Journal
JOURNAL OF THE JAPAN PETROLEUM INSTITUTE
Volume 63, Issue 4, Pages 196-203Publisher
JAPAN PETROLEUM INST
DOI: 10.1627/jpi.63.196
Keywords
Bioethanol; Acetic acid; Supercritical ethanol; Esterification; Catalytic hydrogenolysis
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Funding
- Advanced Low Carbon Technology Research and Development Program (ALCA), Japan Science and Technology Agency: JST [FYs 2011-18]
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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.
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