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公开(公告)号:US20200290884A1
公开(公告)日:2020-09-17
申请号:US16086251
申请日:2017-03-22
Applicant: BASF SE
Inventor: Benedikt KALO , Thomas GEIGER , Rene KOENIG , Ulrich MUELLER , Stefan MAURER
Abstract: A process for the calcination of a zeolitic material, wherein the process contains the steps of (i) providing a zeolitic material containing YO2 and optionally further containing X2O3 in its framework structure in the form of a powder and/or of a suspension of the zeolitic material in a liquid, wherein Y stands for a tetravalent element and X stands for a trivalent element; (ii) atomization of the powder and/or of the suspension of the zeolitic material provided in (i) in a gas stream for obtaining an aerosol; and (iii) calcination of the aerosol obtained in (ii) for obtaining a calcined powder, a zeolitic material obtained by the above process, and its use as a molecular sieve, as an adsorbent for ion-exchange, as a catalyst, and/or as a catalyst support.
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公开(公告)号:US20230101490A1
公开(公告)日:2023-03-30
申请号:US17793668
申请日:2021-01-11
Applicant: BASF SE
Inventor: Maximilian VICARI , Susanne BRITZIUS , Sven REINING , Torsten KATZ , Thomas GEIGER , Gerald MEYER
IPC: C07C29/151 , C07C31/04 , C07C29/154
Abstract: A process for preparing methanol from carbon dioxide and hydrogen in a methanol synthesis unit and working up the reaction mixture obtained stepwise to isolate the methanol, wherein the carbon dioxide, carbon monoxide, dimethyl ether and methane components of value from the streams separated off in the isolation of the methanol from the methanol reaction stream are combusted with an oxygenous gas, and the carbon dioxide in the resultant flue gas is separated off in a carbon dioxide recovery unit and recycled to the methanol synthesis unit.
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公开(公告)号:US20210363007A1
公开(公告)日:2021-11-25
申请号:US17273478
申请日:2019-08-26
Applicant: BASF SE
Inventor: Maximilian VICARI , Thomas GEIGER , Torsten KATZ
IPC: C01B3/38 , C07C29/151 , C07C29/80
Abstract: A process for preparing methanol from a carbon-containing feedstock by producing synthesis gas therefrom in a synthesis gas production unit, converting the synthesis gas to methanol in a methanol synthesis unit and working up the reaction mixture obtained stepwise to isolate the methanol, wherein the carbon monoxide, carbon dioxide, dimethyl ether and methane components of value from the streams separated off in the isolation of the methanol are combusted with an oxygenous gas, and the carbon dioxide in the resultant flue gas is separated off in a carbon dioxide recovery unit and recycled to the synthesis gas production unit and/or to the methanol synthesis unit.
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