Two-step Conversion of Acetic Acid to Bioethanol by Ethyl Esterification and Catalytic Hydrogenolysis

被引:4
作者
Phaiboonsilpa, Natthanon [1 ]
Kawamoto, Haruo [1 ]
Minami, Eiji [1 ]
Masuda, Shouzo [1 ]
Wakagi, Ryota [1 ]
Sunayama, Takayuki [1 ]
Saka, Shiro [1 ]
机构
[1] Kyoto Univ, Grad Sch Energy Sci, Sakyo Ku, Yoshida Honmachi, Kyoto 6068501, Japan
基金
日本科学技术振兴机构;
关键词
Bioethanol; Acetic acid; Supercritical ethanol; Esterification; Catalytic hydrogenolysis; METHYL ESTERIFICATION; FATTY ALCOHOLS; RAPESEED OIL; GAS-PHASE; COPPER; HYDROLYSIS; METHANOL; ACETATE; HYDROGENATION; REDUCTION;
D O I
10.1627/jpi.63.196
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
A two-step conversion of acetic acid to ethanol was discussed by ethyl esterification followed by catalytic hydrogenolysis for highly efficient bioethanol production from lignocellulose via acetic acid fermentation. Non-catalytic supercritical ethanol treatment was demonstrated for the esterification of acetic acid, and an appropriate condition was found to be 270 degrees C/20 MPa for ethyl acetate production. Because of the autocatalytic effect of acetic acid, a low ethanol ratio favored a fast reaction rate but diminished the ethyl acetate yield due to the reverse reaction. Therefore, it seems better to employ a water removal method during the esterification reaction for efficient conversion of acetic acid to ethyl acetate with minimal ethanol. For the hydrogenolysis of ethyl acetate, catalytic activities of several Cu-type catalysts were evaluated with a flow-type reactor. The Cu-Zn catalyst was more effective than other Cu-Cr-type ones in the temperature range of 210-270 degrees C, where only small amounts of methane and ethane (0.89 wt% at 270 degrees C upon the fed methyl acetate) were formed as by-products along with ethanol. These findings will help us to design an efficient bioethanol production process from acetic acid by the proposed two-step method.
引用
收藏
页码:196 / 203
页数:8
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