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公开(公告)号:GR3032014T3
公开(公告)日:2000-03-31
申请号:GR990403108
申请日:1999-11-30
Applicant: BASF AG
Inventor: VICARI MAXIMILIAN , WALTER MARC , SCHWAB EKKEHARD , MUELLER HANS-JOACHIM , KONS GERMAIN , DILLING STEPHAN , POLANEK PETER
IPC: B01J23/755 , C10G45/36 , C10G67/02
Abstract: PCT No. PCT/EP97/00960 Sec. 371 Date Sep. 3, 1998 Sec. 102(e) Date Sep. 3, 1998 PCT Filed Feb. 27, 1997 PCT Pub. No. WO97/32944 PCT Pub. Date Sep. 12, 1997In the process for the selective hydrogenation of dienes in diene-containing feed streams, a diene-containing feed stream is hydrogenated over a nickel-containing precipitated catalyst at from 40 to 100 DEG C., a pressure of from 3 to 20 bar and a WHSV (weight hourly space velocity) of from 1 to 10 kg/(lxh) in the presence of free hydrogen.
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公开(公告)号:CA2583155C
公开(公告)日:2013-07-09
申请号:CA2583155
申请日:2005-10-13
Applicant: BASF AG
Inventor: HILL THOMAS , PETERSEN HERMANN , KONS GERMAIN , JUNICKE HENRIK
Abstract: The invention relates to a catalyst on an oxidic carrier, and to methods for the selective hydrogenation of unsaturated compounds in hydrocarbon flows containing the same, using said catalysts.
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公开(公告)号:CA2583155A1
公开(公告)日:2006-04-20
申请号:CA2583155
申请日:2005-10-13
Applicant: BASF AG
Inventor: PETERSEN HERMANN , JUNICKE HENRIK , KONS GERMAIN , HILL THOMAS
Abstract: A catalyst on an oxidic support and processes for selectively hydrogenating unsaturated compounds in hydrocarbon streams comprising them using these catalysts are described.
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公开(公告)号:ES2140963T3
公开(公告)日:2000-03-01
申请号:ES97905112
申请日:1997-02-27
Applicant: BASF AG
Inventor: VICARI MAXIMILIAN , WALTER MARC , SCHWAB EKKEHARD , MULLER HANS-JOACHIM , KONS GERMAIN , DILLING STEPHAN
IPC: B01J23/755 , C10G45/36 , C10G67/02
Abstract: PCT No. PCT/EP97/00960 Sec. 371 Date Sep. 3, 1998 Sec. 102(e) Date Sep. 3, 1998 PCT Filed Feb. 27, 1997 PCT Pub. No. WO97/32944 PCT Pub. Date Sep. 12, 1997In the process for the selective hydrogenation of dienes in diene-containing feed streams, a diene-containing feed stream is hydrogenated over a nickel-containing precipitated catalyst at from 40 to 100 DEG C., a pressure of from 3 to 20 bar and a WHSV (weight hourly space velocity) of from 1 to 10 kg/(lxh) in the presence of free hydrogen.
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公开(公告)号:DE19608241A1
公开(公告)日:1997-09-18
申请号:DE19608241
申请日:1996-03-04
Applicant: BASF AG
Inventor: VICARI MAXIMILIAN DR , WALTER MARC DR , SCHWAB EKKEHARD DR , MUELLER HANS-JOACHIM DR , KONS GERMAIN , DILLING STEPHAN , POLANEK PETER DR
IPC: B01J23/755 , C10G45/36 , C10G67/02 , C07B35/02 , C07B63/00
Abstract: In the process for the selective hydrogenation of dienes in supply flows containing them, such a flow is hydrogenated on a nickel-containing precipitating catalyst at a temperature of between 40 and 100 DEG C, a pressure of between 3 and 20 bar and a WHSV (weight hourly space velocity) of between 1 and 10 kg/(lxh) in the presence of free hydrogen.
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公开(公告)号:DE102006017906A1
公开(公告)日:2007-10-25
申请号:DE102006017906
申请日:2006-04-18
Inventor: BOELT HEINZ , FRITZ PETER MATTHIAS , KONS GERMAIN , SCHINDLER GOETZ-PETER , SIMON FALK
Abstract: The invention relates to a method and a device for putting into service a reactor and a catalyst, especially a catalyst and a reactor for dehydrogenating a hydrocarbon-containing charge in a plant for producing olefins. Before being put into service, the catalyst and the reactor run through a plurality of oxidation and reduction phases, thereby releasing the chloride contained in the catalyst. The released chloride is carried off into the atmosphere in a gaseous form.
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公开(公告)号:DE59700760D1
公开(公告)日:1999-12-30
申请号:DE59700760
申请日:1997-02-27
Applicant: BASF AG
Inventor: VICARI MAXIMILIAN , WALTER MARC , SCHWAB EKKEHARD , MUELLER HANS-JOACHIM , KONS GERMAIN , DILLING STEPHAN , POLANEK PETER
IPC: B01J23/755 , C10G45/36 , C10G67/02
Abstract: PCT No. PCT/EP97/00960 Sec. 371 Date Sep. 3, 1998 Sec. 102(e) Date Sep. 3, 1998 PCT Filed Feb. 27, 1997 PCT Pub. No. WO97/32944 PCT Pub. Date Sep. 12, 1997In the process for the selective hydrogenation of dienes in diene-containing feed streams, a diene-containing feed stream is hydrogenated over a nickel-containing precipitated catalyst at from 40 to 100 DEG C., a pressure of from 3 to 20 bar and a WHSV (weight hourly space velocity) of from 1 to 10 kg/(lxh) in the presence of free hydrogen.
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公开(公告)号:AT186942T
公开(公告)日:1999-12-15
申请号:AT97905112
申请日:1997-02-27
Applicant: BASF AG
Inventor: VICARI MAXIMILIAN , WALTER MARC , SCHWAB EKKEHARD , MUELLER HANS-JOACHIM , KONS GERMAIN , DILLING STEPHAN , POLANEK PETER
IPC: B01J23/755 , C10G45/36 , C10G67/02
Abstract: PCT No. PCT/EP97/00960 Sec. 371 Date Sep. 3, 1998 Sec. 102(e) Date Sep. 3, 1998 PCT Filed Feb. 27, 1997 PCT Pub. No. WO97/32944 PCT Pub. Date Sep. 12, 1997In the process for the selective hydrogenation of dienes in diene-containing feed streams, a diene-containing feed stream is hydrogenated over a nickel-containing precipitated catalyst at from 40 to 100 DEG C., a pressure of from 3 to 20 bar and a WHSV (weight hourly space velocity) of from 1 to 10 kg/(lxh) in the presence of free hydrogen.
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公开(公告)号:DE102006017908A1
公开(公告)日:2007-10-25
申请号:DE102006017908
申请日:2006-04-18
Inventor: ADAM WOLFGANG , BOELT HEINZ , FRITZ PETER MATTHIAS , KLAPPER KLAUS , KONS GERMAIN , SCHINDLER GOETZ-PETER , SIMON FALK
IPC: B01J38/02
Abstract: The invention relates to a method and a device for the controlled regeneration of a catalyst and of a fired reactor, especially a catalyst and a reactor in a plant for producing olefins from a hydrocarbon-containing charge. During the regeneration phase of the catalyst for recovering the catalytic activity, the burners of the reactor are switched off. After the regeneration phase, the burners are re-ignited by means of inbuilt pilot burners. The pilot burners are monitored and their capacity is adjusted in such a manner that the heat loss of the reactor during the regeneration phase of the catalyst is compensated for.
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公开(公告)号:CA2248020C
公开(公告)日:2005-09-27
申请号:CA2248020
申请日:1997-02-27
Applicant: BASF AG
Inventor: VICARI MAXIMILIAN , KONS GERMAIN , MULLER HANS-JOACHIM , POLANEK PETER , DILLING STEPHAN , WALTER MARC , SCHWAB EKKEHARD
IPC: B01J23/755 , C10G45/36 , C10G67/02
Abstract: In the process for the selective hydrogenation of dienes in supply flows containing them, such a flow is hydrogenated on a nickel- containing precipitating catalyst at a temperature of between 40 and 100 .degree.C, a pressure of between 3 and 20 bar and a WHSV (weight hourly space velocity) of between 1 and 10 kg/(lxh) in the presence of free hydrogen.
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