Experimental Study on Water-gas Shift Reaction Performance at Ultrahigh Temperatures

碩士 === 國立中興大學 === 機械工程學系所 === 103 === In this study, monometallic and bimetallic catalysts (Pt, Ni, and Pt/Ni) supported on single or multiple oxides (Al2O3, TiO2, CeO2/Al2O3, and CeO2/TiO2) were prepared and tested in the catalytic water-gas shift reaction (WGSR) at ultra-high temperatures.The syng...

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Main Authors: Chien-Min Fang, 方建閔
Other Authors: Rei-Yu Chein
Format: Others
Language:zh-TW
Published: 2015
Online Access:http://ndltd.ncl.edu.tw/handle/80011618495391056834
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spelling ndltd-TW-103NCHU53110572017-06-17T04:31:38Z http://ndltd.ncl.edu.tw/handle/80011618495391056834 Experimental Study on Water-gas Shift Reaction Performance at Ultrahigh Temperatures 超高溫水氣轉換反應之實驗探討 Chien-Min Fang 方建閔 碩士 國立中興大學 機械工程學系所 103 In this study, monometallic and bimetallic catalysts (Pt, Ni, and Pt/Ni) supported on single or multiple oxides (Al2O3, TiO2, CeO2/Al2O3, and CeO2/TiO2) were prepared and tested in the catalytic water-gas shift reaction (WGSR) at ultra-high temperatures.The syngas (18%H2, 22%CO2, 30%CO, 30%N2) and steam with steam to carbon ratio of 1, 3, and 5 were used as the feedstock.The operation pressure was fixed as 1 atm while the reaction temperature was varied from 750 to 850℃.The measured results indicated that Ni/Al2O3 has the worst performance as compared with other catalysts.The reason for this result might be attributed to the poor ability of irreducible oxides on metal dispersion.Better WGSR performance can be resulted from bimetallic catalyst supported by multiple oxides.The best CO conversion and H2 yield obtained were 59.48% and 34.18%, respectively.Based on the measured results showing reduced N2 flow rate at reactor outlet, it is suspected that N2 reacts with H2 and deposited carbon to form ammonia (NH3) and hydrogen cyanide (HCN) and results in low H2 yield. Rei-Yu Chein 簡瑞與 2015 學位論文 ; thesis 108 zh-TW
collection NDLTD
language zh-TW
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description 碩士 === 國立中興大學 === 機械工程學系所 === 103 === In this study, monometallic and bimetallic catalysts (Pt, Ni, and Pt/Ni) supported on single or multiple oxides (Al2O3, TiO2, CeO2/Al2O3, and CeO2/TiO2) were prepared and tested in the catalytic water-gas shift reaction (WGSR) at ultra-high temperatures.The syngas (18%H2, 22%CO2, 30%CO, 30%N2) and steam with steam to carbon ratio of 1, 3, and 5 were used as the feedstock.The operation pressure was fixed as 1 atm while the reaction temperature was varied from 750 to 850℃.The measured results indicated that Ni/Al2O3 has the worst performance as compared with other catalysts.The reason for this result might be attributed to the poor ability of irreducible oxides on metal dispersion.Better WGSR performance can be resulted from bimetallic catalyst supported by multiple oxides.The best CO conversion and H2 yield obtained were 59.48% and 34.18%, respectively.Based on the measured results showing reduced N2 flow rate at reactor outlet, it is suspected that N2 reacts with H2 and deposited carbon to form ammonia (NH3) and hydrogen cyanide (HCN) and results in low H2 yield.
author2 Rei-Yu Chein
author_facet Rei-Yu Chein
Chien-Min Fang
方建閔
author Chien-Min Fang
方建閔
spellingShingle Chien-Min Fang
方建閔
Experimental Study on Water-gas Shift Reaction Performance at Ultrahigh Temperatures
author_sort Chien-Min Fang
title Experimental Study on Water-gas Shift Reaction Performance at Ultrahigh Temperatures
title_short Experimental Study on Water-gas Shift Reaction Performance at Ultrahigh Temperatures
title_full Experimental Study on Water-gas Shift Reaction Performance at Ultrahigh Temperatures
title_fullStr Experimental Study on Water-gas Shift Reaction Performance at Ultrahigh Temperatures
title_full_unstemmed Experimental Study on Water-gas Shift Reaction Performance at Ultrahigh Temperatures
title_sort experimental study on water-gas shift reaction performance at ultrahigh temperatures
publishDate 2015
url http://ndltd.ncl.edu.tw/handle/80011618495391056834
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