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公开(公告)号:US20220332587A1
公开(公告)日:2022-10-20
申请号:US17612237
申请日:2020-04-20
Applicant: BASF SE
Inventor: Gerhard OLBERT , Jens FERBITZ , Kai THIELE , Peter VAN DEN ABEEL , Koenraad VANDEWALLE , Jim BRANDTS , Torsten MATTKE
Abstract: The invention relates to a process for producing phosgene by gas-phase reaction of carbon monoxide and chlorine in the presence of a catalyst in a reactor which comprises a plurality of parallel catalyst tubes which are filled with the catalyst and around which at least one fluid heat transfer medium flows, where a feed stream of a mixture of a chlorine input stream and a carbon monoxide input stream is fed into the catalyst tubes and is allowed to react to give a phosgene-comprising product gas mixture, wherein the reaction is carried out at an area load of more than 2.75 kg of phosgene/m2s. The invention also provides a reactor for carrying out the process.
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公开(公告)号:US20220212936A1
公开(公告)日:2022-07-07
申请号:US17605737
申请日:2020-04-14
Applicant: BASF SE
Inventor: Torsten MATTKE , Gerhard OLBERT , Jochen GAUER , Kai THIELE , Koenraad VANDEWALLE , Jens FERBITZ , Peter VAN DEN ABEEL
Abstract: The present invention relates to a process for preparing phosgene by reacting chlorine with carbon monoxide over an activated carbon catalyst, wherein the content of chlorine oxides in the chlorine feed stream is low, to an apparatus for preparation of phosgene and to the use of the phosgene prepared by the process of the invention.
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公开(公告)号:US20180044179A1
公开(公告)日:2018-02-15
申请号:US15557187
申请日:2016-03-10
Applicant: BASF SE
Inventor: Heiner SCHELLING , Torsten MATTKE , Hans-Juergen PALLASCH , Kai THIELE
IPC: C01B7/07 , C01B32/80 , C07C263/10 , B01D53/00
CPC classification number: C01B7/0731 , B01D53/002 , B01D2257/2045 , C01B7/0712 , C01B32/80 , C07C263/10 , C07C263/20 , F25J3/00
Abstract: The invention relates to a method of separating a phosgene- and hydrogen chloride-comprising stream (5), wherein said method comprises conveying the hydrogen chloride- and phosgene-comprising stream (5) into a distillation column (1), withdrawing at the bottom of the distillation column (1) a phosgene-comprising stream (7) and withdrawing at the top of the column an essentially hydrogen chloride-comprising stream (9). At least a portion of the stream (9) withdrawn at the top is compressed and at least partially condensed and at least a portion of the liquid and compressed essentially hydrogen chloride-comprising stream is decompressed and recycled into the top of distillation column (1) as reflux.
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