Supercritical Co-gasification of T-4-hydroxycinnamic Acid and Ethanol
碩士 === 義守大學 === 生物技術與化學工程研究所 === 102 === Lignin is an important component of the plant, about 30%. It is a polymer with phenol-like structure. In this study, cinnamic acid was used as a model compound and gasified in supercritical ethanol to produce fuel gases. Experiments were conducted with...
Main Authors: | , |
---|---|
Other Authors: | |
Format: | Others |
Language: | zh-TW |
Published: |
2014
|
Online Access: | http://ndltd.ncl.edu.tw/handle/5c2387 |
id |
ndltd-TW-102ISU00108009 |
---|---|
record_format |
oai_dc |
spelling |
ndltd-TW-102ISU001080092019-05-15T21:03:46Z http://ndltd.ncl.edu.tw/handle/5c2387 Supercritical Co-gasification of T-4-hydroxycinnamic Acid and Ethanol 肉桂酸與乙醇之超臨界共氣化 Lin wei-Ling 林維玲 碩士 義守大學 生物技術與化學工程研究所 102 Lignin is an important component of the plant, about 30%. It is a polymer with phenol-like structure. In this study, cinnamic acid was used as a model compound and gasified in supercritical ethanol to produce fuel gases. Experiments were conducted with a small batch-type autoclave. The major operating parameters investigated include: the reaction temperature from 400 to 600 °C, the reaction pressure from 50 to 250 bar, and the concentration of cinnamic acid in the feed from 0.25 to 1.0 M. Gaseous products from the reaction were collected and analyzed. The gaseous output consists mainly of H2, CO, CH4 and CO2 as well as small amount of C2H6. It is found that gasification at 50 bar and the feed concentration of 0.25 M, has the highest methane yield. At temperatures below 450 °C, higher feed concentration lowers methane and carbon monoxide production, and increases carbon dioxide output. Chern Shyh-Ming 陳世明 2014 學位論文 ; thesis 108 zh-TW |
collection |
NDLTD |
language |
zh-TW |
format |
Others
|
sources |
NDLTD |
description |
碩士 === 義守大學 === 生物技術與化學工程研究所 === 102 === Lignin is an important component of the plant, about 30%. It is a polymer with phenol-like structure. In this study, cinnamic acid was used as a model compound and gasified in supercritical ethanol to produce fuel gases.
Experiments were conducted with a small batch-type autoclave. The major operating parameters investigated include: the reaction temperature from 400 to 600 °C, the reaction pressure from 50 to 250 bar, and the concentration of cinnamic acid in the feed from 0.25 to 1.0 M. Gaseous products from the reaction were collected and analyzed. The gaseous output consists mainly of H2, CO, CH4 and CO2 as well as small amount of C2H6. It is found that gasification at 50 bar and the feed concentration of 0.25 M, has the highest methane yield. At temperatures below 450 °C, higher feed concentration lowers methane and carbon monoxide production, and increases carbon dioxide output.
|
author2 |
Chern Shyh-Ming |
author_facet |
Chern Shyh-Ming Lin wei-Ling 林維玲 |
author |
Lin wei-Ling 林維玲 |
spellingShingle |
Lin wei-Ling 林維玲 Supercritical Co-gasification of T-4-hydroxycinnamic Acid and Ethanol |
author_sort |
Lin wei-Ling |
title |
Supercritical Co-gasification of T-4-hydroxycinnamic Acid and Ethanol |
title_short |
Supercritical Co-gasification of T-4-hydroxycinnamic Acid and Ethanol |
title_full |
Supercritical Co-gasification of T-4-hydroxycinnamic Acid and Ethanol |
title_fullStr |
Supercritical Co-gasification of T-4-hydroxycinnamic Acid and Ethanol |
title_full_unstemmed |
Supercritical Co-gasification of T-4-hydroxycinnamic Acid and Ethanol |
title_sort |
supercritical co-gasification of t-4-hydroxycinnamic acid and ethanol |
publishDate |
2014 |
url |
http://ndltd.ncl.edu.tw/handle/5c2387 |
work_keys_str_mv |
AT linweiling supercriticalcogasificationoft4hydroxycinnamicacidandethanol AT línwéilíng supercriticalcogasificationoft4hydroxycinnamicacidandethanol AT linweiling ròuguìsuānyǔyǐchúnzhīchāolínjiègòngqìhuà AT línwéilíng ròuguìsuānyǔyǐchúnzhīchāolínjiègòngqìhuà |
_version_ |
1719110039913889792 |