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公开(公告)号:US20200231523A1
公开(公告)日:2020-07-23
申请号:US16647585
申请日:2017-09-29
Inventor: Hongchao LIU , Wenliang ZHU , Zhongmin LIU , Yong LIU , Shiping LIU , Fuli WEN , Youming NI , Xiangang MA
IPC: C07C29/154 , B01J19/18
Abstract: A method for directly producing ethanol from syngas, carried out in three reaction zones, including: feeding a raw material containing syngas and dimethyl ether into a first reaction zone to contact with a solid acid catalyst, reacting; allowing the effluent from the first reaction zone to enter a second reaction zone to contact with a metal catalyst and react; separating the effluent from the second reaction zone to obtain product ethanol and by-product methanol; allowing by-product methanol to enter a third reaction zone to perform a dehydration reaction to obtain dimethyl ether, and allowing the obtained dimethyl ether to enter the first reaction zone to recycle the reaction. This provides a novel method for directly converting syngas to ethanol and an ethanol product can be directly produced by using syngas as a raw material.
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公开(公告)号:US20200239401A1
公开(公告)日:2020-07-30
申请号:US16647174
申请日:2017-09-29
Inventor: Hongchao LIU , Wenliang ZHU , Zhongmin LIU , Yong LIU , Shiping LIU , Fuli WEN , Youming NI , Xiangang MA
IPC: C07C67/36 , C07C51/10 , B01J8/04 , B01J8/06 , B01J23/889 , B01J23/00 , B01J29/40 , B01J29/18 , B01J29/70
Abstract: A method for directly producing methyl acetate and/or acetic acid from syngas, carried out in at least two reaction zones, including: feeding a raw material containing syngas into a first reaction zone to contact and react with a metal catalyst; allowing an obtained effluent to enter a second reaction zone directly or after the addition of carbon monoxide so as to contact and react with a solid acid catalyst; separating the obtained effluent to obtain product of acetate and/or acetic acid, and optionally returning a residual part to enter the first reaction zone and/or the second reaction zone to recycle the reaction. This provides a novel method for directly converting syngas into methyl acetate and/or acetic acid. Further, the product selectivity of the product of methyl acetate or acetic acid is greater than 93%, and the quantity of methyl acetate and acetic acid may be adjusted according to processing.
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