IPC분류정보
국가/구분 |
United States(US) Patent
등록
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국제특허분류(IPC7판) |
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출원번호 |
UP-0014406
(2004-12-16)
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등록번호 |
US-7837863
(2011-01-22)
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발명자
/ 주소 |
- Bhan, Opinder Kishan
- Wellington, Scott Lee
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출원인 / 주소 |
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인용정보 |
피인용 횟수 :
0 인용 특허 :
171 |
초록
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Contact of a crude feed with one or more catalysts produces a total product that include a crude product. The crude feed has a total content of alkali metal, and alkaline-earth metal, in metal salts of organic acids of at least 0.00001 grams per gram of crude feed. At least one of the catalysts incl
Contact of a crude feed with one or more catalysts produces a total product that include a crude product. The crude feed has a total content of alkali metal, and alkaline-earth metal, in metal salts of organic acids of at least 0.00001 grams per gram of crude feed. At least one of the catalysts includes vanadium. The crude product is a liquid mixture at 25° C. and 0.101 MPa and has a total content of alkali metal, and alkaline-earth metal, in metal salts of organic acids of at most 90% of the total content of alkali metal, and alkaline-earth metal, in metal salts of organic acids of the crude feed. One or more other properties of the crude product may be changed by at least 10% relative to the respective properties of the crude feed.
대표청구항
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What is claimed is: 1. A method of producing a crude product, comprising: providing at least one catalyst comprising vanadium, one or more compounds of vanadium, or mixtures thereof; and contacting a crude feed with the catalyst comprising vanadium, one or more compounds of vanadium, or mixtures th
What is claimed is: 1. A method of producing a crude product, comprising: providing at least one catalyst comprising vanadium, one or more compounds of vanadium, or mixtures thereof; and contacting a crude feed with the catalyst comprising vanadium, one or more compounds of vanadium, or mixtures thereof, to produce a total product that includes the crude product, wherein the crude product is a liquid mixture at 25.degree. C. and 0.101 MPa, the crude feed comprising one or more alkali metal salts of one or more organic acids, one or more alkaline-earth metal salts of one or more organic acids, or mixtures thereof, and the crude feed having, per gram of crude feed, a total content of alkali metal, and alkaline-earth metal, in metal salts of organic acids of at least 0.00001 grams; and controlling contacting conditions such that the crude product has a total content of alkali metal, and alkaline-earth metal, in metal salts of organic acids of at most 90% of the content of alkali metal, and alkaline-earth metal, in metal salts of organic acids in the crude feed, wherein content of alkali metal, and alkaline-earth metal, in metal salts of organic acids is as determined by ASTM Method D1318 wherein the catalyst comprises in addition an additional catalyst and the additional catalyst has a pore size distribution of at least 180.ANG. 2. The method of claim 1, wherein at least one of the alkali metals is lithium. 3. The method of claim 1, wherein at least one of the alkali metals is sodium. 4. The method of claim 1, wherein at least one of the alkali metals is potassium. 5. The method of claim 1, wherein at least one of the alkaline-earth metals is magnesium. 6. The method of claim 1, wherein at least one of the alkaline-earth metals is calcium. 7. The method of claim 1, wherein the metals are lithium, sodium, potassium, magnesium, calcium, or mixtures thereof. 8. The method of claim 1, wherein the crude feed comprises in addition at least one zinc salt of an organic acid. 9. The method of claim 1, wherein the crude feed comprises in addition at least one arsenic salt of an organic acid. 10. The method of claim 1, wherein the vanadium catalyst comprises one or more metals from Column 6 of the Periodic Table, one or more compounds of one or more metals from Column 6 of the Periodic Table, or mixtures thereof. 11. The method of claim 1, wherein the vanadium catalyst comprises one or more metals from Columns 6-10 of the Periodic Table, one or more compounds of one or more metals from Columns 6-10 of the Periodic Table, or mixtures thereof. 12. The method of claim 1, wherein the vanadium catalyst comprises one or more elements from Column 15 of the Periodic Table, one or more compounds of one or more elements from Column 15 of the Periodic Table, or mixtures thereof. 13. The method of claim 1, wherein the vanadium catalyst comprises molybdenum, one or more compounds of molybdenum, or mixtures thereof. 14. The method of claim 1, wherein the vanadium catalyst comprises tungsten, one or more compounds of tungsten, or mixtures thereof. 15. The method of claim 1, wherein the vanadium catalyst comprises nickel, one or more compounds of nickel, cobalt, one or more compounds of cobalt, or mixtures thereof. 16. The method of claim 1, wherein the one or more catalysts comprise in addition an additional catalyst, the additional catalyst having a pore size distribution of at least 230 .ANG. 17. The method of claim 1, wherein the additional catalyst comprises one or more metals from Column 6 of the Periodic Table, one or more compounds of one or more metals from Column 6 of the Periodic Table, or mixtures thereof. 18. The method of claim 17, wherein contacting comprises contacting the crude feed with the additional catalyst subsequent to contact with the vanadium catalyst. 19. The method of claim 1, wherein the additional catalyst comprises one or more metals from Column 5 of the Periodic Table, one or more compounds of one or more metals from Column 5 of the Periodic Table, or mixtures thereof. 20. The method of claim 1, wherein the additional catalyst comprises one or more metals from Column 6 of the Periodic Table, one or more compounds of one or more metals from Column 6 of the Periodic Table, or mixtures thereof; and one or more metals from Columns 7-10 of the Periodic Table, one or more compounds of one or more metals from Columns 7-10 of the Periodic Table, or mixtures thereof. 21. The method of claim 1, wherein the additional catalyst comprises one or more metals from Column 6 of the Periodic Table, one or more compounds of one or more metals from Column 6 of the Periodic Table, or mixtures thereof; one or more metals from Columns 7-10 of the Periodic Table, one or more compounds of one or more metals from Columns 7-10 of the Periodic Table, or mixtures thereof; and one or more elements from Column 15 , one or more compounds of one or more elements from Column 15 , or mixture thereof. 22. The method of claim 1, wherein the crude feed has a sulfur content, expressed in grams of sulfur per gram of crude feed, and the contacting conditions are also controlled such that the crude product has a sulfur content of about 70% to about 130% of the sulfur content of the crude feed, wherein sulfur content is as determined by ASTM Method D4294. 23. The method of claim 1, wherein the contacting conditions are also controlled such that the crude product has a viscosity at 37.8.degree. C. of at most 90% of the viscosity of the crude feed at 37.8.degree. C., wherein viscosity is as determined by ASTM Method D445. 24. The method of claim 1, wherein the contacting conditions are also controlled such that the crude product has an API gravity of about 70% to about 130% of an API gravity of the crude feed, wherein API gravity is as determined by ASTM Method D6822. 25. The method of claim 1, wherein the crude feed has a vacuum gas oil (VGO) content of at least 0.001 grams of VGO per gram of crude feed, and the contacting conditions are also controlled such that the crude product has a VGO content of about 70% to about 130% of the VGO content of the crude feed. 26. The method of claim 1, wherein the crude feed has a residue content of at least 0.1 grams of residue per gram of crude feed, and the contacting conditions are also controlled such that the crude product has a residue content of about 70% to about 130% of the residue content of the crude feed, wherein residue content is as determined by ASTM Method D5307. 27. The method of claim 1, wherein the crude feed is contacted in a contacting zone that is on or coupled to an offshore facility. 28. The method of claim 1, wherein contacting comprises contacting the crude feed in the presence of a hydrogen source and/or an inert gas. 29. The method of claim 1, wherein the method further comprises combining the crude product with a crude that is the same as or different from the crude feed to form a blend suitable for transportation and/or treatment facilities. 30. The method of claim 1, wherein the method further comprises processing the crude product to produce transportation fuel. 31. A method of producing transportation fuel, comprising: processing a crude product, wherein the crude product is obtainable by: providing at least one catalyst comprising vanadium, one or more compounds of vanadium, or mixtures thereof; and contacting a crude feed with the catalyst comprising vanadium, one or more compounds of vanadium, or mixtures thereof, to produce a total product that includes the crude product, wherein the crude product is a liquid mixture at 25.degree. C. and 0.101 MPa, the crude feed comprising one or more alkali metal salts of one or more organic acids, one or more alkaline-earth metal salts of one or more organic acids, or mixtures thereof, and the crude feed having, per gram of crude feed, a total content of alkali metal, and alkaline-earth metal, in metal salts of organic acids of at least 0.00001 grams; and controlling contacting conditions such that the crude product has a total content of alkali metal, and alkaline-earth metal, in metal salts of organic acids of at most 90% of the content of alkali metal, and alkaline-earth metal, in metal salts of organic acids in the crude feed, wherein content of alkali metal, and alkaline-earth metal, in metal salts of organic acids is as determined by ASTM Method D1318 wherein the catalyst comprises in addition an additional catalyst and the additional catalyst has a pore size distribution of at least 180 .ANG. 32. The method of claim 31, wherein the processing comprises distilling the crude product into one or more distillate fractions. 33. The method of claim 31, wherein the processing comprises hydrotreating.
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