Process for preparing a hydrotreating catalyst
View Patent ↗Process for preparing a hydrotreating catalyst comprising of from 5 wt % to 50 wt % of molybdenum, of from 0.5 wt % to 20 wt % of nickel and of from 0 to 5 wt % of phosphorus, all based on total dry weight of catalyst, which process comprises (a) treating alumina carrier with molybdenum and nickel and of from 1 to 60% wt of gluconic acid, based on weight of carrier, and optionally phosphorus, (b) optionally drying the treated carrier at a temperature of from 40 to 200° C., and (c) calcining the treated and optionally dried carrier at a temperature of from 200 to 650° C. to obtain the calcined treated carrier.
1. A process for preparing a hydrotreating catalyst, wherein the hydrotreating catalyst comprises from 5 wt % to 50 wt % molybdenum, from 0.5 wt % to 20 wt % nickel, and from 0 to 5 wt % phosphorus, all based on total dry weight of catalyst, which process comprises:
impregnating an alumina carrier with an impregnation solution, consisting essentially of a phosphorus compound, a molybdenum component, a nickel component, and gluconic acid that is present in the impregnation solution in such an amount to provide a ratio of weight of gluconic acid to the total weight of nickel and molybdenum of from 0.1 to 5, and a phosphorus compound, to thereby provide an impregnated carrier;
drying the impregnated carrier at a temperature of from 40 to 200° C. followed by calcining the impregnated carrier at a temperature of from 200 to 650° C. to obtain a calcined impregnated carrier; and
sulphiding the calcined impregnated carrier to obtain the hydrotreating catalyst.
2. A process according to claim 1 , wherein the amount of gluconic acid in the hydrotreating catalyst is of from 2 to 40% wt, based on total dry weight of the alumina carrier.
3. A process according to claim 2 , wherein the amount of phosphorus in the hydrotreating catalyst is of from 1.5 to 3.5% wt, based on total dry weight of hydrotreating catalyst.
4. A process according to claim 1 , wherein the hydrotreating catalyst comprising from 1 wt % to 15 wt % nickel, of from 8 wt % to 40 wt % molybdenum and of from 0.1 to 5 wt % phosphorus, all metal based on total dry weight of hydrotreating catalyst.
5. A process according to claim 4 , in which the alumina of the alumina carrier is gamma alumina.
6. A process for hydrotreating a sulphur-containing hydrocarbon feedstock, which process comprises: contacting the hydrocarbon feedstock at a hydrogen partial pressure from 1 to 70 bar and a temperature of from 200 to 420° C. with a catalyst obtained according to claim 4 .
7. A process for hydrotreating a sulphur-containing hydrocarbon feedstock, which process comprises: contacting the hydrocarbon feedstock at a hydrogen partial pressure from 1 to 70 bar and a temperature of from 200 to 420° C. with a catalyst obtained according to claim 1 .
8. A process according to claim 1 , wherein the gluconic acid concentration of the impregnation solution is such to provide the ratio of gluconic acid to total weight of nickel and molybdenum is of from 0.3 to 2.5.
9. A process according to claim 1 , wherein the gluconic acid concentration of the impregnation solution is such to provide the ratio of gluconic acid to total weight of nickel and molybdenum is of from 0.5 to 2.
10. A process according to claim 9 , wherein the amount of gluconic acid in the impregnated carrier is of from 3 to 30% wt, based on the total dry weight of the alumina carrier.
11. A process according to claim 10 , wherein the hydrotreating catalyst comprising from 2 wt % to 12 wt % nickel, of from 10 wt % to 30 wt % molybdenum and of from 0.2 to 5 wt % phosphorus, all metal based on total dry weight of hydrotreating catalyst.
12. A process for hydrotreating a sulphur-containing hydrocarbon feedstock, which process comprises: contacting the hydrocarbon feedstock at a hydrogen partial pressure from 1 to 70 bar and a temperature of from 200 to 420° C. with a catalyst obtained according to claim 11 .
13. A process according to claim 1 , wherein the gluconic acid concentration of the impregnation solution is such to provide the ratio of gluconic acid to total weight of nickel and molybdenum is of from 0.7 to 1.5.
14. A process according to claim 13 , wherein the amount of gluconic acid in the impregnated carrier is of from 4 to 20% wt, based on the total dry weight of the alumina carrier.
15. A process according to claim 14 , wherein the hydrotreating catalyst comprising from 2 wt % to 12 wt % nickel, of from at least 11 wt % to 30 wt % molybdenum and of from 0.5 to 4.5 wt % phosphorus, all metal based on total dry weight of hydrotreating catalyst.
16. A process for hydrotreating a sulphur-containing hydrocarbon feedstock, which process comprises: contacting the hydrocarbon feedstock at a hydrogen partial pressure from 1 to 70 bar and a temperature of from 200 to 420° C. with a catalyst obtained according to claim 15 .