-
公开(公告)号:ES2214440T3
公开(公告)日:2004-09-16
申请号:ES01964949
申请日:2001-05-22
Applicant: BASF AG
Inventor: FREUDENTHALER EVA , BRAND ALEXANDRA , STERZEL HANS-JOSEF , ENGELMANN JOCHEN , KLATT MARTIN
IPC: C09K21/10 , C07F9/24 , C08G79/02 , C08K3/00 , C08K5/16 , C08K5/5399 , C08L101/00 , C09K21/12
-
公开(公告)号:DE10126718A1
公开(公告)日:2002-12-05
申请号:DE10126718
申请日:2001-05-31
Applicant: BASF AG
Inventor: BRAND ALEXANDRA , SEITZ CHRISTIAN , ENGELMANN JOCHEN
IPC: C08G18/38 , C08G18/48 , C08K5/5399 , C09K21/12 , C09K21/14 , C08G79/02 , C08G18/54 , C08G69/48 , C08G71/04 , C08L85/02 , C08L61/32 , C08J5/18
Abstract: The invention relates to a method for producing a phosphor-nitrogen condensate, comprising the following steps: i) production of a precondensate by reacting urea with melamine at a temperature of at least 170 DEG C, ii) reaction of the precondensate obtained in step i) with phosphoric acid at a temperature of at least 180 DEG C and use of the condensate as a flameproofing agent in plastics.
-
公开(公告)号:DE10033964A1
公开(公告)日:2002-01-24
申请号:DE10033964
申请日:2000-07-13
Applicant: BASF AG
Inventor: BRAND ALEXANDRA
Abstract: Preparation of trialkoxysilanes by reaction of silicon with an alcohol is catalysed by a copper salt whose anion contains at least one non-hydrolyzable fluorine atom or by a mixture of such a salt with another salt.
-
公开(公告)号:CA2410613A1
公开(公告)日:2001-11-29
申请号:CA2410613
申请日:2001-05-22
Applicant: BASF AG
Inventor: KLATT MARTIN , ENGELMANN JOCHEN , FREUDENTHALER EVA , BRAND ALEXANDRA , STERZEL HANS-JOSEF
IPC: C09K21/10 , C07F9/24 , C08G79/02 , C08K3/00 , C08K5/16 , C08K5/5399 , C08L101/00 , C09K21/12
-
公开(公告)号:DE19947591A1
公开(公告)日:2001-04-12
申请号:DE19947591
申请日:1999-10-04
Applicant: BASF AG
Inventor: BRAND ALEXANDRA , STERZEL HANS-JOSEF
Abstract: Isolation of trimethoxysilane from a TMS/methanol mixture comprises forming and separating a TMS-rich extract phase and a methanol-rich raffinate phase by adding a methanol-soluble (in)organic salt. Isolation of trimethoxysilane (TMS) from a TMS/methanol mixture comprises forming and separating a TMS-rich extract phase and a methanol-rich raffinate phase by adding a methanol-soluble (in)organic salt and optionally nonpolar organic solvents, the amount of salt being such that the wt. ratio of TMS to methanol in the extract phase is at least 94 to 6 wt.%.
-
-
-
-