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公开(公告)号:BR112014031094A2
公开(公告)日:2017-06-27
申请号:BR112014031094
申请日:2013-06-26
Applicant: BASF SE
Inventor: ALEXANDER WECK , EKKEHARD SCHWAB , FLORINA CORINA PATCAS , KEREM BAY , KIRSTEN SPANNHOFF , MATTHIAS MIELKE , OLIVER SEEL
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公开(公告)号:BR112014031094A8
公开(公告)日:2021-01-26
申请号:BR112014031094
申请日:2013-06-26
Applicant: BASF SE
Inventor: ALEXANDER WECK , EKKEHARD SCHWAB , FLORINA CORINA PATCAS , KEREM BAY , KIRSTEN SPANNHOFF , MATTHIAS MIELKE , OLIVER SEEL
Abstract: catalisador para conversão de oxigenados em olefinas, processo para a sua preparação e usos relacionados. a presente invenção se refere a um catalisador para a conversão de oxigenados em olefinas, compreendendo - um substrato de suporte e - uma camada aplicada ao substrato, em que a camada compreende um ou mais zeólitos do tipo de estrutura mfi, mel e/ou mww, o um ou mais zeólitos compreendendo um ou mais metais alcalino-terrosos para a preparação e uso dos mesmos, e a um processo para converter oxigenados em olefinas usando o catalisador.
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公开(公告)号:BR112014031392A2
公开(公告)日:2017-06-27
申请号:BR112014031392
申请日:2013-06-26
Applicant: BASF SE
Inventor: ALEXANDER WECK , EKKEHARD SCHWAB , FLORINA CORINA PATCAS , KEREM BAY , KIRSTEN SPANNHOFF
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公开(公告)号:MY151991A
公开(公告)日:2014-07-31
申请号:MYPI20104302
申请日:2009-03-23
Applicant: BASF SE
Inventor: GUNTHER WINDECKER , JENS WEIGUNY , ALEXANDER WECK , ELLEN DAHLHOFF , WOLF-STEFFEN WEISSKER , JÖRG HEILEK , THOMAS KRUG , RALF FREYBERGER
IPC: C07D307/36
Abstract: PROCESSES FOR DECREASING FUMARIC ACID DEPOSITS IN PREPARING MALEIC ANHYDRIDE BY HETEROGENEOUSLY CATALYZED OXIDATION OF A HYDROCARBON WITH MOLECULAR OXYGEN. MALEIC ANHYDRIDE IS ABSORBED FROM THE CRUDE MIXTURE IN AN ABSORBENT IN AN ABSORPTION COLUMN AND DESORBED IN A DESORPTION COLUMN, THE ENTIRETY OR PORTION OF ABSORBENT DEPLETED IN MALEIC ANHYDRIDE, FOR CONTROLLED PRECIPITATION OF FUMARIC ACID, BEING COOLED AND/OR CONCENTRATED BY EVAPORATING A PORTION OF ABSORBENT SUCH THAT THE DIFFERENCE BETWEEN THE CONCENTRATION OF FUMARIC ACID IN THE RECYCLE STREAM AT THE OUTLET OF THE DESORPTION COLUMN UNDER EXISTING CONDITIONS AND THE EQUILIBRIUM CONCENTRATION OF FUMARIC ACID ACCORDING TO THE SOLUBILITY CURVE AFTER COOLING AND/OR EVAPORATION OF A PORTION OF ABSORBENT IS ?25O PPM BY WEIGHT, AND THE FUMARIC ACID PRECIPITATED AS A SOLID IS REMOVED COMPLETELY OR PARTLY FROM THE ABSORBENT RECYCLING SYSTEM AND THE FUMARIC ACID-DEPLETED ABSORBENT IS RECYCLED COMPLETELY OR PARTLY TO THE ABSORPTION COLUMN. (FIGURE 1)
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