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...

Full description

Bibliographic Details
Main Authors: Tzu-Yuan Huang, 黃資元
Other Authors: Hao-Yeh Lee
Format: Others
Language:zh-TW
Published: 2015
Online Access:http://ndltd.ncl.edu.tw/handle/n2q3uk
id ndltd-TW-103NTUS5342104
record_format oai_dc
spelling 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
collection NDLTD
language zh-TW
format Others
sources NDLTD
description 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.
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 AT tzuyuanhuang simulationandanalysisofchemicalloopingprocessestoproducehydrogenwithvariouscoalfuelsources
AT huángzīyuán simulationandanalysisofchemicalloopingprocessestoproducehydrogenwithvariouscoalfuelsources
AT tzuyuanhuang bùtóngméitànránliàoyúhuàxuéhuílùchǎnqīngzhìchéngzhīmónǐyǔfēnxīyánjiū
AT huángzīyuán bùtóngméitànránliàoyúhuàxuéhuílùchǎnqīngzhìchéngzhīmónǐyǔfēnxīyánjiū
_version_ 1719128101922799616