Steam as Gasification Agent for Chemical Looping Combustion of Charcoal in an Annular Dual-tube Moving Bed Reactor
碩士 === 國立臺灣科技大學 === 化學工程系 === 104 === hemical looping combustion was conducted in moving bed reactor with various gasification agents, inclining steam mixture, steam/CO2 mixture, steam/O2 mixture and steam/H2 mixture. In the moving bed reactor, high fixed carbon content solid fuel, BC-charcoal, and...
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ndltd-TW-104NTUS53420342017-09-10T04:30:09Z http://ndltd.ncl.edu.tw/handle/45944509133494743619 Steam as Gasification Agent for Chemical Looping Combustion of Charcoal in an Annular Dual-tube Moving Bed Reactor 以蒸氣作為氣化劑於移動床燃料反應器應用化學迴路燃燒程序處理木炭之評估研究 Yi-Rou Lu 呂易柔 碩士 國立臺灣科技大學 化學工程系 104 hemical looping combustion was conducted in moving bed reactor with various gasification agents, inclining steam mixture, steam/CO2 mixture, steam/O2 mixture and steam/H2 mixture. In the moving bed reactor, high fixed carbon content solid fuel, BC-charcoal, and iron-based oxygen carriers was employed with different gasification agents. Alumina and titania supported Fe2O3 were prepared to evaluate its feasibility as an oxygen carrier for chemical looping combustion. Fe2O3/Al2O3 oxygen carriers were prepared by wet shear granulation preparation and showed better reactivity and recyclability thermogravimetric analysis, crush strength and attrition rate. In this research, BC-charcoal gasification was conducted with various gasification agents at various operational temperatures and gasification agent flow rates to gain high quality syngas produce and determined better operational condition for BC-charcoal combustion in an empty bed reactor. The fuel conversion was increased with increasing operational temperature and gasification agents flow rate in the empty bed reactor. BC-charcoal combustion was successfully carried out in the moving bed fuel reactor with various gasification agents and mostly 100 % yield of carbon dioxide was obtained in all case. Using steam/H2 mixture was reached higher oxygen carriers conversion; furthermore, the reduced Fe2O3/Al2O3 oxygen carriers were capable for hydrogen generation. By analysis of system processing capacity, 20-30% of output processing capacity is acquired for gasification process and other energy could employ for external facility. When steam/O2 mixture and steam/H2 mixture were used for BC-charcoal combustion, it was not acquired extra output processing capacity. Young Ku 顧洋 2016 學位論文 ; thesis 128 en_US |
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碩士 === 國立臺灣科技大學 === 化學工程系 === 104 === hemical looping combustion was conducted in moving bed reactor with various gasification agents, inclining steam mixture, steam/CO2 mixture, steam/O2 mixture and steam/H2 mixture. In the moving bed reactor, high fixed carbon content solid fuel, BC-charcoal, and iron-based oxygen carriers was employed with different gasification agents. Alumina and titania supported Fe2O3 were prepared to evaluate its feasibility as an oxygen carrier for chemical looping combustion. Fe2O3/Al2O3 oxygen carriers were prepared by wet shear granulation preparation and showed better reactivity and recyclability thermogravimetric analysis, crush strength and attrition rate.
In this research, BC-charcoal gasification was conducted with various gasification agents at various operational temperatures and gasification agent flow rates to gain high quality syngas produce and determined better operational condition for BC-charcoal combustion in an empty bed reactor. The fuel conversion was increased with increasing operational temperature and gasification agents flow rate in the empty bed reactor. BC-charcoal combustion was successfully carried out in the moving bed fuel reactor with various gasification agents and mostly 100 % yield of carbon dioxide was obtained in all case. Using steam/H2 mixture was reached higher oxygen carriers conversion; furthermore, the reduced Fe2O3/Al2O3 oxygen carriers were capable for hydrogen generation.
By analysis of system processing capacity, 20-30% of output processing capacity is acquired for gasification process and other energy could employ for external facility. When steam/O2 mixture and steam/H2 mixture were used for BC-charcoal combustion, it was not acquired extra output processing capacity.
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author2 |
Young Ku |
author_facet |
Young Ku Yi-Rou Lu 呂易柔 |
author |
Yi-Rou Lu 呂易柔 |
spellingShingle |
Yi-Rou Lu 呂易柔 Steam as Gasification Agent for Chemical Looping Combustion of Charcoal in an Annular Dual-tube Moving Bed Reactor |
author_sort |
Yi-Rou Lu |
title |
Steam as Gasification Agent for Chemical Looping Combustion of Charcoal in an Annular Dual-tube Moving Bed Reactor |
title_short |
Steam as Gasification Agent for Chemical Looping Combustion of Charcoal in an Annular Dual-tube Moving Bed Reactor |
title_full |
Steam as Gasification Agent for Chemical Looping Combustion of Charcoal in an Annular Dual-tube Moving Bed Reactor |
title_fullStr |
Steam as Gasification Agent for Chemical Looping Combustion of Charcoal in an Annular Dual-tube Moving Bed Reactor |
title_full_unstemmed |
Steam as Gasification Agent for Chemical Looping Combustion of Charcoal in an Annular Dual-tube Moving Bed Reactor |
title_sort |
steam as gasification agent for chemical looping combustion of charcoal in an annular dual-tube moving bed reactor |
publishDate |
2016 |
url |
http://ndltd.ncl.edu.tw/handle/45944509133494743619 |
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