving-bed reactor is also selected in this paper. The objective of this paper is to observe the effects of syngas conversion, operating temperature and pressure in fuel reactor. And also, the maximum hydrogen production rate is investigated under three kinds of coal, Pocahontas No.3 (86.15 wt%), Illinois No.6 (63.75 wt%), and Powder River Basin (PRB , 50.23 wt%). The results are shown that hydrogen production rate is proportional to the carbon content in each kind of coal. However, the phenomenon of the oxygen-carrier temperature at the top of air reactor is reverse proportionally to the carbon content. Finally, the optimal amount of oxygen-carrier and the operating condition of this CDCL process can be found in this work. Hao-Yeh Lee 李豪業 2015 學位論文 ; thesis 179 zh-TW |
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Others
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碩士 === 國立臺灣科技大學 === 化學工程系 === 103 === By following Zeng et al. (2012)’s work, the process of CDCL is simulated by Aspen Plus® with R-Gibbs module for the fuel reactor, air reactor, and hydrogen generator. And the type of moving-bed reactor is also selected in this paper.
The objective of this paper is to observe the effects of syngas conversion, operating temperature and pressure in fuel reactor. And also, the maximum hydrogen production rate is investigated under three kinds of coal, Pocahontas No.3 (86.15 wt%), Illinois No.6 (63.75 wt%), and Powder River Basin (PRB , 50.23 wt%). The results are shown that hydrogen production rate is proportional to the carbon content in each kind of coal. However, the phenomenon of the oxygen-carrier temperature at the top of air reactor is reverse proportionally to the carbon content. Finally, the optimal amount of oxygen-carrier and the operating condition of this CDCL process can be found in this work.
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author2 |
Hao-Yeh Lee |
author_facet |
Hao-Yeh Lee Tzu-Yuan Huang 黃資元 |
author |
Tzu-Yuan Huang 黃資元 |
spellingShingle |
Tzu-Yuan Huang 黃資元 Simulation and Analysis of Chemical Looping Processes to Produce Hydrogen with Various Coal-Fuel Sources |
author_sort |
Tzu-Yuan Huang |
title |
Simulation and Analysis of Chemical Looping Processes to Produce Hydrogen with Various Coal-Fuel Sources |
title_short |
Simulation and Analysis of Chemical Looping Processes to Produce Hydrogen with Various Coal-Fuel Sources |
title_full |
Simulation and Analysis of Chemical Looping Processes to Produce Hydrogen with Various Coal-Fuel Sources |
title_fullStr |
Simulation and Analysis of Chemical Looping Processes to Produce Hydrogen with Various Coal-Fuel Sources |
title_full_unstemmed |
Simulation and Analysis of Chemical Looping Processes to Produce Hydrogen with Various Coal-Fuel Sources |
title_sort |
simulation and analysis of chemical looping processes to produce hydrogen with various coal-fuel sources |
publishDate |
2015 |
url |
http://ndltd.ncl.edu.tw/handle/n2q3uk |
work_keys_str_mv |
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