Study on membrane distillation in continuous fermentation system
碩士 === 嘉南藥理科技大學 === 環境工程與科學系暨研究所 === 98 === Membrane distillation (MD) is a relatively new separation process which is being investigated worldwide as a low cost, energy saving alternative to other conventional separation processes. The major aim of this proposal is that the bioethanol produced from...
Main Authors: | , |
---|---|
Other Authors: | |
Format: | Others |
Language: | zh-TW |
Published: |
2010
|
Online Access: | http://ndltd.ncl.edu.tw/handle/02717025337623432508 |
id |
ndltd-TW-098CNUP5515020 |
---|---|
record_format |
oai_dc |
spelling |
ndltd-TW-098CNUP55150202015-10-13T19:06:44Z http://ndltd.ncl.edu.tw/handle/02717025337623432508 Study on membrane distillation in continuous fermentation system 薄膜蒸餾應用於連續發酵系統之研究 Ming-Chao Yu 游銘昭 碩士 嘉南藥理科技大學 環境工程與科學系暨研究所 98 Membrane distillation (MD) is a relatively new separation process which is being investigated worldwide as a low cost, energy saving alternative to other conventional separation processes. The major aim of this proposal is that the bioethanol produced from fermentation via the membrane distillation system through the expanded polytetrafluoroethylene (ePTFE) membranes. Hopefully, a high flux of MD membrane and ethanol separated from the reaction mixtures can be obtained in this program. We aim to concentrate and purify ethanol through the membranes from simulate fermentation system, and establish a continuous MD system for separate and purify bioethanol from fermentor. Moreover in the energy conservation, this research discusses the effect of little temperature difference. In addition, the effects of temperature and pressure gradient of the MD system and the air-gap distance on the ethanol purify performance will be investigated. Keywords: ePTFE, Membrane distillation, fermentation. Cheng-Lee Lai 賴振立 2010 學位論文 ; thesis 121 zh-TW |
collection |
NDLTD |
language |
zh-TW |
format |
Others
|
sources |
NDLTD |
description |
碩士 === 嘉南藥理科技大學 === 環境工程與科學系暨研究所 === 98 === Membrane distillation (MD) is a relatively new separation process which is being investigated worldwide as a low cost, energy saving alternative to other conventional separation processes. The major aim of this proposal is that the bioethanol produced from fermentation via the membrane distillation system through the expanded polytetrafluoroethylene (ePTFE) membranes. Hopefully, a high flux of MD membrane and ethanol separated from the reaction mixtures can be obtained in this program. We aim to concentrate and purify ethanol through the membranes from simulate fermentation system, and establish a continuous MD system for separate and purify bioethanol from fermentor.
Moreover in the energy conservation, this research discusses the effect of little temperature difference. In addition, the effects of temperature and pressure gradient of the MD system and the air-gap distance on the ethanol purify performance will be investigated.
Keywords: ePTFE, Membrane distillation, fermentation.
|
author2 |
Cheng-Lee Lai |
author_facet |
Cheng-Lee Lai Ming-Chao Yu 游銘昭 |
author |
Ming-Chao Yu 游銘昭 |
spellingShingle |
Ming-Chao Yu 游銘昭 Study on membrane distillation in continuous fermentation system |
author_sort |
Ming-Chao Yu |
title |
Study on membrane distillation in continuous fermentation system |
title_short |
Study on membrane distillation in continuous fermentation system |
title_full |
Study on membrane distillation in continuous fermentation system |
title_fullStr |
Study on membrane distillation in continuous fermentation system |
title_full_unstemmed |
Study on membrane distillation in continuous fermentation system |
title_sort |
study on membrane distillation in continuous fermentation system |
publishDate |
2010 |
url |
http://ndltd.ncl.edu.tw/handle/02717025337623432508 |
work_keys_str_mv |
AT mingchaoyu studyonmembranedistillationincontinuousfermentationsystem AT yóumíngzhāo studyonmembranedistillationincontinuousfermentationsystem AT mingchaoyu báomózhēngliùyīngyòngyúliánxùfājiàoxìtǒngzhīyánjiū AT yóumíngzhāo báomózhēngliùyīngyòngyúliánxùfājiàoxìtǒngzhīyánjiū |
_version_ |
1718040111702081536 |