公开(公告)号：AT15977T

公开(公告)日：1985-10-15

申请号：AT82200076

申请日：1982-01-22

Applicant: STAMICARBON

Inventor： KLEUSKENS ENGELINA CATHARINA ,  VAN DE MOND THEODORUS JOHANNES ,  MAESSEN JOHANNES GERARDUS HEND

IPC: C07C5/42 ,  B01J27/30 ,  B01J38/00 ,  C07B35/04 ,  C07B41/00 ,  C07B43/08 ,  C07B61/00 ,  C07C1/00 ,  C07C5/48 ,  C07C11/12 ,  C07C45/00 ,  C07C45/34 ,  C07C47/22 ,  C07C67/00 ,  C07C253/00 ,  C07C255/08 ,  C11B1/06 ,  C07C120/00

Abstract: Process for the reactivation of a spent oxidic catalyst suitable for oxidation, ammoxidation and/or oxidative dehydrogenation of olefines and that contains a tellurium oxide and as active components mainly oxides of antimony and/or iron. The spent catalyst is mixed with a solid particulate tellurium compound or with a particulate, solid carrier material containing a tellurium compound.

公开(公告)号：DE3060909D1

公开(公告)日：1982-11-11

申请号：DE3060909

申请日：1980-03-27

Applicant: STAMICARBON

Inventor： BEEKHUIS GERRIT ERNST ,  VAN DE MOND THEODORUS JOHANNES ,  NIEUWKAMP JOHANNES GERARDUS MA

IPC: C07D207/26 ,  B01J23/78 ,  C07D201/08 ,  C07D207/263 ,  C07D207/267

公开(公告)号：DE3266722D1

公开(公告)日：1985-11-14

申请号：DE3266722

申请日：1982-01-22

Applicant: STAMICARBON

Inventor： KLEUSKENS ENGELINA CATHARINA ,  VAN DE MOND THEODORUS JOHANNES ,  MAESSEN JOHANNES GERARDUS HEND

IPC: C07C5/42 ,  B01J27/30 ,  B01J38/00 ,  C07B35/04 ,  C07B41/00 ,  C07B43/08 ,  C07B61/00 ,  C07C1/00 ,  C07C5/48 ,  C07C11/12 ,  C07C45/00 ,  C07C45/34 ,  C07C47/22 ,  C07C67/00 ,  C07C253/00 ,  C07C255/08 ,  C11B1/06 ,  C07C120/00

Abstract: Process for the reactivation of a spent oxidic catalyst suitable for oxidation, ammoxidation and/or oxidative dehydrogenation of olefines and that contains a tellurium oxide and as active components mainly oxides of antimony and/or iron. The spent catalyst is mixed with a solid particulate tellurium compound or with a particulate, solid carrier material containing a tellurium compound.

公开(公告)号：DE3567846D1

公开(公告)日：1989-03-02

申请号：DE3567846

申请日：1985-03-05

Applicant: STAMICARBON

Inventor： VAN HARDEVELD RUDOLF ,  VAN DE MOND THEODORUS JOHANNES ,  VANDENBOOREN FRANCISCUS HENRIC

IPC: B01J35/10 ,  C01C3/16

Abstract: An improved process for the preparation of cyanamide or a cyanamide-containing gas mixture by passing urea and/ or urea decomposition products over a catalyst at a temperature in the range of between about 200°C and 600°C. A porous catalyst is utilized which has an intracrystalline pore diameter of at most 8 A, whereby a high conversion to cyanamide is obtained and the formation of melamine by-products is substantially reduced.

公开(公告)号：AT40343T

公开(公告)日：1989-02-15

申请号：AT85200320

申请日：1985-03-05

Applicant: STAMICARBON

Inventor： VAN HARDEVELD RUDOLF ,  VAN DE MOND THEODORUS JOHANNES ,  VANDENBOOREN FRANCISCUS HENRIC

IPC: B01J35/10 ,  C01C3/16

Abstract: An improved process for the preparation of cyanamide or a cyanamide-containing gas mixture by passing urea and/ or urea decomposition products over a catalyst at a temperature in the range of between about 200°C and 600°C. A porous catalyst is utilized which has an intracrystalline pore diameter of at most 8 A, whereby a high conversion to cyanamide is obtained and the formation of melamine by-products is substantially reduced.

公开(公告)号：DE2962677D1

公开(公告)日：1982-06-24

申请号：DE2962677

申请日：1979-04-21

Applicant: STAMICARBON

Inventor： VAN DE MOND THEODORUS JOHANNES ,  DELAHAYE HUBERTUS JOHANNES ALO

IPC: C07C49/403 ,  C07C45/00 ,  C07C45/33 ,  C07C45/39 ,  C07C45/82 ,  C07C67/00 ,  C07C45/37

Abstract: An improved process for the preparation of cyclohexanone from benzene. Benzene is hydrogenated in a gaseous phase in a hydrogenation zone to form cyclohexane; cyclohexane is oxidized in a liquid phase to form a mixture containing cyclohexanol and cyclohexanone; and cyclohexanone is separated from this mixture and is catalytically dehydrogenated to form cyclohexanone and a hydrogen containing gas. The resulting hydrogen containing gas is introduced into a washing zone wherein it is washed with cyclohexane or benzene and the hydrogen gas thus purified is fed into the hydrogenation zone.