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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Main Authors: Yi-Rou Lu, 呂易柔
Other Authors: Young Ku
Format: Others
Language:en_US
Published: 2016
Online Access:http://ndltd.ncl.edu.tw/handle/45944509133494743619
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spelling 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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language en_US
format Others
sources NDLTD
description 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.
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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