公开(公告)号：DE50313194D1

公开(公告)日：2010-11-25

申请号：DE50313194

申请日：2003-12-13

Applicant: BASF SE

Inventor： SOHN MARTIN ,  STROEFER ECKHARD ,  NEVEJANS FILIP ,  PENZEL ULRICH ,  PALLASCH HANS-JUERGEN ,  LEUTHOLD RENE ,  BRODHAGEN ANDREAS ,  WOELFERT ANDREAS ,  MACKENROTH WOLFGANG ,  MAURER MARKUS

IPC: C07C263/10 ,  C07C265/14

公开(公告)号：PT1761483E

公开(公告)日：2010-11-08

申请号：PT05761527

申请日：2005-06-22

Applicant: BASF SE

Inventor： WOELFERT ANDREAS ,  KNOESCHE CARSTEN ,  DAISS ANDREAS

IPC: C07C263/10 ,  C07C265/14

公开(公告)号：DE50214172D1

公开(公告)日：2010-03-04

申请号：DE50214172

申请日：2002-11-19

Applicant: BASF SE

Inventor： WOELFERT ANDREAS ,  MUELLER CHRISTIAN ,  STROEFER ECKHARD ,  PFEFFINGER JOACHIM ,  WEBER MARKUS ,  KNOESCHE CARSTEN

IPC: C07C263/10 ,  B01J12/00 ,  C07C265/14

Abstract: The invention relates to a method for producing isocyanates by reacting primary amines with phosgene in the gaseous phase. Said method is characterized in that the reaction of amine and phosgene occurs in a reaction channel, the internal dimensions of which have a width/height ratio of at least 2/1.

公开(公告)号：AT455094T

公开(公告)日：2010-01-15

申请号：AT02795066

申请日：2002-11-19

Applicant: BASF SE

Inventor： WOELFERT ANDREAS ,  MUELLER CHRISTIAN ,  STROEFER ECKHARD ,  PFEFFINGER JOACHIM ,  WEBER MARKUS ,  KNOESCHE CARSTEN

IPC: C07C263/10 ,  B01J12/00 ,  C07C265/14

Abstract: The invention relates to a method for producing isocyanates by reacting primary amines with phosgene in the gaseous phase. Said method is characterized in that the reaction of amine and phosgene occurs in a reaction channel, the internal dimensions of which have a width/height ratio of at least 2/1.

公开(公告)号：AT448859T

公开(公告)日：2009-12-15

申请号：AT05779042

申请日：2005-09-10

Applicant: BASF SE

Inventor： WOELFERT ANDREAS ,  KNOESCHE CARSTEN ,  PALLASCH HANS-JUERGEN ,  SESING MARTIN ,  STROEFER ECKHARD ,  POLKA HANS-MARTIN ,  HEILIG MANFRED

IPC: B01D53/14 ,  C01B7/07 ,  C01B32/80

Abstract: The invention relates to a process for separating hydrogen chloride and phosgene, which comprises bringing a mixture of hydrogen chloride and phosgene into contact with an ionic liquid in which at least part of the hydrogen chloride is dissolved in a step a) and then separating off the hydrogen chloride dissolved in the ionic liquid in a step b).

公开(公告)号：DE502004010159D1

公开(公告)日：2009-11-12

申请号：DE502004010159

申请日：2004-02-20

Applicant: BASF SE

Inventor： BRODHAGEN ANDREAS ,  SOHN MARTIN ,  NEVEJANS FILIP ,  STROEFER ECKHARD ,  WOELFERT ANDREAS ,  OEHLENSCHLAEGER STEFFEN

IPC: C07C263/10 ,  B01J19/24 ,  C07C265/14

Abstract: Production of polyisocyanates comprises mixing an amine with phosgene, reacting the amine with the phosgene in a tubular reactor, and passing the reactor effluent to a distillation column. Independent claims are also included for: (1) tubular reactor consisting of one or more horizontal and/or vertical segments connected together by sections whose diameter is smaller than that of the narrowest horizontal or vertical segment; (2) use of the above reactor for carrying out gas-liquid reactions; and (3) use of the above reactor for producing isocyanates by reacting primary amines with phosgene.

公开(公告)号：DE502005004848D1

公开(公告)日：2008-09-04

申请号：DE502005004848

申请日：2005-12-10

Applicant: BASF SE

Inventor： WAGNER EVA ,  BEY OLIVER ,  WOELFERT ANDREAS ,  JAEHME JOACHIM ,  BRUCHMANN BERND ,  BAYER ALEXANDER

IPC: C08G18/78 ,  C07C273/18

公开(公告)号：AT402211T

公开(公告)日：2008-08-15

申请号：AT05825088

申请日：2005-12-10

Applicant: BASF SE

Inventor： WAGNER EVA ,  BEY OLIVER ,  WOELFERT ANDREAS ,  JAEHME JOACHIM ,  BRUCHMANN BERND ,  BAYER ALEXANDER

IPC: C08G18/78 ,  C07C273/18

公开(公告)号：CA2674734A1

公开(公告)日：2008-07-24

申请号：CA2674734

申请日：2008-01-14

Applicant: BASF SE

Inventor： DRIESS HEINZ ,  JACHOW HARALD ,  WOELFERT ANDREAS

IPC: B01J8/04 ,  B01J8/06 ,  B01J23/22 ,  B01J23/24 ,  B01J23/28 ,  B01J23/30 ,  B01J23/75 ,  B01J23/755 ,  B01J27/04 ,  B01J27/043 ,  B01J27/047 ,  C01B17/02 ,  C01B17/16

Abstract: The invention relates to a method and a device for producing hydrogen sul fide H2S by the reaction on a fixed catalyst of a reactant mixture containin g gaseous sulfur and hydrogen. The reactant mixture is reacted in a reactor (1) at an absolute pressure from 0.5 bar to 10 bar, a temperature from 300°C to 450°C, and an excess of sulfur. The sulfur excess corresponds to a ratio of excess sulfur to produced H2S of 0.2 kg to 3 kg sulfur per kg of produce d H2S.