Fabrication of Au/Y catalysts for 0℃ CO Oxidation

碩士 === 國立臺灣大學 === 化學工程學研究所 === 96 === Au/Y catalysts, with high catalytic activity for CO oxidation at 0℃, were prepared in chloroauric acid solutions (HAuCl4). A possible deposition mechanism of gold supported on Y-type zeolite (Au/Y) was developed, according to the experimental results obtained fr...

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Main Authors: Shih-Ting Liu, 劉詩婷
Other Authors: Ben-Zu Wan
Format: Others
Language:zh-TW
Published: 2008
Online Access:http://ndltd.ncl.edu.tw/handle/66628293377960526607
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spelling ndltd-TW-096NTU050630472016-05-11T04:16:51Z http://ndltd.ncl.edu.tw/handle/66628293377960526607 Fabrication of Au/Y catalysts for 0℃ CO Oxidation 製備Au/Y觸媒應用於0℃CO氧化反應 Shih-Ting Liu 劉詩婷 碩士 國立臺灣大學 化學工程學研究所 96 Au/Y catalysts, with high catalytic activity for CO oxidation at 0℃, were prepared in chloroauric acid solutions (HAuCl4). A possible deposition mechanism of gold supported on Y-type zeolite (Au/Y) was developed, according to the experimental results obtained from this research. The effects of water vapor on catalytic activity of Au/Y and the reason for deactivation during the reaction were studied. The catalysts were characterized by AA, ICP, temperature-programmed reduction (TPR), XRD, UV-Vis, HRTEM. It was found that an optimum ratio of H+ and Na+ in zeolite Y, from the pretreatment process of HY and the pretreatment temperature, caused high gold loading. However, more H+ on zeolite Y (HY) would enhance the aggregation of gold species during deposition on Au/Y and result the lower gold loading and the lower catalytic activity. The effects of preparation conditions (i.e. chloroauric acid concentration, NaOH(aq) addition process, pH of gold solution, mixing time, deposition temperature and drying temperature) on gold loading and catalytic activity of Au/Y were significant. In a solution with higher pH, the gold species contained less chlorine, which would generate more gold polymers for deposition. Therefore, Au particles on Au/Y were larger. Gold loading and catalytic activities were lower. In a solution with higher gold concentration, more gold species were deposited on the surface of Y, which caused dramatic deactivation during CO oxidation. Drying temperature of Au/Y catalysts can highly affect the activity of Au/Y for CO oxidation. Some gold species can be reduced during drying at 60℃, which causes the sintering of gold particles and the decreasing of catalytic activity. The main reason for deactivation of Au/Y during CO oxidation were CO2 poison and increasing the gold particle size. It is proposed in this study that during the deposition process, chloride dissociated from AuCl(OH)2 to form [Au(OH)2]+, which then reacted with the zeolite as follows: [Au(OH)2]+ + Hx(Na)1-xY Ben-Zu Wan 萬本儒 2008 學位論文 ; thesis 107 zh-TW
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language zh-TW
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description 碩士 === 國立臺灣大學 === 化學工程學研究所 === 96 === Au/Y catalysts, with high catalytic activity for CO oxidation at 0℃, were prepared in chloroauric acid solutions (HAuCl4). A possible deposition mechanism of gold supported on Y-type zeolite (Au/Y) was developed, according to the experimental results obtained from this research. The effects of water vapor on catalytic activity of Au/Y and the reason for deactivation during the reaction were studied. The catalysts were characterized by AA, ICP, temperature-programmed reduction (TPR), XRD, UV-Vis, HRTEM. It was found that an optimum ratio of H+ and Na+ in zeolite Y, from the pretreatment process of HY and the pretreatment temperature, caused high gold loading. However, more H+ on zeolite Y (HY) would enhance the aggregation of gold species during deposition on Au/Y and result the lower gold loading and the lower catalytic activity. The effects of preparation conditions (i.e. chloroauric acid concentration, NaOH(aq) addition process, pH of gold solution, mixing time, deposition temperature and drying temperature) on gold loading and catalytic activity of Au/Y were significant. In a solution with higher pH, the gold species contained less chlorine, which would generate more gold polymers for deposition. Therefore, Au particles on Au/Y were larger. Gold loading and catalytic activities were lower. In a solution with higher gold concentration, more gold species were deposited on the surface of Y, which caused dramatic deactivation during CO oxidation. Drying temperature of Au/Y catalysts can highly affect the activity of Au/Y for CO oxidation. Some gold species can be reduced during drying at 60℃, which causes the sintering of gold particles and the decreasing of catalytic activity. The main reason for deactivation of Au/Y during CO oxidation were CO2 poison and increasing the gold particle size. It is proposed in this study that during the deposition process, chloride dissociated from AuCl(OH)2 to form [Au(OH)2]+, which then reacted with the zeolite as follows: [Au(OH)2]+ + Hx(Na)1-xY
author2 Ben-Zu Wan
author_facet Ben-Zu Wan
Shih-Ting Liu
劉詩婷
author Shih-Ting Liu
劉詩婷
spellingShingle Shih-Ting Liu
劉詩婷
Fabrication of Au/Y catalysts for 0℃ CO Oxidation
author_sort Shih-Ting Liu
title Fabrication of Au/Y catalysts for 0℃ CO Oxidation
title_short Fabrication of Au/Y catalysts for 0℃ CO Oxidation
title_full Fabrication of Au/Y catalysts for 0℃ CO Oxidation
title_fullStr Fabrication of Au/Y catalysts for 0℃ CO Oxidation
title_full_unstemmed Fabrication of Au/Y catalysts for 0℃ CO Oxidation
title_sort fabrication of au/y catalysts for 0℃ co oxidation
publishDate 2008
url http://ndltd.ncl.edu.tw/handle/66628293377960526607
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AT liúshītíng zhìbèiauychùméiyīngyòngyú0coyǎnghuàfǎnyīng
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