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Heavy crude oils having high sulfur content and viscosities are upgraded by a hydrodesulfurization (HDS) process that includes microwave irradiation of a mixture of the sour heavy crude oil with at least one catalyst and optionally, one or more sensitizers, and irradiation in the presence of hydroge

Heavy crude oils having high sulfur content and viscosities are upgraded by a hydrodesulfurization (HDS) process that includes microwave irradiation of a mixture of the sour heavy crude oil with at least one catalyst and optionally, one or more sensitizers, and irradiation in the presence of hydrogen. The process is also adapted to microwave treatment of hard to break emulsions, either above ground or below ground where water-in-oil emulsions are initially formed, followed by the catalytic hydrodesulfurization promoted by application of further microwave energy to the demulsified crude oil stream.

대표청구항 ▼

1. A process for upgrading a sulfur-containing crude oil feedstream to improve the API gravity and reduce the sulfur content, the process comprising: a. mixing the crude oil with one or more hydrotreating catalysts to provide a catalyst-crude oil reaction mixture;b. irradiating the reaction mixture

1. A process for upgrading a sulfur-containing crude oil feedstream to improve the API gravity and reduce the sulfur content, the process comprising: a. mixing the crude oil with one or more hydrotreating catalysts to provide a catalyst-crude oil reaction mixture;b. irradiating the reaction mixture with microwave energy at a power level of from about 100 watts to about 10,000 watts for an exposure time of up to 30 minutes in the presence of hydrogen at a pressure ranging from one atmosphere to 300 psig to raise the temperature of the reaction mixture to a range of from 200° C. to 250° C.;c. maintaining the temperature of the reaction mixture for said exposure time to form a hydrodesulfurized mixture;d. separating the hydrodesulfurized mixture into a catalyst-containing solid phase and a liquid phase containing a hydrodesulfurized crude oil and sulfur-containing compounds; ande. recovering the hydrodesulfurized crude oil. 2. The process of claim 1, wherein the one or more catalysts is selected from the group consisting of powdered iron, palladium oxide, calcium oxide, an alkali metal oxide catalyst, traditional hydrotreating catalysts, and combinations thereof. 3. The process of claim 1, wherein the hydrotreating catalyst comprises at least one metal selected from Groups VIB and VIIIB of the Periodic Table. 4. The process of claim 3 in which the at least one metal is selected from the group consisting of iron, palladium, nickel, cobalt, chromium, vanadium, molybdenum, tungsten, a combination of metals such as nickel-molybdenum, cobalt-nickel-molybdenum, cobalt-molybdenum, nickel-tungsten and nickel-tungsten-titanium. 5. The process of claim 1 that includes adding a polar compound to the mixture of crude oil and catalyst in step (a). 6. The process of claim 5, wherein the polar compound is an ethanolamine. 7. The process of claim 1 which includes adding activated carbon to the mixture of step (a). 8. The process of claim 1, wherein the microwave energy is at a frequency of from about 200 MHz to about 10,000 MHz. 9. The process of claim 1, wherein the power level is from 500 watts to 5,000 watts and the exposure time is between 20 and 25 minutes. 10. The process of claim 1, wherein the reaction is carried out in a flow-through reactor at an hourly space velocity of the liquid phase that is in range of from 0.10 per hour to 10 per hour. 11. The process of claim 10, wherein the liquid phase hourly space velocity is in the range from 0.30 per hour to 3 per hour. 12. The process of claim 1 in which the crude oil feedstream includes both bound and free water, the process comprising the additional preliminary steps of: i. separating the crude oil feedstream into free water and a water-in-crude oil emulsion containing only bound water;ii. separating any free crude oil from the emulsion;iii. irradiating the emulsion with microwave energy to substantially break the emulsion;iv. separating the free water from the broken emulsion to provide oil containing less than 3% bound water, and thereafter performing steps (a)-(e). 13. The process of claim 1 in which a polar compound and microwave sensitizer is added to the mixture of crude oil and catalyst in step (a). 14. The process of claim 12, wherein the one or more catalysts is selected from the group consisting of powdered iron, palladium oxide, calcium oxide, an alkali metal oxide catalyst, traditional hydrotreating catalysts, and combinations thereof. 15. The process of claim 12, wherein the hydrotreating catalyst comprises at least one metal selected from Groups VIB and VIIIB of the Periodic Table. 16. The process of claim 15 in which the at least one metal is selected from the group consisting of iron, palladium, nickel, cobalt, chromium, vanadium, molybdenum, tungsten, a combination of metals such as nickel-molybdenum, cobalt-nickel-molybdenum, cobalt-molybdenum, nickel-tungsten and nickel-tungsten-titanium. 17. The process of claim 12 that includes adding a polar compound to the mixture of crude oil and catalyst in step (a). 18. The process of claim 17, wherein the polar compound is an ethanolamine. 19. The process of claim 12 which includes adding activated carbon to the mixture of step (a). 20. The process of claim 12, wherein the microwave energy is at a frequency of from about 200 MHz to about 10,000 MHz. 21. The process of claim 12, wherein the power level is from 500 watts to 5,000 watts and the exposure time is between 20 and 25 minutes. 22. The process of claim 12, wherein the reaction is carried out in a flow-through reactor at an hourly space velocity of the liquid phase that is in range of from 0.10 per hour to 10 per hour. 23. The process of claim 22, wherein the liquid phase hourly space velocity is in the range from 0.30 per hour to 3 per hour.