Experiments on Reaction of Glycerol and Tert-Butyl Alcohol at Elevated Temperatures
碩士 === 大同大學 === 化學工程學系(所) === 102 === High-temperature batch reactions of glycerol and tert-butyl alcohol using a solid catalyst Amberlyst-70 were performed in this study. Six experiments were located uniformly over the operating conditions (reaction temperature range (180℃-205℃), TBA/GLY molar rati...
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ndltd-TW-102TTU050630212019-05-15T21:32:55Z http://ndltd.ncl.edu.tw/handle/xft5e4 Experiments on Reaction of Glycerol and Tert-Butyl Alcohol at Elevated Temperatures 甘油與叔丁醇高溫反應之實驗研究 Yu-Heng Lai 賴昱衡 碩士 大同大學 化學工程學系(所) 102 High-temperature batch reactions of glycerol and tert-butyl alcohol using a solid catalyst Amberlyst-70 were performed in this study. Six experiments were located uniformly over the operating conditions (reaction temperature range (180℃-205℃), TBA/GLY molar ratio (1:1- 6:1), and catalyst weight (6wt% - 16wt% by weight of glycerol)). The components of the product organic phase consisted of unconverted TBA, isobutylene (IB), 2,2,4-trimethyl-1-pentene,2,4,4-trimethyl-2-pentene(DIBs),2,2,4,6-pentamethyl-3-heptene,2,2,6,6-tetramethyl-4-methyleneheptane (TIBs) and the oxygen-limited hydrocarbons (HCs). The product aqueous phase was composed of water, unconverted TBA and glycerol. Among the six uniformly distributed experiments, the optimized operating conditions were at the reacting temperature (205℃), the catalyst loading (12wt% of the initial loading of glycerol) and the TBA/GLY molar ratio (5). A maximal conversion of glycerol (98.1%) and the weight ratio of the product organic phase to the initial feed (67.1%) can be achieved. Jyh-Shyong Chang 張志雄 2014 學位論文 ; thesis 119 zh-TW |
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碩士 === 大同大學 === 化學工程學系(所) === 102 === High-temperature batch reactions of glycerol and tert-butyl alcohol using a solid catalyst Amberlyst-70 were performed in this study. Six experiments were located uniformly over the operating conditions (reaction temperature range (180℃-205℃), TBA/GLY molar ratio (1:1- 6:1), and catalyst weight (6wt% - 16wt% by weight of glycerol)). The components of the product organic phase consisted of unconverted TBA, isobutylene (IB), 2,2,4-trimethyl-1-pentene,2,4,4-trimethyl-2-pentene(DIBs),2,2,4,6-pentamethyl-3-heptene,2,2,6,6-tetramethyl-4-methyleneheptane (TIBs) and the oxygen-limited hydrocarbons (HCs). The product aqueous phase was composed of water, unconverted TBA and glycerol.
Among the six uniformly distributed experiments, the optimized operating conditions were at the reacting temperature (205℃), the catalyst loading (12wt% of the initial loading of glycerol) and the TBA/GLY molar ratio (5). A maximal conversion of glycerol (98.1%) and the weight ratio of the product organic phase to the initial feed (67.1%) can be achieved.
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author2 |
Jyh-Shyong Chang |
author_facet |
Jyh-Shyong Chang Yu-Heng Lai 賴昱衡 |
author |
Yu-Heng Lai 賴昱衡 |
spellingShingle |
Yu-Heng Lai 賴昱衡 Experiments on Reaction of Glycerol and Tert-Butyl Alcohol at Elevated Temperatures |
author_sort |
Yu-Heng Lai |
title |
Experiments on Reaction of Glycerol and Tert-Butyl Alcohol at Elevated Temperatures |
title_short |
Experiments on Reaction of Glycerol and Tert-Butyl Alcohol at Elevated Temperatures |
title_full |
Experiments on Reaction of Glycerol and Tert-Butyl Alcohol at Elevated Temperatures |
title_fullStr |
Experiments on Reaction of Glycerol and Tert-Butyl Alcohol at Elevated Temperatures |
title_full_unstemmed |
Experiments on Reaction of Glycerol and Tert-Butyl Alcohol at Elevated Temperatures |
title_sort |
experiments on reaction of glycerol and tert-butyl alcohol at elevated temperatures |
publishDate |
2014 |
url |
http://ndltd.ncl.edu.tw/handle/xft5e4 |
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