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公开(公告)号:DE3528313A1
公开(公告)日:1987-02-12
申请号:DE3528313
申请日:1985-08-07
Applicant: BASF AG
Inventor: BOEHNING KARL-HEINZ DR , MROSS WOLF DIETER DR , SCHWARZMANN MATTHIAS DR , BECKER HANS-JUERGEN DR , PLUECKHAN JUERGEN DR , RENNER KLAUS-CHRISTIAN DR
IPC: B01J23/66 , B01J35/10 , C07D301/10 , B01J23/50
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公开(公告)号:DE3368920D1
公开(公告)日:1987-02-12
申请号:DE3368920
申请日:1983-03-18
Applicant: BASF AG
Abstract: Olefins are prepared by converting methanol and/or dimethyl ether in the presence of a zeolite catalyst at elevated temperatures by a process wherein the catalyst used is a borosilicate zeolite which has been molded together with an amorphous binder containing aluminum oxide and silicon dioxide. The advantage of using the borosilicate catalyst is that the yield of C2-C4-olefins is improved at the expense of formation of higher hydrocarbons.
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公开(公告)号:AT23327T
公开(公告)日:1986-11-15
申请号:AT84108454
申请日:1984-07-18
Applicant: BASF AG
Inventor: TAGLIEBER VOLKER DR , HOELDERICH WOLFGANG DR , KUMMER RUDOLF DR , MROSS WOLF DIETER DR , SALADIN GUENTER
IPC: C07B61/00 , B01J21/00 , B01J29/04 , B01J29/86 , C07C67/00 , C07C209/00 , C07C209/60 , C07C211/02 , C07C85/18 , C07C87/06
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公开(公告)号:DE3361378D1
公开(公告)日:1986-01-16
申请号:DE3361378
申请日:1983-03-18
Applicant: BASF AG
Inventor: HOELDERICH WOLFGANG DR , HIMMEL WALTER DR , MROSS WOLF DIETER DR , SCHWARZMANN MATTHIAS DR
Abstract: Olefins are prepared by converting methanol and/or dimethyl ether in the presence of a zeolite catalyst at elevated temperatures by a process wherein the catalyst used is a borosilicate zeolite which has been molded together with an amorphous binder containing aluminum oxide and silicon dioxide. The advantage of using the borosilicate catalyst is that the yield of C2-C4-olefins is improved at the expense of formation of higher hydrocarbons.
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公开(公告)号:DE3407289A1
公开(公告)日:1985-09-05
申请号:DE3407289
申请日:1984-02-29
Applicant: BASF AG
Inventor: BIFFAR WERNER DR , KRATTE KLAUS DR , LEHNERT RUDI DR , MROSS WOLF DIETER DR , STARKE KLAUS , SCHWARZMANN MATTHIAS DR
Abstract: The application relates to a process for the catalytic purification of nitrogen oxide-containing exhaust gases from internal combustion engines, in which ammonia is added to the exhaust gases and the gas mixture is passed over a non-noble metal catalyst which may, if appropriate, be applied to a support.
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公开(公告)号:DE3263412D1
公开(公告)日:1985-06-05
申请号:DE3263412
申请日:1982-09-09
Applicant: BASF AG
Abstract: A process for the preparation of olefins from methanol and/or dimethyl ether by conversion in the presence of a zeolite catalyst, in particular a borosilicate zeolite, at elevated temperature, with the addition of a small amount of an electron donor.
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公开(公告)号:DE3261547D1
公开(公告)日:1985-01-24
申请号:DE3261547
申请日:1982-07-16
Applicant: BASF AG
Abstract: The process for the preparation of olefins by converting methanol and/or dimethyl ether in the presence of a zeolite catalyst is improved by treating the catalyst with hydrogen fluoride. Aluminosilicate zeolites and borosilicate zeolites, especially those of the pentasil type, are chiefly used.
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18.
公开(公告)号:DE3164202D1
公开(公告)日:1984-07-19
申请号:DE3164202
申请日:1981-10-05
Applicant: BASF AG
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19.
公开(公告)号:DE2641000A1
公开(公告)日:1978-03-16
申请号:DE2641000
申请日:1976-09-11
Applicant: BASF AG
Inventor: MROSS WOLF DIETER DR , TITZENTHALER ECKART DR , SCHARZMANN MATTHIAS DR , KOOPMANN JUERGEN DR
IPC: B01J23/66 , C07D301/10 , C07D303/02
Abstract: Catalysts for ethylene oxide prepn. from ethylene and O2 comprise Ag and alkali metals or their cpds. deposited on a support. The catalysts contain (a) 0.1-2 atom % Na and (b) either 0.05-0.35 atom % K, 0.003-0.25 atom % Rb, 0.0005-0.2 atom % Cs or a corresp. amt. of a mixt. thereof. All percentages are based on the Ag content. The Ag content is pref. 2-12 (esp. 5-10) wt.% based on the wt. of the catalyst. The catalysts are pref. prepd. by impregnating the support with an aq. soln. of an Ag complex salt (e.g. an Ag-amine carboxylate) and suitable alkali metal cpds. (e.g. hydroxides), steaming the resulting composite until the Ag cpd. decomposes, and calcining the product at 100-400 degrees C to constant wt. Other standard methods can also be used. The catalysts have higher activity and selectivity than conventional Ag catalysts promoted with alkali(ne earth) metals, and/or have a longer life.
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20.
公开(公告)号:DE2622228A1
公开(公告)日:1977-12-08
申请号:DE2622228
申请日:1976-05-19
Applicant: BASF AG
Inventor: MROSS WOLF DIETER DR , TITZENTHALER ECKART DR , SCHWARZMANN MATTHIAS DR , KOOPMANN JUERGEN DR
IPC: B01J23/66 , C07D301/10
Abstract: Catalysts for ethylene oxide prepn. from ethylene and O2 comprise Ag and alkali metals or their cpds. deposited on a support. The catalysts contain (a) 0.1-2 atom % Na and (b) either 0.05-0.35 atom % K, 0.003-0.25 atom % Rb, 0.0005-0.2 atom % Cs or a corresp. amt. of a mixt. thereof. All percentages are based on the Ag content. The Ag content is pref. 2-12 (esp. 5-10) wt.% based on the wt. of the catalyst. The catalysts are pref. prepd. by impregnating the support with an aq. soln. of an Ag complex salt (e.g. an Ag-amine carboxylate) and suitable alkali metal cpds. (e.g. hydroxides), steaming the resulting composite until the Ag cpd. decomposes, and calcining the product at 100-400 degrees C to constant wt. Other standard methods can also be used. The catalysts have higher activity and selectivity than conventional Ag catalysts promoted with alkali(ne earth) metals, and/or have a longer life.
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