Method for preparing a catalyst comprising an active nickel phase distributed in a shell via hexanol impregnation
A process for preparing a catalyst comprising an active nickel phase and an alumina support, said catalyst comprising between 1% and 50% by weight of elemental nickel relative to the total weight of the catalyst, the nickel being distributed both over a crust at the periphery of the support, and at the core of the support, which process comprises the following steps: a) said support is impregnated with a volume V1 of a hexanol solution of between 0.2 and 0.8 times the total pore volume TPV of said support in order to obtain an impregnated support; b) the impregnated support obtained at the end of step a) is impregnated with a solution comprising a precursor of the nickel active phase in order to obtain a catalyst precursor; c) the catalyst precursor obtained at the end of step b) is dried at a temperature below 250° C.
1 . A process for preparing a catalyst comprising an active phase based on nickel and alumina support, said catalyst comprising between 1% and 50% by weight of elemental nickel relative to the total weight of the catalyst, the nickel being distributed both over a crust at the periphery of the support, and at the core of the support, the thickness of said crust being between 2% and 15% of the diameter of the catalyst, the size of the nickel particles in the catalyst, measured in oxide form, being less than 15 nm, which process comprises the following steps:
a) said support is impregnated with a volume V1 of a hexanol solution of between 0.2 and 0.8 times the total pore volume TPV of said support in order to obtain an impregnated support;
b) the impregnated support obtained at the end of step a) is impregnated with a solution comprising at least one precursor of the nickel active phase in order to obtain a catalyst precursor;
c) the catalyst precursor obtained at the end of step b) is dried at a temperature below 250° C.
2 . The process as claimed in claim 1 , wherein, in step b), the volume V2 of the solution comprising at least one precursor of the nickel active phase impregnated on the impregnated support obtained at the end of step a) is such that V2=TPV−V1.
3 . The process as claimed in claim 1 , wherein step c) is carried out for a time of between 0.5 hour and 12 hours.
4 . The process as claimed in claim 1 , further comprising a step d) in which the catalyst obtained at the end of step c) is calcined at a temperature of between 250° C. and 600° C.
5 . The process as claimed in claim 4 , wherein step d) is carried out for between 0.5 hour and 24 hours.
6 . The process as claimed in claim 1 , wherein, in step a), said volume V1 of said hexanol solution is between 0.25 and 0.75 times the total pore volume TPV of said support.
7 . The process as claimed in claim 1 , wherein, in step a), the hexanol solution is an n-hexanol solution.
8 . The process as claimed in claim 1 , wherein a further step b1) is carried out in which either the impregnated support obtained at the end of step a), or the catalyst precursor obtained at the end of step b), is impregnated with at least one solution containing at least one organic compound comprising at least one carboxylic acid function, or at least one alcohol function, or at least one ester function, or at least one amide function, or at least one amine function, steps b) and b1) being carried out in any order, or simultaneously.
9 . The process as claimed in claim 8 , wherein the volume V2 of the solution comprising at least one precursor of the active nickel phase and the volume V3 of the solution comprising at least one organic compound which are impregnated on the impregnated support obtained at the end of step a) are such that V2+V3=TPV−V1.
10 . The process as claimed in claim 8 , wherein the steps b) and b1) are carried out simultaneously.
11 . The process as claimed in claim 10 , wherein the volume V2′ of the solution comprising at least one precursor of the active nickel phase and at least one organic compound which are impregnated on the impregnated support obtained at the end of step a) is such that V2′=TPV−V1.
12 . The process as claimed in claim 8 , wherein the mole ratio of said organic compound introduced in step b1) to the nickel element introduced in step b) is between 0.01 and 5.0 mol/mol.
13 . The process as claimed in claim 8 , wherein the organic compound of step b1) is oxalic acid, malonic acid, glycolic acid, lactic acid, tartronic acid, citric acid, tartaric acid, pyruvic acid, levulinic acid, ethylene glycol, propane-1,3-diol, butane-1,4-diol, glycerol, xylitol, mannitol, sorbitol, diethylene glycol, glucose, gamma-valerolactone, dimethyl carbonate, diethyl carbonate, formamide, N-methylformamide, acetamide, N-methylacetamide, N, N-dimethylmethanamide, 2-pyrrolidone, γ-lactam, lactamide, urea, alanine, arginine, lysine, proline, serine, and/or EDTA.
14 . The process as claimed in claim 1 , wherein a further step a1) is carried out in which the impregnated support obtained at the end of step a) is left to mature for 0.5 hour to 40 hours.
15 . The process as claimed in claim 8 , wherein the nickel particles in the catalyst have a size, measured in oxide form, which is less than 13 nm.