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公开(公告)号:MY140438A
公开(公告)日:2009-12-31
申请号:MYPI20041938
申请日:2004-05-20
Applicant: BASF AG
Inventor: DIETERLE MARTIN DR , HIBST HARTMUT PROF DR , POEPEL WOLFGANG JUERGEN DR , PETZOLDT JOCHEN DR , MUELLER-ENGEL KLAUS JOACHIM DR
IPC: B01J23/00 , B01J8/10 , B01J23/887 , B01J23/888 , B01J35/00 , B01J37/00 , B01J37/02 , B01J37/08 , C07C51/215 , C07C51/235 , C07C51/25
Abstract: CATALYTICALLY ACTIVE MULTIELEMENT OXIDE MATERIALS WHICH CONTAIN AT LEAST ONE OF THE ELEMENTS NB AND WAND THE ELEMENTS MO, V AND CU ARE PREPARED BY A PROCESS IN WHICH AN INTIMATE DRY BLEND CONTAINING AMMONIUM IONS IS PREPARED AND SAID DRY BLEND IS SUBJECTED TO A THERMAL TREATMENT IN AN ATMOSPHERE HAVING A LOW MOLECULAR OXYGEN CONTENT AT ELEVATED TEMPERATURES, A PORTION OF THE AMMONIUM IONS CONTAINED IN THE INTIMATE DRY BLEND BEING DECOMPOSED WITH LIBERATION OF AMMONIA AND THE OXYGEN CONTENT OF THE THERMAL TREATMENT ATMOSPHERE BEING INCREASED IN THE COURSE OF THE THERMAL TREATMENT.
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公开(公告)号:MY147936A
公开(公告)日:2013-02-15
申请号:MYPI20060775
申请日:2006-02-23
Applicant: BASF AG
Inventor: PETZOLDT JOCHEN DR , CREMER ULRICH DR , DIETERLE MARTIN DR
Abstract: THE PRESENT INVENTION RELATES TO A PROCESS FOR CHARGING A REACTOR WITH A CATALYST, TO THE RESULTING CHARGED REACTORS, AND TO THE USE THEREOF FOR CARRYING OUT CATALYTIC GAS PHASE REACTIONS.
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公开(公告)号:MY140688A
公开(公告)日:2010-01-15
申请号:MYPI20040837
申请日:2004-03-11
Applicant: BASF AG
Inventor: DIETERLE MARTIN DR RER NAT , PETZOLDT JOCHEN DR , MUELLER-ENGEL KLAUS JOACHIM DR , MARTAN HANS DR
Abstract: IN A PROCESS FOR HETEROGENEOUSLY CATALYZED PARTILA GAS PHASE OXIDATION OF PROPENE TO ACRYLIC ACID, THE STARTING REACTION GAS MIXTURE IS OXIDIZED AT A PROPENE LOADING OF
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公开(公告)号:MY136659A
公开(公告)日:2008-11-28
申请号:MYPI20040570
申请日:2004-02-20
Applicant: BASF AG
Inventor: PETZOLDT JOCHEN DR , DIETERLE MARTIN DR , ARNOLD HEIKO DR , RUPPEL WILHELM DR , MUELLER-ENGEL KLAUS JOACHIM DR
Abstract: IN A PROCESS FOR HETEROGENEOUSLY CATALYZED PARTIAL GAS PHASE OXIDATION OF PROPENE TO ACROLEIN, THE STARTING REACTION GAS MIXTURE IS OXIDIZED OVER A FIXED CATALYST BED 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 SPATIALLY 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:MY143553A
公开(公告)日:2011-05-31
申请号:MYPI20094284
申请日:2004-05-20
Applicant: BASF AG
Inventor: DIETERLE MARTIN DR , HIBST HARTMUT PROF DR , POEPEL WOLFGANG JUERGEN DR , PETZOLDT JOCHEN DR , MUELLER-ENGEL KLAUS JOACHIM DR
IPC: C07C51/235 , B01J8/10 , B01J23/00 , B01J23/887 , B01J23/888 , B01J35/00 , B01J37/00 , B01J37/02 , B01J37/08 , C07C51/215 , C07C51/25
Abstract: Disclosed is a method for producing catalytically active multielement oxide materials containing at least one of the elements Nb and W as well as elements Mo, V, and Cu. According to the inventive method, an intimate dry mixture containing ammonium ions is produced and is thermally treated at a raised temperature in an atmosphere that is low in molecular oxygen. A partial quantity of the ammonium ions contained in the intimate dry mixture is decomposed so as to release ammonia while the oxygen concentration of the thermal treatment atmosphere is increased in the course of the thermal treatment.
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公开(公告)号:MY139342A
公开(公告)日:2009-09-30
申请号:MYPI20044486
申请日:2004-10-29
Applicant: BASF AG
Abstract: A PROCESS FOR THE LONG-TERM OPERATION OF A TWO-STAGE HETEROGENEOUSLY CATALYZED GAS PHASE PARTIAL OXIDATION OF PROPENE TO ACRYLIC ACID, IN WHICH THE TEMPERATURE OF THE FIXED CATALYST BEDS IS INCREASED OVER THE TIME AND THE GAS PHASE PARTIAL OXIDATION IS INTERRUPTED FROM TIME TO TIME AND AN OXYGEN-CONTAINING GAS MIXTURE IS CONDUCTED THROUGH THE FIXED CATALYST BEDS AT ELEVATED TEMPERATURE OF THE FIXED CATALYST BEDS.
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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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9.
公开(公告)号:MY144309A
公开(公告)日:2011-08-29
申请号:MYPI20041246
申请日:2004-04-05
Applicant: BASF AG
Inventor: SCHINDLER GOTZ-PETER DR , MACHHAMMER OTTO DR , MUELLER-ENGEL KLAUS JOACHIM DR , HECHLER CLAUS DR , PETZOLDT JOCHEN DR , ADAMI CHRISTOPH DR , HARTH KLAUS DR
IPC: C07C253/08 , B01J23/62 , B01J23/63 , C07C45/33 , C07C45/34 , C07C45/35 , C07C51/25 , C07C253/26 , C07C255/08
Abstract: A PROCESS FOR PREPARING AT LEAST ONE PARTIAL OXIDATION AND/OR AMMOXIDATION PRODUCT OF A HYDROCARBON BY PARTIALLY DEHYDROGENATING AT LEAST ONE SATURATED HYDROCARBON H UNDER HETEROGENEOUS CATALYSIS AND USING THE RESULTING PRODUCT GAS MIXTURE A, WHICH COMPRISES THE PARTIALLY DEHYDROGENATED HYDROCARBON H, AS SUCH OR IN MODIFIED FORM FOR HETEROGENEOUSLY CATALYZED PARTIAL OXIDATION AND/OR AMMOXIDATION OF THE PARTIALLY DEHYDROGENATED HYDROCARBON PRESENT IN THE PRODUCT GAS MIXTURE A, SAID PROCESS INCLUDING AT LEAST ONE MECHANICAL SEPARATING OPERATION INSERTED BETWEEN THE PRODUCT GAS MIXTURE A AND THE HETEROGENEOUSLY CATALYZED PARTIAL OXIDATION AND/OR AMMOXIDATION.
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10.
公开(公告)号:MY139735A
公开(公告)日:2009-10-30
申请号:MYPI20044514
申请日:2004-11-01
Applicant: BASF AG
Inventor: PETZOLDT JOCHEN DR , MUELLER-ENGEL KLAUS JOACHIM M DR
IPC: B01J23/888 , B01J35/00 , B01J35/02 , C07C45/35
Abstract: ACROLEIN IS PREPARED BY A PROCESS OF HETEROGENEOUS CATALYZED PARTIAL GAS PHASE OXIDATION, BY PASSING A STARTING REACTION GAS MIXTURE WHICH COMPRISES PROPENE, MOLECULAR OXYGEN AND AT LEAST ONE INERT GAS, IN WHICH THE MOLECULAR OXYGEN TO PROPENE (O2:C3H6) MOLE RATIO IS ≥1, AND CARBON DIOXIDE AND SATURATED HYDROCARBONS TOGETHER IN A TOTAL AMOUNT OF AT MOST 15 MOL %, AT ELEVATED TEMPERATURE AND AT AN HOURLY SPACE VELOCITY ON THE FIXED CATALYST BED OF PROPENE PRESENT IN THE STARTING REACTION GAS MIXTURE OF ≥120 I (STP)/LOH THROUGH A FIXED CATALYST BED WHOSE CATALYSTS ARE COMPRISED OF ANNULAR UNSUPPORTED CATALYSTS WHOSE ACTIVE COMPONENT IS AT LEAST ONE MULTIMETAL OXIDE OF FORMULA I, MO12WACOBFECBIDSIEKTON (I) WHEREIN A RANGES FROM ≥1 TO ≤3, B RANGES FROM ≥3 TO ≤8, C RANGES FROM ≥1 TO ≤4, D RANGES FROM ≥0.5 TO ≤1.5, E RANGES FROM ≥O TO ≤10, AND F RANGES FROM ≥0 TO ≤0.2 AND N IS A NUMBER WHICH IS DETERMINED BY THE VALENCY AND FREQUENCY OF THE ELEMENTS IN THE COMPOSITION OF FORMULA I OTHER THAN OXYGEN, IN SUCH A WAY THAT THE PROPENE CONVERSION IN SINGLE PASS IS ≥90 MOL % AND THE ASSOCIATED SELECTIVITY OF ACROLEIN FORMATION IS ≥80 MOL %, WHEREIN, IN THE MULTI METAL OXIDE COMPOSITION OF FORMULA I, THE FOLLOWING MOLE RATIOS ARE: CO/FE=FROM 2 TO 4 AND CO/MO=FROM 0.3 TO 0.7.
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