초록 ▼

The invention relates to a method for desulfurizing naphtha boiling-range hydrocarbons such as cracked naphtha. More particularly, the invention relates to hydrotreating the naphtha under selective hydrotreating conditions, and then removing mercaptans from the hydrotreater effluent using a caustic

The invention relates to a method for desulfurizing naphtha boiling-range hydrocarbons such as cracked naphtha. More particularly, the invention relates to hydrotreating the naphtha under selective hydrotreating conditions, and then removing mercaptans from the hydrotreater effluent using a caustic extractant.

대표청구항 ▼

1. A naphtha desulfurization method, comprising:(a) contacting a sulfur-containing naphtha with hydrogen in the presence of a catalytically effective amount of a hydrotreating catalyst under catalytic hydrotreating conditions to form a hydrodesulfurized naphtha; (b) contacting the hydrodesulfurized

1. A naphtha desulfurization method, comprising:(a) contacting a sulfur-containing naphtha with hydrogen in the presence of a catalytically effective amount of a hydrotreating catalyst under catalytic hydrotreating conditions to form a hydrodesulfurized naphtha; (b) contacting the hydrodesulfurized naphtha with a first phase of a treatment composition containing water, alkali metal hydroxide, cobalt phthalocyanine sulfonate, and alkylphenols and having at least two phases, (i) the first phase containing dissolved alkali metal alkylphenylate, dissolved alkali metal hydroxide, water, and dissolved sulfonated cobalt phthalocyanine, and (ii) the second phase containing water and dissolved alkali metal hydroxide; (c) extracting mercaptan sulfur from the hydrodesulfurized naphtha to the first phase; and (d) separating an upgraded naphtha having less mercaptan sulfur than the hydrodesulfurized naphtha. 2. The method of claim 1 wherein, during the contacting of step (b), the first phase is applied to and flows over and along hydrophylic metal fibers, and the hydrocarbon flows over the first phase co-current with first phase flow.3. The method of claim 2 wherein the mercaptans are reversion mercaptans.4. The method of claim 3 wherein the reversion mercaptans have a molecular weight greater than about C4.5. The method of claim 4 wherein the reversion mercaptans have a molecular weight ranging from about C5 to about C8.6. The method of claim 1 wherein the sulfonated cobalt phthalocyanine is present in the first phase in an amount ranging from about 10 to about 500 wppm, based upon the weight of the treatment solution.7. The method of claim 1 wherein the treatment composition contains about 15 wt. % to about 55 wt. % dissolved alkylphenols, about 10 wppm to about 500 wppm dissolved sulfonated cobalt phthalocyanine, about 25 wt. % to about 60 wt. % dissolved alkali metal hydroxide, and about 10 wt. % to about 50 wt. % water, based on the weight of the treatment solution.8. The method of claim 7 wherein the first phase is present in step (b) in an amount ranging from about 3 vol. % to about 100 vol. %, based on the volume of the hydrodesulfurized naphtha, and the contacting is conducted in the substantial absence of oxygen.9. The method of claim 1 wherein at least a portion of the alkylphenols are cresols obtained from the hydrodesulfurized naphtha.10. The method of claim 1 wherein the sulfonated cobalt phthalocyanine is cobalt phthalocyanine disulfonate.11. The method of claim 1 further comprising conducting an oxidizing amount oxygen and the first phase from step (c) to an oxidizing region and oxidizing the mercaptan sulfur in the first phase to disulfides, separating the disulfides from the first phase, and then conducting the first phase to a polishing region wherein a water-immiscible solvent further separates disulfides from the first phase, wherein the contacting of step (b) is conducted under substantially anaerobic conditions.12. The method of claim 11 further comprising conducting the second phase from step (b) to a concentrating region wherein water is removed from the second phase to regulate the treatment composition's water content; and conducting the concentrated second phase from the concentrating region to the second phase of step (b) for re-use.13. The method of claim 12 wherein the treatment composition is formed by combining water in an amount ranging from about 10 wt. % to about 50 wt. %, alkali metal hydroxide in an amount ranging from about 25 wt. % to about 60 wt. %, sulfonated cobalt phthalocyanine in an amount ranging from about 10 wppm to about 500 wppm, and alkylphenols in an amount ranging from about 10 wt. % to about 50 wt. %, based on the weight of the treatment composition.14. The method of claim 13 wherein(i) the hydrocarbon is a selectively hydrotreated naphtha containing reversion mercaptans, (ii) at least a portion of the alkylphenols are cresols obtained from the selectively hydrotreated naphtha, (iii) wherein the reversion mercaptans have a molecular weight greater than about C5, (iv) the sulfonated cobalt pthalocyanine is cobalt pthalocyanine disulfonate, and (v) wherein the method is operated continuously. 15. A continuous method for treating and upgrading a selectively hydrotreated naphtha, comprising:(a) contacting a selectively hydrotreated naphtha under substantially anaerobic conditions with an extractant composition, wherein (i) the extractant is substantially immiscible with its analogous bottom phase of aqueous alkali metal hydroxide, and (ii) the extractant contains water, dissolved alkali metal alkylphenylate, dissolved alkali metal hydroxide, and dissolved sulfonated cobalt phthalocyanine; (b) extracting mercaptan sulfur from the naphtha to the extractant; (c) separating (i) an extractant containing mercaptan sulfur and (ii) an upgraded naphtha having less mercaptan sulfur than the selectively hydrotreated naphtha. 16. The method of claim 15 wherein the naphtha contains reversion mercaptans having a molecular weight greater than about C4.17. The method of claim 16 wherein the reversion mercaptans have a molecular weight greater ranging from about C5 to about C8. 18. The method of claim 15 wherein, during the contacting of step (a), the extractant is applied to and flows over and along hydrophylic metal fibers, and the selectively hydrotreated naphtha flows over the extractant co-current with the flow of extractant.19. The method of claim 15 wherein the extractant composition is formed by combining water in an amount ranging from about 10 wt. % to about 50 wt. %, alkali metal hydroxide in an amount ranging from about 25 wt. % to about 60 wt. %, sulfonated cobalt phthalocyanine in an amount ranging from about 10 ppm to about 500 ppm, and alkylphenols in an amount ranging from about 10 wt. % to about 50 wt. %, based on the weight of the extractant, and wherein at least a portion of the alkyl phenols are cresols obtained from the selectively hydrotreated naphtha.20. The method of claim 19 wherein the extractant is present in an amount ranging from about 3 vol. % to about 100 vol. %, based on the volume of the hydrocarbon, and wherein the extractant contains dissolved alkali metal hydroxide in an amount ranging from about 1 wt. % to about 40 wt. %, dissolved alkali metal alkylphenylate ions in an amount ranging from about 10 wt. % to about 95 wt. %, and sulfonated cobalt pthalocyanine in an amount ranging from about 10 ppm to about 500 ppm, based on the weight of the extractant.21. The method of claim 20 wherein the sulfonated cobalt phthalocyanine is cobalt phthalocyanine disulfonate.22. The method of claim 15 further comprising(d) conducting an oxidizing amount oxygen and the extractant containing mercaptan sulfur to an oxidizing region and oxidizing the mercaptan sulfur to disulfides; (e) separating the disulfides from the extractant; (f) conducting at least a portion of the extractant in step (e) to a polishing region, wherein a water-immiscible solvent further separates disulfides from the extractant prior to the re-use of the extractant. 23. The method of claim 22 further comprising(g) conducting the bottom phase from step (a) to a concentrating region wherein water is removed from the bottom phase to regulate the extractant's water content; and then (h) conducting the bottom phase away from the concentrating region to step (a) for re-use. 24. The method of claim 23 wherein(i) the hydrocarbon is a selectively hydrotreated naphtha containing reversion mercaptans and cresols, (ii) the extractant contains alkylphenols obtained from the cresols in the selectively hydrotreated naphtha, (iii) wherein the reversion mercaptans have a molecular weight greater than about C5, and (iv) the sulfonated cobalt pthalocyanine is cobalt pthalocyanine disulfonate.