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公开(公告)号:JP2003231887A
公开(公告)日:2003-08-19
申请号:JP2002297104
申请日:2002-10-10
Applicant: BASF AG
Inventor: KOCH MICHAEL , SCHWAB EKKEHARD , TRUBENBACH PETER , SCHAFER HARALD
Abstract: PROBLEM TO BE SOLVED: To provide a process for catalytically hydrogenating a hydrocarbon stream by which the fewest possible undesired secondary components such as oligomers and/or polymers and/or cracking products are formed. SOLUTION: The hydrocarbon stream is catalytically hydrogenated by adding a basic compound to the starting material stream without using a different solvent from the hydrocarbon stream to be hydrogenated. Thereby, the formation of undesired secondary components on the catalyst is effectively prevented. COPYRIGHT: (C)2003,JPO
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公开(公告)号:BR9404365A
公开(公告)日:1995-07-04
申请号:BR9404365
申请日:1994-11-07
Applicant: BASF AG
Inventor: TRUBENBACH PETER , MCKEE GRAHAM EDMUND , WOHLFROMM HANS
IPC: C04B35/622 , B22F1/00 , B22F3/10 , B22F3/22 , C04B35/565 , C04B35/634 , C04B35/638 , C08K3/14 , C08K3/22 , C08K3/08 , C08L59/04
Abstract: Process for producing shaped sintered parts containing finely divided carbon by shaping a mixture of a) a ceramic and/or metallic powder and b) polyoxymethylene and/or a copolymer containing a predominant proportion of oxymethylene units to give a green body, removing the binder by treatment with a gaseous acid, pyrolysis and sintering, with there being added to the mixture of a) and b) a thermoplastic c) which, at temperatures of from 90 to 220 DEG C, is molten, miscible with polyoxymethylene and stable and does not undergo a crosslinking reaction with formaldehyde, and also a composition for this process.
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公开(公告)号:AU8989701A
公开(公告)日:2002-04-02
申请号:AU8989701
申请日:2001-09-19
Applicant: BASF AG
Inventor: KAIBEL GERD , OOST CARSTEN , STROEZEL MANFRED , MEYER GERALD , TRUBENBACH PETER , SARTOR KARL-HEINZ , HENERS JURGEN
Abstract: A process is proposed for the separation of C 5+ cuts by distillation into a low-boiler (A), a medium-boiler (B) and a high-boiler fraction (C) in one or more dividing-wall columns (TK), in which a dividing wall (T) is arranged in the longitudinal direction of the column with formation of an upper, common column region ( 1 ), a lower, common column region ( 6 ), a feed part ( 2, 4 ) with rectifying section ( 2 ) and stripping section ( 4 ), and a withdrawal part ( 3, 5 ) with rectifying section ( 5 ) and stripping section ( 3 ), with feed of the C 5+ cut (A, B, C) into the central region of the feed part ( 2, 4 ), discharge of the high-boiler fraction (C) from the bottom of the column, discharge of the low-boiler fraction (A) via the top of the column, and discharge of the medium-boiler fraction (B) from the central region of the withdrawal part ( 3, 5 ), wherein the dividing ratio of the liquid reflux at the upper end of the dividing wall (T) is set in such a way that the proportion of high-boiling key components in the liquid reflux over the stripping section ( 3 ) of the withdrawal part at the upper end of the dividing wall (T) is from 10 to 80%, preferably from 30 to 50%, of the limit value allowed in the medium-boiler fraction (B), and wherein the heating power in the evaporator at the bottom of the dividing-wall column (TK) is set in such a way that the concentration of the low-boiling key components in the liquid at the lower end of the dividing wall (T) is from 10 to 80%, preferably from 30 to 50%, of the limit value allowed in the medium-boiler fraction (B).
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