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In a desulfurization process for the removal of organosulfur compounds from a hydrocarbon fluid stream such as cracked-gasoline or diesel fuel wherein a bifunctional sorbent system is employed, surface treatment of the bifunctional sorbent during the use of same for desulfurization results in an ext

In a desulfurization process for the removal of organosulfur compounds from a hydrocarbon fluid stream such as cracked-gasoline or diesel fuel wherein a bifunctional sorbent system is employed, surface treatment of the bifunctional sorbent during the use of same for desulfurization results in an extension of the useful life of the bifunctional sorbent prior to the regeneration and reactivation of same for further use in the desulfurization of the hydrocarbon fluid stream.

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1. A process for enhancing the activity of a bifunctional sorbent composition to be used in desulfurization of a hydrocarbon fluid stream containing organosulfur compounds which comprises contacting the surface of said bifunctional sorbent composition with a reducing agent under conditions such that

1. A process for enhancing the activity of a bifunctional sorbent composition to be used in desulfurization of a hydrocarbon fluid stream containing organosulfur compounds which comprises contacting the surface of said bifunctional sorbent composition with a reducing agent under conditions such that sulfur deposits on the surface of the bifunctional sorbent are removed wherein said bifunctional sorbent is a composition comprising (a) a base component and (b) a promoter component wherein said base component comprises zinc oxide and said promoter component comprises a reduced metal selected from the group consisting of nickel, cobalt, iron, manganese, tungsten, silver, gold, copper, platinum, zinc, tin, ruthenium, molybdenum, antimony, vanadium, iridium, platinum, chromium and palladium.2. A process in accordance with claim 1 wherein the bifunctional sorbent has been removed from a desulfurization zone.3. A process in accordance with claim 2 wherein the resulting surface treated bifunctional sorbent is returned to said desulfurization zone following surface treatment of the bifunctional sorbent.4. A process in accordance with claim 1 wherein said reducing agent is hydrogen.5. A process in accordance with claim 4 wherein said bifunctional sorbent is surface treated with hydrogen at a temperature within a range of about 100° F. to about 1,000° F., a pressure within a range of about 15 psia to about 1500 psia and for a time sufficient to effect the removal of deposits on the surface of said composition.6. A process in accordance with claim 5 wherein said surface treatment is carried out for a period of time within a range of from about 1 to about 30 minutes.7. A process for the removal of organosulfur compounds from a hydrocarbon fluid stream which comprises:(a) contacting said stream with a bifunctional sorbent composition under conditions to produce a desulfurized hydrocarbon fluid stream and a sulfurized bifunctional sorbent; (b) removing the desulfurized fluid stream from said desulfurization zone; (c) passing at least a portion of the sulfurized bifunctional sorbent to a regeneration zone; (d) regenerating at least a portion of the sulfurized bifunctional sorbent in said regeneration zone to remove at least a portion of the sulfur thereon in order to restore the sulfur removal function of the bifunctional sorbent thus producing a desulfurized sorbent; (e) passing at least a portion of the desulfurized sorbent to an activation zone; (f) activating at least a portion of the desulfurized sorbent in the activation zone whereby the reduced valence state promoter metal content is reestablished and the promotional activity of the bifunctional sorbent composition so as to effect removal of organosulfur compounds from a hydrocarbon fluid stream when contacted with same; and thereafter (g) using at least a portion of the resulting desulfurized activated bifunctional sorbent composition for desulfurization of a hydrocarbon fluid stream, the improvement which comprises contacting the surface of said bifunctional sorbent composition with a reducing agent under conditions such that the deposits of the surface of said bifunctional sorbent composition are removed. 8. A process in accordance with claim 7 wherein the bifunctional sorbent being contacted with a reducing agent is one that has been removed from the desulfurization zone.9. A process in accordance with claim 8 wherein the resulting surface treated bifunctional sorbent is reintroduced to said desulfurization zone following the surface treatment of same.10. A process in accordance with claim 8 wherein said reducing agent is hydrogen.11. A process in accordance with claim 10 wherein said bifunctional sorbent composition is treated with hydrogen at a temperature in the range of 100° F. to about 1,000° F., a pressure in the range of about 15 to about 1500 psia and for a time sufficient to effect the removal of deposits from the surface of said bifunctional sorbent.12. A process in accordance with claim 11 wherein said surface treatment is carried out for a period of time within a range of from about 15 to about 30 hours.13. A process in accordance with claim 12 wherein said surface treatment remove sulfur deposits on the surface of said bifunctional sorbent.14. A process in accordance with claim 7 wherein said bifunctional sorbent is a composition comprising (a) a base component and (b) a promoter component wherein said base component comprises zinc oxide and said promoter component comprises a reduced metal selected from the group consisting of nickel, cobalt, iron, manganese, tungsten, silver, gold, copper, platinum, zinc, tin, ruthenium, molybdenum, antimony, vanadium iridium, platinum, chromium and palladium.15. A process for enhancing the activity of a bifunctional sorbent composition to be used in desulfurization of a hydrocarbon fluid stream containing organosulfur compounds which comprises contacting the surface of said bifunctional sorbent composition, wherein said bifunctional sorbent has been removed from a desulfurization zone, with a reducing agent under conditions such that sulfur deposits on the surface of the bifunctional sorbent are removed, and wherein the resulting surface treated bifunctional sorbent is returned to said desulfurization zone following surface treatment of said bifunctional sorbent.16. A process in accordance with claim 15 wherein said reducing agent is hydrogen.17. A process in accordance with claim 16 wherein said bifunctional sorbent is surface treated with hydrogen at a temperature within a range of about 100° F. to about 1,000° F., a pressure within a range of about 15 psia to about 1500 psia and for a time sufficient to effect the removal of deposits on the surface of said composition.18. A process in accordance with claim 17 wherein said surface treatment is carried out for a period of time within a range of from about 1 to about 30 minutes.19. A process for the removal of organosulfur compounds from a hydrocarbon fluid stream which comprises:(a) contacting said stream with a bifunctional sorbent composition under conditions to produce a desulfurized hydrocarbon fluid stream and a sulfurized bifunctional sorbent; (b) removing the desulfurized fluid stream from said desulfurization zone; (c) passing at least a portion of the sulfurized bifunctional sorbent to a regeneration zone; (d) regenerating at least a portion of the sulfurized bifunctional sorbent in said regeneration zone to remove at least a portion of the sulfur thereon in order to restore the sulfur removal function of the bifunctional sorbent thus producing a desulfurized sorbent; (e) passing at least a portion of the desulfurized sorbent to an activation zone; (f) activating at least a portion of the desulfurized sorbent in the activation zone whereby the reduced valence state promoter metal content is reestablished and the promotional activity of the bifunctional sorbent composition so as to effect removal of organosulfur compounds from a hydrocarbon fluid stream when contacted with same; and thereafter (g) using at least a portion of the resulting desulfurized activated bifunctional sorbent composition for desulfurization of a hydrocarbon fluid stream, the improvement which comprises contacting the surface of said bifunctional sorbent composition that has been removed from the desulfurization zone with a reducing agent under conditions such that the deposits of the surface of said bifunctional sorbent composition are removed and wherein the resulting surface treated bifunctional sorbent is reintroduced to said desulfurization zone following the surface treatment of same. 20. A process in accordance with claim 19 wherein said reducing agent is hydrogen.21. A process in accordance with claim 20 wherein said bifunctional sorbent composition is treated with hydrogen at a temperature in the range of 100° F. to about 1,000° F., a pressure in the range of about 15 to about 1500 psia and for a time sufficient to effect the removal of deposits from the surface of said bifunctional sorbent.22. A process in accordance with claim 21 wherein said surface treatment is carried out for a period of time within a range of from about 15 to about 30 hours.23. A process in accordance with claim 22 wherein said surface treatment remove sulfur deposits on the surface of said bifunctional sorbent.24. A process in accordance with claim 19 wherein said bifunctional sorbent is a composition comprising (a) a base component and (b) a promoter component wherein said base component comprises zinc oxide and said promoter component comprises a reduced metal selected from the group consisting of nickel, cobalt, iron, manganese, tungsten, silver, gold, copper, platinum, zinc, tin, ruthenium, molybdenum, antimony, vanadium iridium, platinum, chromium and palladium.25. A process for enhancing the activity of a bifunctional sorbent composition to be used in desulfurization of a hydrocarbon fluid stream containing organosulfur compounds which consists essentially of contacting the surface of said bifunctional sorbent composition wherein the bifunctional sorbent has been removed from a desulfurization zone with a reducing agent under conditions such that sulfur deposits on the surface of the bifunctional sorbent are removed and wherein the resulting surface treated bifunctional sorbent is returned to said desulfurization zone following surface treatment of the bifunctional sorbent.26. A process in accordance with claim 25 wherein said reducing agent is hydrogen.27. A process in accordance with claim 26 wherein said bifunctional sorbent is surface treated with hydrogen at a temperature within a range of about 100° F. to about 1,000° F., a pressure within a range of about 15 psia to about 1500 psia and for a time sufficient to effect the removal of deposits on the surface of said composition.28. A process in accordance with claim 27 wherein said surface treatment is carried out for a period of time within a range of from about 1 to about 30 minutes.