Process for regenerating a catalyst
View Patent ↗A process for regenerating one or more deactivated cobalt comprising Fischer-Tropsch catalyst particle(s), comprising the steps of: (i) oxidizing the catalyst particle(s) at a temperature between 20 and 400° C.; (ii) treating the catalyst particle(s) for more than 5 minutes with a solvent, which solvent comprises an amine, (iii) drying the catalyst particle(s); and (iv) optionally reducing the catalyst particle(s) with hydrogen or a hydrogen comprising gas. This process may be preceded by a step in which Fischer-Tropsch product is removed from the catalyst particle(s).
1. A process for regenerating one or more cobalt comprising Fischer-Tropsch catalyst particles in situ in a reactor tube, said catalyst particle(s) having been deactivated by use in a Fischer-Tropsch process, said process for regenerating comprising the steps of:
(i) oxidising the catalyst particle(s) at a temperature between 20 and 400° C.;
(ii) treating the catalyst particle(s) for more than 5 minutes with a solvent, which solvent comprises ammonium carbonate and an amine selected from the group consisting of methylamine, ethylamine, propylamine, butylamine and mixtures thereof;
(iii) drying the catalyst particle(s); and
(iv) reducing the catalyst particle(s) with hydrogen or a hydrogen comprising gas.
2. The process according to claim 1 , wherein treatment step (ii) comprises the steps of:
(ii)a filling pores of the catalyst particle(s) with a solvent at a temperature in the range of from 5 to 40° C. using a pore fill method;
(ii)b leaving the solvent in the pores for more than 5 minutes at a temperature between 5 and 90° C.
3. The process according to claim 1 , wherein the catalyst particle(s) is/are reduced with hydrogen or a hydrogen comprising gas after the oxidation step and before the treatment step (ii).
4. The process according to claim 1 , wherein the solvent used in step (ii) additionally comprises one or more chemical compounds chosen from the group consisting of nitric acid, weak organic acids, ammonium salts, and alkyl ammonium salts.
5. The process according to claim 1 , wherein the solvent used in step (ii) comprises ammonium carbonate and methylamine.
6. The process according to claim 1 , wherein the solvent used in step (ii) comprises a mixture of ammonium carbonate, methyl amine and water.
7. The process according to claim 1 , wherein the solvent used in step (ii) comprises a mixture of ammonium carbonate, methyl amine and water, with a weight ratio of the methylamine to the ammonium carbonate in the range of from 1:0.25 to 1:2, and/or with a weight ratio of the ammonium carbonate to water in the range of from 1:0.5 to 1:4, and/or with a weight ratio of the methylamine to water in the range of from 1:0.25 to 1:4.
8. The process according to claim 1 , wherein the catalyst particle(s) is/are fixed bed particle(s) larger than 1 mm or immobilised slurry particle(s) larger than 1 mm.
9. The process according to claim 8 , wherein at least 20% of the catalyst particle(s) is treated, and whereby the at least 20% of the catalyst particle(s) is located at a downstream end of the reactor tube and is subjected to step (ii).
10. A process for regenerating one or more cobalt comprising Fischer-Tropsch catalyst particles, said catalyst particle(s) having been deactivated by use in a Fischer-Tropsch process in a reactor tube, said process for regenerating comprising the steps of:
(a) oxidising the catalyst particle(s) in the reactor tube at a temperature between 20 and 400° C.;
(b) unloading the catalyst particle(s) from the reactor tube;
(c) treating catalyst particle(s) for more than 5 minutes with a solvent, which solvent comprises ammonium carbonate and an amine selected from the group consisting of methylamine, ethylamine, propylamine, butylamine and mixtures thereof;
(d) drying and optionally heating the catalyst particle(s).
11. The process according to claim 10 , wherein treatment step (c) comprises the steps of:
(c)I filling pores of the catalyst particle(s) with a solvent at a temperature in the range of from 5 to 40° C. using a pore fill method;
(c)II leaving the solvent in the pores for more than 5 minutes at a temperature between 5 and 90° C.
12. The process according to claim 10 , wherein the catalyst particle(s) is/are reduced with hydrogen or a hydrogen comprising gas after the oxidation step and before the treatment step (c).
13. The process according to claim 10 , wherein the solvent used in step (a) additionally comprises one or more chemical compounds chosen from the group consisting of nitric acid, weak organic acids, ammonium salts, and alkyl ammonium salts.
14. The process according to claim 10 , wherein the solvent used in step (c) comprises ammonium carbonate and methylamine.
15. The process according to claim 10 , wherein the solvent used in step (c) comprises a mixture of ammonium carbonate, methyl amine and water.
16. The process according to claim 10 , wherein the solvent used in step (c) comprises a mixture of ammonium carbonate, methyl amine and water, with a weight ratio of the methylamine to the ammonium carbonate in the range of from 1:0.25 to 1:2, and/or with a weight ratio of the ammonium carbonate to water in the range of from 1:0.5 to 1:4, and/or with a weight ratio of the methylamine to water in the range of from 1:0.25 to 1:4.
17. The process according to claim 10 , wherein the catalyst particle(s) is/are fixed bed particle(s) larger than 1 mm or immobilised slurry particle(s) larger than 1 mm.
18. The process according to claim 17 , wherein at least 20% of the catalyst particle(s) is treated, and whereby the at least 20% of the catalyst particle(s) is located at a downstream end of the reactor tube and is subjected to step (c).