[특허]Hydroprocessing catalysts and methods for making thereof

Chevron U.S.A. Inc.

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특허 상세정보

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Hydroprocessing catalysts and methods for making thereof

특허상세정보
국가/구분	United States(US) Patent 등록
국제특허분류(IPC7판)	C10G-047/26 C10G-047/32 C10G-047/36 C10G-065/00 C10G-065/10 C10G-065/18 C10G-047/00 C10G-047/02
출원번호	US-0233477 (2011-09-15)
등록번호	US-9068132 (2015-06-30)
발명자 / 주소	Yang, Shuwu Chabot, Julie Reynolds, Bruce Edward Kou, Bo
출원인 / 주소	Chevron U.S.A. Inc.
인용정보	피인용 횟수 : 0 인용 특허 : 74

초록

A method to reduce metal deposit in the hydroprocessing or upgrade of heavy oil feedstock is provided. The method comprises feeding an improved catalyst feed to the system, with the improved catalyst feed comprising a fresh slurry catalyst and a deoiled spent catalyst, with the deoiled spent catalyst being present in an amount of at least 10% the catalyst feed for the heavy oil upgrade system to have at least a 5% reduction in metal contaminant build-up compared to heavy oil upgrade system without the deoiled spent catalyst in the feed.

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1. A method to reduce deposit of at least a metal contaminant from a heavy oil feedstock in a system to upgrade the heavy oil feedstock, wherein the system to upgrade the heavy oil feedstock further comprises a catalyst feed system, the method comprising: (a) providing a fresh slurry catalyst having at least one metal selected from the group consisting of Group VIB, Group VIII and Group IIB and comprising a plurality of particles dispersed as a slurry in a hydrocarbon medium at a total metal concentration of 500 wppm to 3 wt. % of metals to heavy oil feedstock; and(b) providing a deoiled spent catalyst comprising a plurality of particles dispersed in a hydrocarbon medium as a slurry, wherein the deoiled spent catalyst has less than 80% but more than 10% of the original catalytic activity; and(c) combining the fresh slurry catalyst with the deoiled spent catalyst to form a total amount of slurry catalyst to the heavy oil upgrade system, wherein the dry weight ratio of fresh slurry catalyst to deoiled spent catalyst ranges from 1:5 to 5:1 and(d) contacting the heavy oil feedstock with the total amount of slurry catalyst to the heavy oil upgrade system under hydrocracking conditions to convert at least a portion of the heavy oil feedstock to lower boiling hydrocarbons, forming upgraded products; andwherein the deoiled spent catalyst is present in the catalyst feed system in an amount sufficient to reduce the deposit of the metal contaminant in the system to upgrade the heavy oil feedstock of at least 5% compared to an upgrade system without the deoiled spent catalyst. 2. The method of claim 1, wherein the amount of the deoiled spent catalyst present in the catalyst feed system is at least 10% of the total amount of slurry catalyst to the heavy oil upgrade system. 3. The method of claim 1, wherein the deoiled spent catalyst is present in the catalyst feed system at a dry weight ratio of fresh slurry catalyst to deoiled spent catalyst ranging from 1:5 to 5:1. 4. The method of claim 1, wherein the deoiled spent catalyst is present in an amount ranging from 20 to 75% of the total amount of catalyst in the catalyst feed system. 5. The method of claim 1, further comprising providing the total amount of catalyst to the heavy oil upgrade system to the catalyst feed system at a total concentration of 500 wppm to 3 wt. % of metals to heavy oil feedstock. 6. The method of claim 5, further comprising providing the total amount of catalyst to the heavy oil upgrade system to the catalyst feed system at a total concentration of 2000 wppm to 1.5 wt. % of metals to heavy oil feedstock. 7. The method of claim 1, wherein the deoiled spent catalyst of step (b) has more than 25% of the original catalytic activity. 8. The method of claim 1, wherein the deoiled spent catalyst of step (b) has more than 75% of the original catalytic activity. 9. The method of claim 1, wherein the deoiled spent catalyst of step (b) has more than 25% but less than 50% of the original catalytic activity. 10. The method of claim 1, wherein the deoiled spent catalyst of step (b) is slurried in the hydrocarbon medium at a weight ratio ranging from 1:1 to 1:25 of deoiled spent catalyst to hydrocarbon medium. 11. The method of claim 1, wherein the deoiled spent catalyst of step (b) is slurried in the hydrocarbon medium at a weight ratio ranging from 1:3 to 1:20 of deoiled spent catalyst to hydrocarbon medium. 12. The method of claim 1, wherein the deoiled spent catalyst of step (b) is slurried in the hydrocarbon medium at a weight ratio ranging from 1:5 to 1:10 of deoiled spent catalyst to hydrocarbon medium. 13. The method of claim 1, wherein the hydrocarbon medium of step (b) is selected from the group of vacuum gas oil, naphtha, medium cycle oil, light cycle oil , heavy cycle oil, solvent donor, aromatic solvent, and mixtures thereof. 14. The method of claim 1, wherein the deoiled spent catalyst comprises a first slurry catalyst that has been used in a hydroprocessing operation and contains less than 10 wt. % soluble hydrocarbons as unconverted heavy oil feed. 15. The method of claim 14, wherein the first slurry catalyst contains less than 2 wt. % soluble hydrocarbons as unconverted heavy oil feed. 16. The method of claim 14, wherein the first slurry catalyst has a solid content ranging from 5 to 50 wt. % in soluble hydrocarbons and having at least 50% of the soluble hydrocarbons removed in a deoiling step. 17. The method of claim 1, wherein the fresh slurry catalyst is prepared from at least a Group VIB metal precursor compound and optionally at least a Promoter metal precursor compound selected from Group VIII, Group IIB, Group IIA, Group IVA metals and combinations thereof. 18. The method of claim 1, wherein the fresh slurry catalyst further comprises a plurality of particles with a mean particle size ranging from 0.05 to 50 microns dispersed in a hydrocarbon medium. 19. The method of claim 1, wherein the deoiled spent catalyst and the fresh catalyst are combined into one feed stream for contacting the heavy oil feedstock. 20. The method of claim 1, wherein the catalyst feed system further comprises separate feed streams for contacting the deoiled spent catalyst and the fresh catalyst with the heavy oil feedstock. 21. The method of claim 1, wherein the deoiled spent catalyst further comprises a plurality of particles with a mean particle size ranging from 0.05 to 50 microns dispersed in a hydrocarbon medium. 22. The method of claim 1, wherein the deoiled spent catalyst is treated with a solution selected from the group of deionized water, a mineral acid, an oxidizing agent, and combinations thereof.

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Hydroprocessing catalysts and methods for making thereof

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Hydroprocessing catalysts and methods for making thereof

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