Patent EA-001167-B1 (EA)
Title: Process for increasing the activity of zeolite containing particulate solids
Inventor: DAVIS ROBERT E
IPC: B01J38/48
Filed: 1996-12-20
Abstract: 1. A process for increasing the activity of a zeolite-containing particulate solid containing contaminants which block the pores of the zeolite and adversely affect the activity of the solid, which process comprises: a) forming a slurry of said particulate solid with a liquid containing at least one activating agent selected from the group consisting of acids, enzymes and surfactants, said agent being effective to solubilize or dislodge the contaminants; b) agitating said slurry in a contactor under activation conditions, including a temperature and a time sufficient to solubilize or dislodge the contaminants, so that the resulting solubilized or dislodged contaminants are carried by the liquid from the resulting particulate solid; c) separating the resulting particulate solid from the liquid carrying the solubilized or dislodged contaminants in the contactor; d) withdrawing from the contactor a portion of the liquid carrying the solubilized or dislodged contaminants; e) separating the resulting particulate solid from the separated liquid remaining in the slurry; f) washing the separated particulate solid to remove therefrom residual liquid containing said activating agent; and g) recovering a treated zeolite-containing particulate solid having a level of activity greater than the activity of the contaminated solid. 2. The process of claim 1, wherein the solubilized or dislodged contaminants are removed from an upper liquid level of the agitated slurry in admixture with said withdrawn liquid, the mixture is filtered to remove the contaminants, and the filtrate is recycled to the slurry. 3. The process of claim 1, wherein the agent is malic, acetic, maleic, citric, formic, oxalic, hydrochloric, nitric, or sulfuric acid, ammonium bifluoride, an enzyme, a detergent or a mixture of any of said agents. 4. A process for reactivating a spent zeolite-containing particulate catalyst containing carbonaceous deposits and one or more other contaminants which block the pores of the zeolite and adversely affect the catalytic activity thereof, which comprises: a) removing carbonaceous deposits from the spent catalyst by contacting the catalyst with an oxygen-containing gas under controlled oxidation conditions, b) cooling the resulting catalyst having a reduced level of carbonaceous deposits, c) forming a slurry of the cooled catalyst with an aqueous solution of an activating agent selected from the group consisting of acids, enzymes, and surfactants effective to solubilize or dislodge the contaminants; d) agitating said slurry in a contactor under activation conditions, including an elevated temperature and a time sufficient to solubilize or dislodge the contaminants, so that the resulting solubilized or dislodged contaminants are carried by the solution from the resulting catalyst; e) separating the resulting catalyst from the liquid carrying the solubilized or dislodged contaminants in the contactor; f). withdrawing a portion of the solution carrying the solubilized or dislodged contaminants from the slurry; g) separating the resulting catalyst from the solution remaining in the slurry; h) washing the separated catalyst to remove any residual solution; and i) recovering a treated zeolite-containing catalyst having a level of catalytic activity greater than that of the contaminated solid. 5. The process of claim 4, wherein the acid is malic, ammonium bifluoride, acetic, maleic, citric, formic, oxalic, hydrochloric, nitric, or sulfuric acid, or a mixture of any of said acids. 6. The process of claim 4, wherein the solubilized or dislodged contaminants are removed from the upper surface of the agitated slurry in admixture with said withdrawn solution, the mixture is filtered to remove the contaminants, and the filtrate is recycled to the slurry. 7. The process of claim 4, wherein said catalyst is fresh catalyst, equilibrium catalyst, or spent catalyst. 8. The process of claim 4, where the agitation is effected mechanically, by the introduction of a gas into the slurry, or a combination thereof. 9. The process of claim 4, where the elevated temperature is below 100 degree C, but not greater than the deactivation temperature of said agent. 10. The process of claim 4, wherein the zeolitic catalyst to be reactivated is a zeolitic catalyst continuously withdrawn from a hydrocarbon processing unit, and the reactivated catalyst is continuously returned to the hydrocarbon processing unit. 11. The process of claim 1, wherein the particulate solid is a zeolitic catalyst which is periodically withdrawn from a hydrocarbon processing unit, and the recovered treated catalyst is continuously returned to the hydrocarbon processing unit. 12. The process of claim 1, wherein the treated solid is subjected to a rare earth element exchange process to introduce one or more rare earth elements into the zeolite. 13. The process of claim 2, wherein the filtrate recycled to the slurry is pumped into a lower portion of the slurry and flows upwardly in the slurry. 14. The process of claim 6, wherein the filtrate recycled to the slurry is pumped into a lower portion of the slurry and flows upwardly in the slurry. 15. The process of 13, wherein an aeration medium is introduced into a lower portion of the slurry and flows upwardly in the slurry. 16. The process of claim 14, wherein an aeration medium is introduced into a lower portion of the slurry and flows upwardly in the slurry. 17. The process of claim 1, wherein the liquid contains an acid and a surfactant. 18. The process of claim 14, wherein the acqueous solution contains an acid and a surfacant. 19. The process of claim 17, wherein an aeration medium is introduced into a lower portion of the slurry, and the containinants are removed from an upper liquid level in the contactor. 20. The process of claim 18, wherein an aeration medium is introduced into a lower portion of the slurry, and the containinants are removed from an upper liquid level in the contactor. 21. The process of claim 1, wherein the liquid contains an acid and a surfactant; agitation of the slurry is effected by stirring and aeration; and the liquid carrying the solubilized or dislodged contaminants is withdrawn from an upper liquid level in the contactor. 22. The process of claim 4, wherein an aeration medium is introduced into a lower portion of the slurry, and the containinants are removed from an upper liquid level in the contactor.