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公开(公告)号:US09944588B2
公开(公告)日:2018-04-17
申请号:US15526780
申请日:2014-11-17
Inventor: Youming Ni , Wenliang Zhu , Yong Liu , Hongchao Liu , Zhongmin Liu , Lina Li , Shiping Liu , Hui Zhou
IPC: C07C69/00 , C07C69/06 , C07C67/39 , B01D3/14 , B01J29/70 , B01J29/40 , C07C53/02 , C07C43/10 , C07C43/04 , C08F212/36 , C08F212/08
CPC classification number: C07C69/06 , B01D3/14 , B01J29/40 , B01J29/7038 , C07C41/56 , C07C43/043 , C07C43/10 , C07C53/02 , C07C67/39 , C08F212/08 , C08F212/36 , C07C43/30
Abstract: A method for preparing methyl formate in which a raw material containing formaldehyde, methanol and/or dimethyl ether is introduced into a first reaction zone to come into contact with a catalyst A, and a component I is obtained by separation, the component I is introduced into a second reaction zone to come into contact with a catalyst B so as to obtain, by separation, methyl formate as a product, dimethyl ether that is returned to the first reaction zone and a component II that is returned to the second reaction zone, the catalysts have a long service life, the reaction conditions are mild, and the utilization rate of the raw material is high, thus enabling a continuous production for large-scale industrial application.
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公开(公告)号:US09938227B2
公开(公告)日:2018-04-10
申请号:US15526868
申请日:2014-11-17
Inventor: Youming Ni , Wenliang Zhu , Yong Liu , Hongchao Liu , Zhongmin Liu , Lina Li , Shiping Liu , Hui Zhou
IPC: C07C69/00 , C07C67/39 , C07C67/00 , C07C69/06 , C07C41/50 , C07C43/04 , C07C43/30 , B01J39/05 , B01J29/08 , B01J29/18 , B01J29/40 , B01J29/65 , B01J29/70 , B01J31/10 , B01J39/20 , C07C41/18
CPC classification number: C07C67/39 , B01J29/084 , B01J29/18 , B01J29/40 , B01J29/65 , B01J29/7007 , B01J29/7038 , B01J31/10 , B01J39/05 , B01J39/20 , B01J2231/50 , B01J2231/70 , C07C41/18 , C07C41/50 , C07C43/04 , C07C43/30 , C07C67/00 , C07C69/06
Abstract: Method for preparing methyl formate and coproducing dimethyl ether by reacting a formaldehyde and methanol raw material (molar ratio range of 1:4 to 1:0.05) in a First Reaction Region at ranges from 50° C. to 100° C. with Catalyst A resulting in post-reaction material separated into Constituent I. Reacting Constituent I in a Second Reaction Region at ranges from 50° C. to 200° C. and from 0.1 MPa to 10 MPa with Catalyst B resulting in post-reaction material, which is separated into methyl formate, dimethyl ether and Constituent II. At least 1% of dimethyl ether is product, and recycling the rest to the First Reaction Region. Constituent II is recycled to the Second Reaction Region. Each component is gaseous phase and/or liquid phase, independently. The method shows long catalyst life, mild reaction condition, high utilization ratio of raw materials, continuous production and large scale industrial application potential.
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