Oil/bitumen emulsion separation
View Patent ↗In one implementation, a method for recovery of crude oil from a production fluid comprising an oil-water emulsion is provided. The method comprises adding a solid hydrophilic compound to the production fluid to form a production fluid-solid hydrophilic compound mixture. The method further comprises separating the production fluid-solid hydrophilic compound mixture to produce an oil phase containing the heavy crude oil and a water phase containing the solid hydrophilic compound. The production fluid-solid hydrophilic compound mixture may be separated by centrifuging the production fluid-solid hydrophilic compound mixture to produce the oil phase and the water phase. After separation, the oil phase may be analyzed to determine at least one of: oil composition, physical properties, and geochemical analysis. The crude oil comprises at least one of heavy crude oil, bitumen or combinations thereof.
1. A method for recovering crude oil from a production fluid comprising an oil-water emulsion, the method comprising:
adding a solid hydrophilic compound to the production fluid to form a production fluid-solid hydrophilic compound mixture; and
separating the production fluid-solid hydrophilic compound mixture to produce an oil phase containing the crude oil and a water phase containing the solid hydrophilic compound, wherein the crude oil comprises at least one of heavy crude oil, bitumen and combinations thereof.
2. The method of claim 1 , wherein the solid hydrophilic compound is selected from the group consisting of calcium sulfate (CaSO 4 ), ball clay, and combinations thereof.
3. The method of claim 1 , wherein separating the production fluid-solid hydrophilic compound mixture comprises centrifuging the production fluid-solid hydrophilic compound mixture to produce the oil phase containing the crude oil and the water phase containing the solid hydrophilic compound.
4. The method of claim 1 , wherein the separated oil phase has a basic sediment and water (BS&W) content of less than 2% by volume.
5. The method of claim 1 , further comprising mixing the solid hydrophilic compound and the production fluid prior to separating the production fluid-solid hydrophilic compound mixture.
6. The method of claim 1 , wherein separating the production fluid-solid hydrophilic compound mixture is performed at a temperature of 40 degrees Celsius or less.
7. The method of claim 6 , wherein separating the production fluid-solid hydrophilic compound mixture is performed at a temperature of from 20 degrees Celsius to 35 degrees Celsius.
8. The method of claim 1 , wherein the solid hydrophilic compound is added to the production fluid in an amount from about 10 to about 30 percent by weight based on the total weight of the production fluid.
9. The method of claim 8 , wherein the solid hydrophilic compound is added to the production fluid in an amount from about 15 to about 25 percent by weight based on the total weight of the production fluid.
10. The method of claim 8 , wherein the solid hydrophilic compound is added to the production fluid in an amount from about 10 to about 22 percent by weight based on the total weight of the production fluid.
11. The method of claim 1 , wherein the crude oil has an API gravity from 5 to 12 degrees.
12. The method of claim 1 , wherein the crude oil has an API gravity from 8 to 12 degrees.
13. The method of claim 1 , further comprising:
analyzing the oil phase to determine at least one of: oil composition, physical properties, and geochemical properties.
14. The method of claim 3 , wherein centrifuging the production fluid-solid hydrophilic compound mixture to produce the oil phase containing the crude oil and the water phase containing the solid hydrophilic compound comprises operating a centrifuge at 10,000 to 12,000 rpm for a period of 45 minutes or less.
15. A method for recovering crude oil from a production fluid comprising an oil-water emulsion, the method comprising:
adding a solid hydrophilic compound to the production fluid to form a production fluid-solid hydrophilic compound mixture, wherein the solid hydrophilic compound is selected from the group consisting of: calcium sulfate (CaSO 4 ), ball clay, and combinations thereof; and
centrifuging the production fluid-solid hydrophilic compound mixture to produce an oil phase containing the crude oil and a water phase containing the solid hydrophilic compound, wherein the crude oil comprises at least one of heavy crude oil, bitumen and combinations thereof.
16. The method of claim 15 , further comprising analyzing the oil phase to determine at least one of: oil composition, physical properties, and geochemical properties.
17. The method of claim 15 , wherein the crude oil has an API gravity from 5.1 to 8 degrees and the solid hydrophilic compound is added to the production fluid in an amount from about 15 to about 25 percent by weight based on the total weight of the production fluid.
18. The method of claim 15 , wherein the crude oil has an API gravity from 8 to 12 degrees and the solid hydrophilic compound is added to the production fluid in an amount from about 10 to about 22 percent by weight based on the total weight of the production fluid.
19. The method of claim 15 , wherein centrifuging the production fluid-solid hydrophilic compound mixture to produce the oil phase containing the crude oil and the water phase containing the solid hydrophilic compound comprises operating a centrifuge at 10,000 to 12,000 rpm for a period of less than 30 minutes.
20. The method of claim 15 , wherein the crude oil comprises bitumen.