-
公开(公告)号:AU2006222065A1
公开(公告)日:2006-09-14
申请号:AU2006222065
申请日:2006-03-03
Applicant: BASF AG
Inventor: MACHHAMMER OTTO , CRONE SVEN , SCHINDLER GOTZ-PETER , BORGMEIER FRIEDER
Abstract: The invention relates to a process for preparing propene from propane, comprising the steps: A) a feed gas stream a comprising propane is provided; B) the feed gas stream a comprising propane, if appropriate steam and if appropriate and an oxygenous gas stream are fed into a dehydrogenation zone and propane is subjected to a dehydrogenation to propene to obtain a product gas stream b comprising propane, propene, methane, ethane, ethene, nitrogen, carbon monoxide, carbon dioxide, steam, if appropriate hydrogen and if appropriate oxygen; C) the product gas stream b is cooled, if appropriate compressed and steam is removed by condensation to obtain a steam-depleted product gas stream c; D) uncondensable or low-boiling gas constituents are removed by contacting the product gas stream c with an inert absorbent and subsequently desorbing the gases dissolved in the inert absorbent to obtain a C 3 hydrocarbon stream d 1 and an offgas stream d 2 comprising methane, ethane, ethene, nitrogen, carbon monoxide, carbon dioxide, if appropriate hydrogen and if appropriate oxygen; E) the Ca hydrocarbon stream d 1 is cooled and if appropriate compressed to obtain a gaseous or liquid Ca hydrocarbon stream e 1; F) the C 3 hydrocarbon stream e 1 is if appropriate fed into a first distillation zone and separated distillatively into a stream f 1 composed of propane and propene and a stream f 2 comprising ethane and ethene; G) the stream e 1 or f 1 is fed into a (second) distillation zone and separated distillatively into a product stream g 1 composed of propene and a stream g 2 composed of propane, the stream g 2 being recirculated at least partially into the dehydrogenation zone.
-
公开(公告)号:AU2006204488A1
公开(公告)日:2006-07-13
申请号:AU2006204488
申请日:2006-01-04
Applicant: BASF AG
Inventor: BORGMEIER FRIEDER , MACHHAMMER OTTO , SCHINDLER GOTZ-PETER , CRONE SVEN
Abstract: A process for preparing propene from propane, comprising the steps: A) a feed gas stream a comprising propane is provided; B) the fed gas stream a comprising propane, if appropriate steam and, if appropriate, an oxygenous gas stream are fed into a dehydrogenation zone and propane is subjected to a dehydrogenation to propene to obtain a product gas stream b comprising propane, propene, methane, ethane, ethene, carbon monoxide, carbon dioxide, steam, if appropriate hydrogen and, if appropriate, oxygen; C) product gas stream b is cooled, if appropriate condensed and steam is removed by condensation to obtain a steam-depleted product gas stream c; D) product gas stream c is contacted in a first absorption zone with a selective, inert absorbent which selectively absorbs propene to obtain an absorbent stream d1 laden substantially with propene and a gas stream d2 comprising propane, methane, ethane, ethene, carbon monoxide, carbon dioxide and hydrogen; E) if appropriate, the absorbent stream d1 is decompressed to a lower pressure in a first desorption zone to obtain an absorbent stream e1 laden substantially with propene and a gas stream e2 comprising propene, and gas stream e2 is recycled into the first absorption zone, F) from the absorbent stream d1 or e1 laden substantially with propene, in at least one second desorption zone, by decompression, heating and/or stripping the absorbent stream d1 or e1, a gas stream f1 comprising propene is released and the selective absorbent is recovered.
-
公开(公告)号:AU2005313500A1
公开(公告)日:2006-06-15
申请号:AU2005313500
申请日:2005-12-08
Applicant: BASF AG
Inventor: CRONE SVEN , MACHHAMMER OTTO , SCHINDLER GOTZ-PETER
Abstract: The invention relates to a process for preparing propene from propane, comprising the steps: A) a feed gas stream a comprising propane is provided; B) the feed gas stream a comprising propane and an oxygenous gas stream are fed into a dehydrogenation zone and propane is subjected to a nonoxidative catalytic, autothermal dehydrogenation to propene to obtain a product gas stream b comprising propane, propene, methane, ethane, ethene, C4+ hydrocarbons, carbon monoxide, carbon dioxide, steam and hydrogen, C) the product gas stream b is cooled and steam is removed by condensation to obtain a steam-depleted product gas stream c, D) carbon dioxide is removed by gas scrubbing to obtain a carbon dioxide-depleted product gas stream d, E) the product gas stream d is cooled and a liquid hydrocarbon stream e1 comprising propane, propene, methane, ethane, ethene and C4+ hydrocarbons is removed by condensation to leave a residual gas stream e2 comprising methane, hydrogen and carbon monoxide, F) the liquid hydrocarbon stream e1 is fed into a first distillation zone and separated distillatively into a stream f1 comprising propane, propene and the C4+ hydrocarbons and a stream f2 comprising ethane and ethene, G) the stream f1 is fed into a second distillation zone and separated distillatively into a product stream g1 comprising propene and a stream g2 comprising propane and the C4+ hydrocarbons.
-
公开(公告)号:AU2005305996A1
公开(公告)日:2006-05-26
申请号:AU2005305996
申请日:2005-11-16
Applicant: BASF AG
Inventor: CRONE SVEN , FRITZ PETER MATTHIAS , SIMON FALK , BOLT HEINZ , SCHINDLER GOTZ-PETER
Abstract: The invention provides a process for hydrogenating streams in plants for producing alkenes by catalytic dehydrogenation of light alkanes, and also an apparatus for carrying out the process. The entire hydrocarbon stream to the dehydrogenation reactor, consisting of fresh and recycled alkane, is subjected upstream of the dehydrogenation reactor to a full hydrogenation of all unsaturated hydrocarbons present therein. This drastically reduces coke formation in the dehydrogenation reactor. The energy demand for the preheating of the reactant stream to reaction temperature is reduced since the energy released in the exothermic hydrogenation remains virtually fully in the hydrocarbon stream.
-
公开(公告)号:NO20044561L
公开(公告)日:2004-11-26
申请号:NO20044561
申请日:2004-10-22
Applicant: BASF AG
Inventor: HESSE MICHAEL , HARTH KLAUS , HOFSTADT OTTO , SCHINDLER GOTZ-PETER , SIMON FALK
IPC: B01J23/62 , B01J21/06 , B01J23/63 , B01J35/00 , B01J35/10 , B01J37/00 , C07B61/00 , C07C5/333 , C07C11/06 , C07C5/327
Abstract: The invention relates to a process for preparing a catalyst support, in which zirconium dioxide powder is mixed with a binder, if desired a pore former, if desired an acid, water and, if desired, further additives to give a kneadable composition and the composition is homogenized, shaped to produce shaped bodies, dried and calcined, wherein the binder is a monomeric, oligomeric or polymeric organosilicon compound. Suitable binders are monomeric, oligomeric or polymeric silanes, alkoxysilanes, aryloxysilanes, acryloxysilanes, oximinosilanes, halosilanes, aminoxysilanes, aminosilanes, amidosilanes, silazanes or silicones. The invention also provides the catalyst support which has been prepared in this way, a catalyst comprising the support and its use as dehydrogenation catalyst.
-
公开(公告)号:NO20044561A
公开(公告)日:2004-11-26
申请号:NO20044561
申请日:2004-10-22
Applicant: BASF AG
Inventor: HESSE MICHAEL , HARTH KLAUS , HOFSTADT OTTO , SCHINDLER GOTZ-PETER , SIMON FALK
IPC: B01J23/62 , B01J21/06 , B01J23/63 , B01J35/00 , B01J35/10 , B01J37/00 , C07B61/00 , C07C5/333 , C07C11/06 , C07C5/327
CPC classification number: C07C5/3332 , B01J21/066 , B01J23/002 , B01J23/63 , B01J35/002 , B01J35/10 , B01J35/109 , B01J37/0009 , B01J37/0018 , B01J2523/00 , C07C2521/06 , Y02P20/52 , C07C11/06 , B01J2523/13 , B01J2523/15 , B01J2523/3706 , B01J2523/41 , B01J2523/43 , B01J2523/48 , B01J2523/828
-
67.
公开(公告)号:AU2003266395A1
公开(公告)日:2004-04-23
申请号:AU2003266395
申请日:2003-09-18
Applicant: BASF AG
Inventor: SCHINDLER GOTZ-PETER , PETZOLDT JOCHEN , ADAMI CHRISTOPH , MACHHAMMER OTTO , MULLER-ENGEL KLAUS JOACHIM , MARTAN HANS , HECHLER CLAUS
IPC: B01J23/00 , B01J23/887 , C07C5/32 , C07C5/48 , C07C7/05 , C07C11/06 , C07C27/00 , C07C45/35 , C07C51/215 , C07C51/25 , C07C235/24 , C07C253/24 , C07C253/26 , C07C255/08 , C07D301/10
Abstract: In a process for preparing at least one partial oxidation and/or ammoxidation product of propylene, the propylene is obtained from crude propane by dehydrogenating and subjected in the presence of unconverted propane as a constituent of a gas mixture 2 which comprises a total C 4 -hydrocarbon content of
-
公开(公告)号:AU2003255444A1
公开(公告)日:2004-03-11
申请号:AU2003255444
申请日:2003-08-14
Applicant: BASF AG
Inventor: SCHINDLER GOTZ-PETER , HARTH KLAUS
Abstract: In an isothermal method for dehydrogenation of alkanes (I) to the corresponding alkenes (II) over a bed of dehydrogenation catalyst (A), the new feature is that the bed contains a catalytically inactive, inert diluent (B).
-
公开(公告)号:AU2003254335A1
公开(公告)日:2004-02-02
申请号:AU2003254335
申请日:2003-07-10
Applicant: BASF AG
Inventor: HARTH KLAUS , HIBST HARTMUT , SCHINDLER GOTZ-PETER , WALSDORFF CHRISTIAN
IPC: B01J23/62 , C07B61/00 , C07C5/333 , C07C11/167
Abstract: The invention relates to a process for preparing butadiene from n-butane comprising the steps (A) providing an n-butane-containing feed gas stream, (B) feeding the n-butane-containing feed gas stream into a first dehydrogenation zone and nonoxidatively catalytically dehydrogenating n-butane to 1-butene, 2-butene and optionally butadiene to obtain a first product gas stream comprising n-butane, 1-butene and 2-butene, with or without butadiene and secondary components, (C) feeding the first product gas stream comprising n-butane, 1-butene and 2-butene, with or without butadiene and secondary components, into a second dehydrogenation zone and oxidatively dehydrogenating 1-butene and 2-butene to butadiene to give a second product gas stream comprising butadiene, n-butane and steam, with or without secondary components, (D) recovering butadiene from the second product gas stream.
-
公开(公告)号:AU2002362492A1
公开(公告)日:2003-04-14
申请号:AU2002362492
申请日:2002-10-01
Applicant: BASF AG
Inventor: MAAS HEIKO , HEIDEMANN THOMAS , STEPHAN JURGEN , SCHINDLER GOTZ-PETER , STEINBRENNER ULRICH
IPC: C07C15/00 , C07C309/31 , C11D1/22 , C07C5/333 , C07C309/28
-
-
-
-
-
-
-
-
-