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公开(公告)号:DE59803261D1
公开(公告)日:2002-04-11
申请号:DE59803261
申请日:1998-11-27
Applicant: BASF AG
Inventor: HEINEKE DR , SCHWAB DR , FISCHER DR , SCHMID DR , BAEUMLE MONIKA
Abstract: Colloidal palladium for hydrogenating olefins, acetylene, dienes and (un)saturated nitriles consists of palladium clusters having an average particle size of 0.2-2.0 nm. At least 80% of the palladium clusters have a particle diameter which deviates not more than 0.2 nm from the average particle diameter. The clusters have protective ligands on the surface. Independent claims are also included for: (1) production of a palladium colloidal solution by reacting a palladium salt with a reductant made of 4-30 C alcohol, and a protective ligand of phosphane and/or aromatic nitrogen compound at 0-300o C; (2) production of colloidal palladium comprising forming the above palladium colloidal solution, precipitating the colloidal palladium by adding a hydrocarbon solvent, removing the colloidal palladium, and drying; and (3) production of a palladium-containing heterogeneous catalyst by forming the palladium solution as above, impregnating a carrier selected from alumina, silicon dioxide, zirconium dioxide, titanium dioxide, carbon, zeolite and silicate.
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公开(公告)号:DE19753464A1
公开(公告)日:1999-06-10
申请号:DE19753464
申请日:1997-12-02
Applicant: BASF AG
Inventor: HEINEKE DANIEL DR , SCHWAB EKKEHARD DR , FISCHER MARTIN DR , SCHMID GUENTER DR , BAEUMLE MONIKA
IPC: B01J23/44 , B01J35/00 , B01J31/24 , B01J31/22 , C07C11/107 , C07C5/09 , C07B35/02 , C07B43/04 , C01G55/00
Abstract: Colloidal palladium for hydrogenating olefins, acetylene, dienes and (un)saturated nitriles consists of palladium clusters having an average particle size of 0.2-2.0 nm. At least 80% of the palladium clusters have a particle diameter which deviates not more than 0.2 nm from the average particle diameter. The clusters have protective ligands on the surface. Independent claims are also included for: (1) production of a palladium colloidal solution by reacting a palladium salt with a reductant made of 4-30 C alcohol, and a protective ligand of phosphane and/or aromatic nitrogen compound at 0-300o C; (2) production of colloidal palladium comprising forming the above palladium colloidal solution, precipitating the colloidal palladium by adding a hydrocarbon solvent, removing the colloidal palladium, and drying; and (3) production of a palladium-containing heterogeneous catalyst by forming the palladium solution as above, impregnating a carrier selected from alumina, silicon dioxide, zirconium dioxide, titanium dioxide, carbon, zeolite and silicate.
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