-
公开(公告)号:PL2200976T3
公开(公告)日:2012-04-30
申请号:PL08804005
申请日:2008-09-11
Applicant: BASF SE
Inventor: KNÖSCHE CARSTEN , WÖLFERT ANDREAS , MATTKE TORSTEN , STROEFER ECKHARD , BLANKERTZ HEINRICH-JOSEF , GEISSLER BERNHARD
IPC: C07C263/10
-
公开(公告)号:AT516282T
公开(公告)日:2011-07-15
申请号:AT08804546
申请日:2008-09-22
Applicant: BASF SE
Inventor: SIEGERT MARKUS , LANG NEVEN , SZARVAS LASZLO , SIGWART CHRISTOPH , WINDLIN FRANZ NIKLAUS , STROEFER ECKHARD
IPC: C07D323/06 , B01D3/14
Abstract: A process for separating trioxane from a feed stream I comprising formaldehyde, trioxane and water, in which a) a feed stream I comprising formaldehyde as main component and trioxane and water as secondary components is provided, b) the feed stream I, a recycle stream V and a recycle stream VII comprising formaldehyde as main component and water and trioxane as secondary components are fed into a first distillation stage and distilled at a pressure of from 0.1 to 2.5 bar to give a stream II comprising formaldehyde as main component and water as secondary component and a stream III comprising trioxane as main component and water and formaldehyde as secondary components and a stream X comprising water, trioxane and formaldehyde, c) the stream III is, if appropriate after removal of low boilers from the stream III in a low boiler removal stage, distilled in a second distillation stage at a pressure of from 0.2 to 17.5 bar, with the pressure in the second distillation stage being from 0.1 to 15 bar higher than the pressure in the first distillation stage, to give a stream IV consisting essentially of trioxane and the recycle stream V comprising trioxane as main component and water and formaldehyde as secondary components, c1) the stream IV is purified in at least one further trioxane distillation stage at a pressure at the top of from 0.5 to 2 bar to give purified trioxane as side offtake stream XII in the enrichment section of the column, d) the stream X and, if appropriate, a stream IX comprising water as main component are fed into a third distillation stage and distilled at a pressure of from 1 to 10 bar to give a stream VI consisting essentially of water and a recycle stream VII comprising formaldehyde as main component and water and trioxane as secondary components, is described.
-
公开(公告)号:AT512130T
公开(公告)日:2011-06-15
申请号:AT07703734
申请日:2007-01-09
Applicant: BASF SE
Inventor: KLOETZER MATTHIAS , STROEFER ECKHARD , BLANKERTZ HEINRICH-JOSEF
IPC: C07C263/06 , C07C265/14
-
公开(公告)号:PT1581457E
公开(公告)日:2011-04-29
申请号:PT03789225
申请日:2003-12-11
Applicant: BASF SE
Inventor: OLBERT GERHARD , WALSDORFF CHRISTIAN , FIENE MARTIN , STROEFER ECKHARD , HARTH KLAUS
-
公开(公告)号:ES2353960T3
公开(公告)日:2011-03-08
申请号:ES03784115
申请日:2003-07-30
Applicant: BASF SE
Inventor: WALSDORFF CHRISTIAN , STROEFER ECKHARD , DEBERDT FILIP , FIENE MARTIN , JACOBS JAN , HARTH KLAUS;
IPC: C07C263/10 , B01J23/46 , C01B7/04 , C07C263/20 , C25B1/26
Abstract: Procedimiento para producir isocianatos orgánicos con los pasos (a) aportación de una primera cantidad parcial de cloro, en donde el cloro de la primera cantidad parcial presenta un contenido de bromo y yodo libre o enlazado
-
公开(公告)号:ES2353005T3
公开(公告)日:2011-02-24
申请号:ES03789262
申请日:2003-12-13
Applicant: BASF SE
Inventor: STROEFER ECKHARD , LEUTHOLD RENE , MAURER MARKUS , SOHN MARTIN , PALLASCH HANS-JURGEN , MACKENROTH WOLFGANG , BRODHAGEN ANDREAS , WOLFERT ANDREAS , NEVEJANS FILIP , PENZEL ULRICH
IPC: C07C263/10 , C07C265/14
Abstract: Método para la producción de poliisocianatos mediante reacción de aminas orgánicas con fosgeno, caracterizado porque la reacción se efectúa en al menos tres etapas, en cuyo caso la primera etapa se realiza en un dispositivo de mezcla, la segunda etapa en al menos un aparato de tiempo de residencia y la tercera etapa en una o varias columnas (de reacción y la presión es más baja en cada una de las etapas siguientes que en la etapa previa.
-
公开(公告)号:AT489376T
公开(公告)日:2010-12-15
申请号:AT06793286
申请日:2006-09-06
Applicant: BASF SE
Inventor: SIEGERT MARKUS , LANG NEVEN , STROEFER ECKHARD , STAMMER ACHIM
IPC: C07D317/12
Abstract: Processes comprising: providing a reactive distillation column having an upper region, a middle region and a lower region; feeding ethylene glycol and an aqueous formaldehyde solution into the reactive distillation column in the middle region of the reactive distillation column; reacting the ethylene glycol and the aqueous formaldehyde solution in the reactive distillation column in the presence of a catalyst to form dioxolane; removing a product stream comprising dioxolane in an amount of at least 75% by weight from the upper region of the reactive distillation column; and removing a bottom stream comprising one or more components having boiling points higher than dioxolane from the lower region of the reactive distillation column.
-
公开(公告)号:SG166091A1
公开(公告)日:2010-11-29
申请号:SG2010064228
申请日:2006-08-23
Applicant: BASF SE
Inventor: WOELFERT ANDREAS , KNOESCHE CARSTEN , DAISS ANDREAS , CHENG TSUNG-CHIEH , MATTKE TORSTEN , STROEFER ECKHARD
Abstract: The present invention relates to a process for preparing isocyanates and an apparatus suitable for this purpose, and also its use.
-
公开(公告)号:DE502004011738D1
公开(公告)日:2010-11-18
申请号:DE502004011738
申请日:2004-03-03
Applicant: BASF SE
Inventor: STROEFER ECKHARD , LANG NEVEN , STEINBRENNER ULRICH , HASSE HANS , OTT MICHAEL , GRUETZNER THOMAS
IPC: C07C45/83 , C07C45/00 , C07C45/82 , C07C47/04 , C07C47/058
-
公开(公告)号:AT483676T
公开(公告)日:2010-10-15
申请号:AT04716587
申请日:2004-03-03
Applicant: BASF SE
Inventor: STROEFER ECKHARD , LANG NEVEN , STEINBRENNER ULRICH , HASSE HANS , OTT MICHAEL , GRUETZNER THOMAS
IPC: C07C45/83 , C07C45/00 , C07C45/82 , C07C47/04 , C07C47/058
Abstract: Process for preparing high-concentration gaseous formaldehyde having a molar CH 2 O:H 2 O ratio of >=0.6 from an aqueous formaldehyde solution by evaporation of at least part of the solution, in which the aqueous formaldehyde solution is heated to a vaporization temperature T and the gas phase formed is taken off, wherein the evaporation temperature T obeys the relationship: T[° C.]>=T' min [° C.] where T' min (c)=A+Bx(c/100)+Cx(c/100) 2 +Dx(c/100) 3 and A=+68.759, B=+124.77, C=-12.851, D=-10.095, where c is the instantaneous CH 2 O content of the aqueous formaldehyde solution during the evaporation in percent by weight and is from 20 to 99% by weight.
-
-
-
-
-
-
-
-
-