Process for preparing a transition metal-silicate catalyst
First Claim
1. A process for the preparation of a transition metal-silicate catalyst in which an insoluble, basic compound of a transition metal having an atomic number between 26 and 30 is precipitated with an alkaline precipitation agent from an aqueous solution of such a metal salt, as a suspension, which precipitate is allowed to mature in suspended form and is subsequently separated, dried and reduced, wherein, after the transition metal ions have been practically completely precipitated, soluble silicate is added.
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Abstract
The invention provides a process for the preparation of a transition metal-silicate catalyst in which an insoluble, basic compound of a transition metal having an atomic number between 26 and 30 (in particular nickel which has an atomic number of 28) is rapidly precipitated with an alkaline precipitation agent from an aqueous solution of such a metal salt, as a suspension, which precipitate is allowed to mature for a longer period in a suspended form, and, after the transition metal ions have been practically completely precipitated, soluble silicate is added to the suspension, after which the solids are separated from the liquid, optionally washed, dried and reduced.
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Citations
16 Claims
- 1. A process for the preparation of a transition metal-silicate catalyst in which an insoluble, basic compound of a transition metal having an atomic number between 26 and 30 is precipitated with an alkaline precipitation agent from an aqueous solution of such a metal salt, as a suspension, which precipitate is allowed to mature in suspended form and is subsequently separated, dried and reduced, wherein, after the transition metal ions have been practically completely precipitated, soluble silicate is added.
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16. A transition metal/transition metal silicate catalyst, which contains 30 to 70% of active metal, calculated on the total weight of the catalyst, wherein the active metal surface area is between 100 and 160 m2 /g in the case of nickel and between 1 and 25 m2 /g in the case of cobalt and copper, and wherein the BET total surface area and the pore volume are at least 20% higher and the filtration speed from the hydrogenated mixture is at least 5×
- that of a co-precipitated catalyst of the same composition.
Specification