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公开(公告)号:US20240300817A1
公开(公告)日:2024-09-12
申请号:US18277415
申请日:2022-02-10
Applicant: BASF SE
Inventor: Torsten MATTKE , Kai THIELE , Jens FERBITZ , Peter VAN DEN ABEEL , Hans-Juergen PALLASCH
IPC: C01B7/07 , B01D53/00 , C01B32/80 , C07C263/20
CPC classification number: C01B7/0712 , B01D53/002 , C01B7/0731 , C01B32/80 , C07C263/20 , B01D2256/26 , B01D2257/2064
Abstract: A process of separating phosgene and hydrogen chloride, comprises: conveying a mixed stream containing hydrogen chloride and phosgene into a distillation column; withdrawing from the distillation column a bottom stream containing phosgene; withdrawing a top stream containing hydrogen chloride; compressing at least a portion of the top stream and at least partially condensing the compressed top stream to form a liquid stream, decompressing at least a portion of the liquid stream to form a cooled liquid stream and a cooled gas stream; and recycling the cooled liquid stream to the top of the distillation column as a reflux; the process additionally comprising temporarily introducing an absorbing solvent into the distillation column, in particular during starting-up and/or shutting-down of the process. The process allows for safe operation even when hydrogen chloride production only gradually begins or decreases, without the necessity of storing hydrogen chloride.
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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 At least a portion of the stream (9) withdrawn at the top is compressed and at least partially condensed and at least a portion of the liquid and compressed essentially hydrogen chloride-comprising stream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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