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公开(公告)号:ZA201400863B
公开(公告)日:2015-12-23
申请号:ZA201400863
申请日:2014-02-05
Applicant: BASF SE
Inventor: PACIELLO ROCCO , FRIES DONATA MARIA , SCHÄFER MARTIN , SCHAUB THOMAS , RITTINGER STEFAN , BASSLER PETER
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公开(公告)号:ES2554328T3
公开(公告)日:2015-12-18
申请号:ES07712307
申请日:2007-02-23
Applicant: BASF SE
Inventor: MAAS STEFFEN , JOHANN THORSTEN , KOCH MICHAEL , SIRCH TILMAN , SCHLITTER STEPHAN , RITTINGER STEFAN , STEINIGER MICHAEL
IPC: C07C29/141 , C07C31/20
Abstract: Proceso para la hidrogenación catalítica de metilolalcanales de la fórmula general**Fórmula** en la cual R1 y R2 significan, independientemente entre sí, otro grupo metilol o un grupo alquilo con 1 a 22 átomos de C, o un grupo arilo o aralquilo con 6 a 33 átomos de, en la fase líquida en un catalizador de hidrogenación, caracterizado porque adicionando al menos una amina terciaria, una base inorgánica o un ácido inorgánico u orgánico al afluente de hidrogenación se ajusta un valor de pH de 7,0 a 9,0 en el efluente de hidrogenación.
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公开(公告)号:PL2655310T3
公开(公告)日:2015-05-29
申请号:PL11801704
申请日:2011-12-15
Applicant: BASF SE
Inventor: SCHAUB THOMAS , FRIES DONATA MARIA , PACIELLO ROCCO , MOHL KLAUS-DIETER , SCHÄFER MARTIN , RITTINGER STEFAN , DECKERT PETRA , BASSLER PETER
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公开(公告)号:CA2891452A1
公开(公告)日:2014-05-30
申请号:CA2891452
申请日:2013-11-26
Applicant: BASF SE
Inventor: SCHNEIDER DANIEL , MOHL KLAUS-DIETER , SCHAFER MARTIN , PASCHOLD JURGEN , TELES JOAQUIM HENRIQUE , RITTINGER STEFAN
Abstract: The invention relates to a method for producing methyl formate by carbonylating methanol with carbon monoxide in a carbonylation reactor in the presence of a catalyst system containing alkali formate and alkali alcoholate, thereby obtaining a reaction mixture (RG) which contains methyl formate, alkali formate, alkali alcoholate and optionally unreacted methanol and unreacted carbon monoxide and which is removed from the carbonylation reactor. The reaction mixture (RG) contains at least 0.5 wt.% alkali alcoholate, based on the total weight of the reaction mixture (RG), and the molar ratio of alkali formate to alkali alcoholate in the reaction mixture (RG) is greater than 1.
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公开(公告)号:CA2859128A1
公开(公告)日:2013-06-27
申请号:CA2859128
申请日:2012-11-29
Applicant: BASF SE
Inventor: BASSLER PETER , RITTINGER STEFAN , SCHNEIDER DANIEL , FRIES DONATA MARIA , MOHL KLAUS-DIETER , TELES JOAQUIM HENRIQUE , SCHAFER MARTIN , PASCHOLD JURGEN
Abstract: Process for obtaining formic acid by thermal separation of a stream comprising formic acid and a tertiary amine (I), in which a liquid stream comprising formic acid and tertiary amine (I) is produced by combining tertiary amine (I) and a formic acid source, secondary components comprised therein are separated off, formic acid is removed by distillation from the resulting liquid stream in a distillation apparatus, where the bottom output from the distillation apparatus is separated into two liquid phases, and the upper liquid phase is recirculated to the formic acid source and the lower liquid phase is recirculated to the separation of the secondary components and/or to the distillation apparatus, wherein low boilers are removed by distillation from the upper liquid phase and recirculated to the depleted stream.
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公开(公告)号:ZA201201783B
公开(公告)日:2013-05-29
申请号:ZA201201783
申请日:2012-03-12
Applicant: BASF SE
Inventor: SCHAUB THOMAS , FRIES DONATA MARIA , PACIELLO ROCCO , MOHL KLAUS-DIETER , SCHAFER MARTIN , RITTINGER STEFAN , SCHNEIDER DANIEL
IPC: C07C20060101
Abstract: A process is proposed for preparing formic acid by reaction of carbon dioxide (1) with hydrogen (2) in a hydrogenation reactor (I) in the presence of a catalyst containing an element from group 8, 9 or 10 of the Periodic Table, of a tertiary amine containing at least 12 carbon atoms per molecule, and of a polar solvent comprising one or more monoalcohols selected from methanol, ethanol, propanols and butanols, and water, to form formic acid/amine adducts as intermediates, which are subsequently cleaved thermally, with workup of the outputs (3) from the hydrogenation reactor (I) in several process steps, a stream (13) comprising tertiary amine from the workup being used as a selective solvent for the catalyst.
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公开(公告)号:ES2398853T3
公开(公告)日:2013-03-22
申请号:ES08709204
申请日:2008-02-25
Applicant: BASF SE
Inventor: SIRCH TILMAN , STEININGER MICHAEL , MAAS STEFFEN , RITTINGER STEFAN , SCHLITTER STEPHAN
IPC: C07C29/141 , C07C45/75 , C07C45/82 , C07C47/19
Abstract: Procedimiento para la obtención de aldehído hidroxipivalínico mediante aldolización de aldehído isobutírico conformaldehído y subsiguiente elaboración por destilación de la descarga de reacción obtenida, caracterizado porquela descarga de reacción se alimenta a una columna de destilación, que se acciona a una presión de cabeza en elintervalo de 0,5 a 1,5 bar, y en la que está prevista, en la zona de cabeza, una condensación de dos etapas en laque los vapores se conducen en primer lugar a un condensador parcial accionado a una temperatura en el intervalode 50 a 80ºC, cuyo condensado se devuelve al menso parcialmente a la columna de destilación, y en la que losvapores no condensados en el condensador parcial se alimentan a un condensador post-conectado, accionado auna temperatura en el intervalo de -40 a +30ºC, cuyo condensado se esclusa al menos parcialmente.
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公开(公告)号:MX2009009273A
公开(公告)日:2009-09-09
申请号:MX2009009273
申请日:2008-02-25
Applicant: BASF SE
Inventor: MAAS STEFFEN , SIRCH TILMAN , RITTINGER STEFAN , SCHLITTER STEPHAN , STEININGER MICHAEL
IPC: C07C29/141 , C07C45/75 , C07C45/82 , C07C47/19
Abstract: La invención se relaciona con hidroxipivalinaldehído, que se produce mediante la aldolización de isobutiraldehído con formaldehído y procesandmiento subsecuente del producto de reacción mediante destilación, en donde el producto de reacción se alimenta a una columna de destilación, que se opera a una presión superior que varía entre 0.5 y 1.5 bar y en la que se proporciona un proceso de condensación de dos etapas en la región superior. En este proceso, los vapores primero se alimentan a un condensador parcial operado a una temperatura que varía entre 50 y 80ºC, el condensado del cual se regresa cuando menos parcialmente a la columna de destilación, y los vapores que no se condensan en el condensador parcial se alimentan a un condensador de corriente abajo operado a una temperatura que varía entre -40º y +30ºC, el condensado del cual se descarga cuando menos parcialmente.
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公开(公告)号:MY165581A
公开(公告)日:2018-04-05
申请号:MYPI20083289
申请日:2008-08-26
Applicant: BASF SE
Inventor: STEINIGER MICHAEL , MAAS STEFFEN , JOHANN THORSTEN , KOCH MICHAEL , SIRCH TILMAN , SCHLITTER STEPHAN , RITTINGER STEFAN
IPC: C07C31/20 , C07C29/141 , C07C47/02
Abstract: 1 3 PROCESS FOR HYDROGENATING METHYLOLALKANALS ABSTRACT A PROCESS FOR CATALYTICALLY HYDROGENATING METHYLOIALKANALS OF THE GENERAL FORMULA R I OHCHF-C-CHO 1 2 R IN WHICH R1 AND R2 ARE EACH INDEPENDENTLY A FURTHER METHYLOL GROUP OR AN ALKYL GROUP HAVING FROM I TO 22 CARBON ATOMS OR AN ARYL OR ARALKYL GROUP HAVING FROM 6 TO 33 CARBON ATOMS, IN THE LIQUID PHASE OVER A HYDROGENATION CATALYST, WHICH COMPRISES SETTING A PH OF FROM 7.0 TO 9.0 IN THE HYDROGENATION EFFLUENT BY ADDING AT LEAST ONE TERTIARY AMINE, AN INORGANIC BASE OR AN INORGANIC OR ORGANIC ACID TO THE HYDROGENATION FEED.
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公开(公告)号:ZA201504591B
公开(公告)日:2017-11-29
申请号:ZA201504591
申请日:2015-06-25
Applicant: BASF SE
Inventor: RITTINGER STEFAN , PASCHOLD JÜRGEN , SCHÄFER MARTIN , MOHL KLAUS-DIETER , SCHNEIDER DANIEL , TELES JOAQUIM HENRIQUE
Abstract: The invention relates to a method for producing methyl formate by carbonylating methanol with carbon monoxide in a carbonylation reactor in the presence of a catalyst system containing alkali formate and alkali alcoholate, thereby obtaining a reaction mixture (RG) which contains methyl formate, alkali formate, alkali alcoholate and optionally unreacted methanol and unreacted carbon monoxide and which is removed from the carbonylation reactor. The reaction mixture (RG) contains at least 0.5 wt.% alkali alcoholate, based on the total weight of the reaction mixture (RG), and the molar ratio of alkali formate to alkali alcoholate in the reaction mixture (RG) is greater than 1.
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