Process Development for Transesterification of Triglyceride and It''s Application

博士 === 國立清華大學 === 化學工程學系 === 91 === Abstract The ever increasing crude oil prices, limited resources and growing environmental concerns have placed greater emphasis on the need to develop viable alternative fuels. Biodiesel is one of the most promising cleaner alternative fuels produced...

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Main Authors: Jech-Wei Chen, 陳志威
Other Authors: Wen-Teng Wu
Format: Others
Language:zh-TW
Published: 2003
Online Access:http://ndltd.ncl.edu.tw/handle/78804655289440924003
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spelling ndltd-TW-091NTHU00630112016-06-22T04:21:07Z http://ndltd.ncl.edu.tw/handle/78804655289440924003 Process Development for Transesterification of Triglyceride and It''s Application 油脂轉酯化反應之製程開發及其應用 Jech-Wei Chen 陳志威 博士 國立清華大學 化學工程學系 91 Abstract The ever increasing crude oil prices, limited resources and growing environmental concerns have placed greater emphasis on the need to develop viable alternative fuels. Biodiesel is one of the most promising cleaner alternative fuels produced from renewable resources. This work aims at the transesterification of triglyceride from natural resources. Immobilized lipase catalyzing transesterification of oils with alcohols is one of the methods for the production of biodiesel. However, the enzyme frequently deactivates by lower-carbon alcohols like methanol, leading to the decrease of reaction rate. An investigation into the mechanism of lipase deactivation revealed that the lower-carbon alcohol adsorbs on the surface of the immobilized enzyme, forming a barrier and thereby blocking the contact of triglyceride. Pretreatment and regeneration of using tert-butanol and 2-butanol can increase the activity of the enzyme and makes the process economically feasible. Pretreatment of the immobilized lipase (Novozyme 435) by immersion in the alcohol resulted in seven to ten fold increase in activity compared to that without pretreatment. By following complete deactivation of the enzyme by methanol, washing with tert-butanol and 2-butanol, the enzyme was successfully regenerated to about 75% and 56% of its original activity, respectively. For developing the enzymatic transesterification process, two different strategies have been investigated, i.e. a two-stage process and a dilution process. Using these two processes, 95% conversion can be achieved within the reaction time of 300 min and 63 min, respectively. In these two processes the enzyme can also maintain its activity for six months without any significant loss of activity. This process was also successfully employed for other applications like the recovery of vitamin E and phyto-sterols from the deodorized distillate of soybean oil. Wen-Teng Wu 吳文騰 2003 學位論文 ; thesis 119 zh-TW
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description 博士 === 國立清華大學 === 化學工程學系 === 91 === Abstract The ever increasing crude oil prices, limited resources and growing environmental concerns have placed greater emphasis on the need to develop viable alternative fuels. Biodiesel is one of the most promising cleaner alternative fuels produced from renewable resources. This work aims at the transesterification of triglyceride from natural resources. Immobilized lipase catalyzing transesterification of oils with alcohols is one of the methods for the production of biodiesel. However, the enzyme frequently deactivates by lower-carbon alcohols like methanol, leading to the decrease of reaction rate. An investigation into the mechanism of lipase deactivation revealed that the lower-carbon alcohol adsorbs on the surface of the immobilized enzyme, forming a barrier and thereby blocking the contact of triglyceride. Pretreatment and regeneration of using tert-butanol and 2-butanol can increase the activity of the enzyme and makes the process economically feasible. Pretreatment of the immobilized lipase (Novozyme 435) by immersion in the alcohol resulted in seven to ten fold increase in activity compared to that without pretreatment. By following complete deactivation of the enzyme by methanol, washing with tert-butanol and 2-butanol, the enzyme was successfully regenerated to about 75% and 56% of its original activity, respectively. For developing the enzymatic transesterification process, two different strategies have been investigated, i.e. a two-stage process and a dilution process. Using these two processes, 95% conversion can be achieved within the reaction time of 300 min and 63 min, respectively. In these two processes the enzyme can also maintain its activity for six months without any significant loss of activity. This process was also successfully employed for other applications like the recovery of vitamin E and phyto-sterols from the deodorized distillate of soybean oil.
author2 Wen-Teng Wu
author_facet Wen-Teng Wu
Jech-Wei Chen
陳志威
author Jech-Wei Chen
陳志威
spellingShingle Jech-Wei Chen
陳志威
Process Development for Transesterification of Triglyceride and It''s Application
author_sort Jech-Wei Chen
title Process Development for Transesterification of Triglyceride and It''s Application
title_short Process Development for Transesterification of Triglyceride and It''s Application
title_full Process Development for Transesterification of Triglyceride and It''s Application
title_fullStr Process Development for Transesterification of Triglyceride and It''s Application
title_full_unstemmed Process Development for Transesterification of Triglyceride and It''s Application
title_sort process development for transesterification of triglyceride and it''s application
publishDate 2003
url http://ndltd.ncl.edu.tw/handle/78804655289440924003
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