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公开(公告)号:MY137358A
公开(公告)日:2009-01-30
申请号:MYPI20034626
申请日:2003-12-03
Applicant: BASF AG
Inventor: BASLER PETER DR , SIEGEL WOLFGANG DR , ACHHAMMER GUNTHER DR , NEGELE ANTON DR , MENIG HELMUTH DR , RUPPEL WILHELM DR , ZEHNER PETER DR , LUYKEN HERMANN , VOGT VOLKER DR
Abstract: THE PRESENT INVENTION RELATES TO A PROCESS FOR PREPARING HYDROCYANIC ACID (HCN) BY CATALYTIC DEHYDRATION OF GASEOUS FORMAMIDE IN A REACTOR WHICH HAS AN INTERNAL REACTOR SURFACE MADE OF A STEEL COMPRISING IRON AND CHRONIUM AND NICKEL, AND ALSO TO A REACTOR FOR PREPARING HYDROCYANIC ACID BY CATALYTIC DEHYDRATION OF GASEOUS FORMAMIDE, WHICH REACTOR HAS AN INTERNAL REACTOR SURFACE MADE OF A STEEL COMPRISING IRON AND CHRONIUM AND NICKEL, AND ALSO TO THE USE OF THE REACTOR OF THE PRESENT INVENTION IN A PROCESS FOR PREPARING HYDROCYANIC ACID BY CATALYTIC DEHYDRATION OF GASEOUS FORMAMIDE.
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公开(公告)号:MY135595A
公开(公告)日:2008-05-30
申请号:MYPI20040685
申请日:2004-02-27
Applicant: BASF AG
Inventor: DIETERLE MARTIN DR , PETZOLDT JOCHEN DR , ARNOLD HEIKO DR , RUPPEL WILHELM DR , MUELLER-ENGEL KLAUS JOACHIM DR
IPC: C07C57/055 , C07C51/10 , C07C51/25
Abstract: IN A PROCESS FOR HETEROGENEOUSLY CATALYZED PARTIAL GAS PHASE OXIDATION OF ACROLEIN TO ACRYLIC ACID, THE STARTING REACTION GAS MIXTURE IS OXIDIZED OVER A FIXED CATALYST BED 1 WHICH CONSISTS OF AT LEAST TWO FIXED CATALYST BED ZONES AND IS ACCOMMODATED IN TWO SUCCESSIVE TEMPERATURE ZONES A,B, AND THE TRANSITION FROM TEMPERATURE ZONE A TO TEMPERATURE ZONE B DOES NOT COINCIDE WITH A TRANSITION FROM ONE FIXED CATALYST BED ZONE TO ANOTHER FIXED CATALYST BED ZONE.
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公开(公告)号:MY128287A
公开(公告)日:2007-01-31
申请号:MYPI20010925
申请日:2001-03-01
Applicant: BASF AG
Inventor: WEIGUNY JENS DR , STORCK SEBASTIAN DR RER NAT , TENTEN ANDREAS DR , RUPPEL WILHELM DR
IPC: C07D307/60 , B01J27/28 , B01J38/04 , C07B61/00 , C07C51/215
Abstract: IN A PROCESS FOR PREPARING MALEIC ANHYDRIDE BY HETEROGENEOUSLY CATALYZED GAS-PHASE OXIDATION OF HYDROCARBONS HAVING AT LEAST FOUR CARBON ATOMS USING OXYGEN-CONTAINING GASES IN THE PRESENCE OF A VOLATILE PHOSPHORUS COMPOUND OVER A CATALYST COMPRISING VANADIUM, PHOSPHORUS AND OXYGEN IN A SHELL-AND-TUBE REACTOR UNIT (2) HAVING AT LEAST TWO SUCCESSIVE COOLED REACTION ZONES, THE TEMPERATURE OF THE FIRST REACTION ZONE IS FROM 350 TO 450°C. AND THE TEMPERATURE OF THE SECOND AND FURTHER REACTION ZONES IS FROM 350 TO 480°C. AND THE TEMPERATURE DIFFERENCE BETWEEN THE HOTTEST REACTION ZONE AND THE COOLEST REACTION ZONE IS AT LEAST 2°C.(FIG 1A)
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公开(公告)号:CZ294399B6
公开(公告)日:2004-12-15
申请号:CZ229395
申请日:1995-09-07
Applicant: BASF AG
Inventor: RUPPEL WILHELM DR , WEGERLE ULRIKE , TENTEN ANDREAS DR , HAMMON ULRICH DR
IPC: B01J23/88 , B01J8/06 , B01J21/02 , B01J23/16 , B01J23/887 , B01J27/132 , B01J27/192 , C07B61/00 , C07C45/35 , C07C47/22
Abstract: In the present invention, there is described a process of catalytic oxidation of propylene to acrolein in gaseous phase wherein a gas-phase mixture of propene and oxygen is catalytically oxidized by passing a reactant gas mixture comprising propene and oxygen through a plurality of catalyst containing contact tubes in a fixed bed reactor and simultaneously passing only one heat-exchange medium at elevated temperature over the exterior surfaces of the contact tubes in a longitudinal flow pattern which is co-current with the direction of flow of the reactants through said tube; simultaneously superposing a transverse flow on said longitudinal flow of heat exchange medium by means of an arrangement of successive baffles along the contact tubes which leave passage cross-sections free, thereby resulting in a meandrous flow of the heat-exchange medium through the reactor and setting the flow rate of said heat-exchange medium so that its temperature between the point of entry of the medium into the reactor and its point of exit increases by 2 to 10 degC.
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公开(公告)号:ES2080540T5
公开(公告)日:2003-07-01
申请号:ES93102913
申请日:1993-02-25
Applicant: BASF AG
Inventor: HESS KLAUS DR , RUPPEL WILHELM DR , MORSBACH BERND , REGENAUER WILLI
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公开(公告)号:ES2169457T3
公开(公告)日:2002-07-01
申请号:ES98108692
申请日:1998-05-13
Applicant: BASF AG
Inventor: AQUILA WERNER DR , FUCHS HARTWIG , WORZ OTTO DR , RUPPEL WILHELM DR , HALBRITTER KLAUS DR
Abstract: Continuous technical preparation of aldehydes of formula (I) comprises dehydration of the corresponding alcohol of formula (II) with an oxygen-containing gas using a catalyst based on copper, silver and/or gold on an inert carrier in a multi-pipe reactor. This is followed by rapid cooling of the reaction gases, separation of the aldehyde from the resulting condensate and recycling of any unreacted alcohol. During the process (II) is vapourised, the alcohol vapour is mixed with the oxygen-containing gas, the resulting vapour is passed through a 0.5 cm layer of the catalyst at a temperature that is greater than the boiling point of the alcohol but lower than the starting temperature of the reaction and the vapour is then allowed to pass through a number of parallel pipes which are filled with catalyst and kept warm by a circulating fluid. The pipes have an inner diameter, D, of 0.5-3 cm and are at least 5 cm long and the reaction temperature is 300-600 degrees C. R1R2CHO (I) R1R2CH-CH2-OH (II) R1 = H and R2 = CH2=C(CH3)- (isoprenal); or R1+R2 = (CH3)2C= (prenal)
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公开(公告)号:DE59602040D1
公开(公告)日:1999-07-08
申请号:DE59602040
申请日:1996-03-01
Applicant: BASF AG
Inventor: HEFNER WERNER DR , MACHHAMMER OTTO DR , NEUMANN HANS-PETER DR , TENTEN ANDREAS DR , RUPPEL WILHELM DR , VOGEL HERBERT DR
Abstract: In continuous gas phase oxidn. of C3H6 to acrolein (I) and/or acrylic acid (II) with heterogeneous catalyst in an oxidn. reactor, the charge gas mixt. (III) contains only inert diluent gas(es) (IIIA) in addn. to C3H6 and O2 and (pt. of) (IIIA) is sepd. from the prodn. gas mixt. and recycled to the oxidn. reactor. The novelty is that (IIIA) consists of over 85 vol. % 1-5C satd. hydrocarbon(s).
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公开(公告)号:ES2116795T3
公开(公告)日:1998-07-16
申请号:ES96103128
申请日:1996-03-01
Applicant: BASF AG
Inventor: HEFNER WERNER DR , MACHHAMMER OTTO DR , NEUMANN HANS-PETER DR , TENTEN ANDREAS DR , RUPPEL WILHELM DR , VOGEL HERBERT DR
IPC: C07B35/04 , C07B41/06 , C07B41/08 , C07C27/00 , C07C45/32 , C07C45/35 , C07C47/22 , C07C51/235 , C07C51/25 , C07C51/265 , C07C57/05 , C07D301/08
Abstract: Continuous gas phase partial oxidn. of an organic cpd. (I) with heterogeneous catalyst in an oxidn. reactor uses a charge gas mixt. contg. (I) O2 and an inert diluent gas (II), which consists partly of combustible gases (IIA). The novelty is that the (IIA) fraction of (II) in the prod. gas stream leaving the oxidn. reactor is not recycled to partial oxidn. but used in another chemical reaction.
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49.
公开(公告)号:CZ9600735A3
公开(公告)日:1996-10-16
申请号:CZ73596
申请日:1996-03-08
Applicant: BASF AG
Inventor: WERNER HEFNER DR , OTTO MACHHAMMER DR , NEUMANN HANS-PETER DR , TENTEN ANDREAS DR , RUPPEL WILHELM DR , VOGEL HERBERT DR
IPC: C07B35/04 , C07B41/06 , C07B41/08 , C07C27/00 , C07C45/35 , C07C47/22 , C07C51/235 , C07C51/25 , C07C51/265 , C07C57/05 , C07D301/08
CPC classification number: C07D301/08 , C07C45/35 , C07C51/235 , C07C51/25 , C07C51/252 , C07C51/265 , C07C47/22
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公开(公告)号:DE19508532A1
公开(公告)日:1996-09-12
申请号:DE19508532
申请日:1995-03-10
Applicant: BASF AG
Inventor: HEFNER WERNER DR , MACHHAMMER OTTO DR , NEUMANN HANS-PETER DR , TENTEN ANDREAS DR , RUPPEL WILHELM DR , VOGEL HERBERT DR
Abstract: In continuous gas phase oxidn. of C3H6 to acrolein (I) and/or acrylic acid (II) with heterogeneous catalyst in an oxidn. reactor, the charge gas mixt. (III) contains only inert diluent gas(es) (IIIA) in addn. to C3H6 and O2 and (pt. of) (IIIA) is sepd. from the prodn. gas mixt. and recycled to the oxidn. reactor. The novelty is that (IIIA) consists of over 85 vol. % 1-5C satd. hydrocarbon(s).
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