抄録
A new method for ethanol synthesis from dimethyl ether (DME) and synthesis gas (syngas) via a two-stage reaction system was presented. In the first stage reaction, H-mordenite zeolite catalyst was used to convert DME into methyl acetate (MA) through carbonylation reaction. The MA produced from the first stage reactor was hydrogenated by Cu/ZnO catalyst in the followed second stage reactor to form ethanol and methanol. The conversion of DME kept at a stable value regardless of the different R2 reaction temperatures. The highest MA selectivity of 80.9% and the lowest selectivity of methanol and ethanol at 413 K indicated that most of MA was not converted under this reaction temperature. The selectivity of methanol and ethanol increased when the reaction temperature was increased from 413 to 453 K.
本文言語 | 英語 |
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ページ(範囲) | 357-358 |
ページ数 | 2 |
ジャーナル | Journal of the Japan Petroleum Institute |
巻 | 52 |
号 | 6 |
DOI | |
出版ステータス | 出版済み - 2009 |
ASJC Scopus 主題領域
- 燃料技術
- エネルギー工学および電力技術