Distillation and solvent extraction process for rerefining used lubricating oil

Claims

I claim:

1. A method of rerefining used oil containing lubricating oil comprising:

(a) removing from the used oil a volatile forecut to provide a resulting oil containing lubricating oil;

(b) evaporating the resulting oil in an evaporator unit at reduced pressure, greater than about 2.0 millimeters of mercury, to form heavy and light fractions, with a portion of said light fraction recycled and mixed into the resulting oil prior to the resulting oil entering the evaporator unit, in a quantity effective for lowering the vaporization temperature of the resulting oil to reduce the tendency of fouling, coking and cracking of the resulting oil during evaporation;

(c) mixing the light fraction not recycled into the resulting oil with an effective amount of tetrahydrofurfuryl alcohol for removing impurities from the light fraction; and

(d) thereafter separating the light fraction from the tetrahydrofurfuryl alcohol.

2. The method as recited in claim 1 wherein the evaporator unit is an agitated thin film evaporator.

3. The method as recited in claim 1 wherein the evaporator unit is a wiped-film evaporator.

4. The method as recited in claim 1 wherein substantially all of the water, gasoline, and other similar volatile components that may be present in the used oil have been removed prior to step (a) of claim 1.

5. The method as recited in claim 1 wherein the volatile forecut has a flash point less than about 116.degree. C.

6. The method as recited in claim 1 wherein the evaporation in step (b) of claim 45 occurs in the temperature range of about 265.degree. F. to 480.degree. F.

7. The method as recited in claim 1 wherein the ratio of the resulting oil to the light fraction recycled into the resulting oil is about 4:1.

8. The method as recited in claim 1 wherein the amount of the light fraction that is recycled is between about 5% and 300% by weight of the resulting oil.

9. The method as recited in claim 1 wherein said light fraction is light lube oil and the method further comprises:

(a) evaporating at reduced pressure the heavy fraction obtained from the evaporation of the resulting oil to form a heavy lube oil fraction and a residual fraction;

(b) mixing the heavy lube oil fraction with an effective amount of tetrahydrofurfuryl alcohol for removing impurities from the heavy lube oil fraction; and

(c) thereafter separating the heavy lube oil from the tetrahydrofurfuryl alcohol.

10. The method as recited in claim 9 wherein a portion of the heavy lube oil fraction is recycled and mixed into the heavy fraction prior to evaporation thereof in a quantity effective for lowering the vaporization temperature of the heavy fraction to reduce the tendency of coking and cracking of the heavy fraction during evaporation thereof.

11. The method as recited in claim 9 wherein the heavy fraction is evaporated in an agitated thin film evaporator.

12. The method as recited in claim 9 wherein the heavy fraction is evaporated in a wiped-film evaporator.

13. The method as recited in claim 9 wherein the evaporation of the resulting oil occurs in the range of about 2 millimeters of mercury to 5 millimeters of mercury absolute.

14. The method as recited in claim 9 wherein the evaporation of the heavy fraction occurs in the range of about 0.5 millimeters of mercury to 3.0 millimeters of mercury absolute.

15. The method as recited in claim 9 wherein

(a) the heavy lube oil and tetrahydrofurfuryl alcohol mixture is separated into a heavy oil raffinate and a light oil tetrahydrofurfuryl alcohol extract;

(b) the light lube oil and tetrahydrofurfuryl alcohol mixture is separated into a light lube oil raffinate and a light oil tetrahydrofurfuryl alcohol extract;

(c) tetrahydrofurfuryl alcohol is removed from the heavy oil raffinate by distilling and steam stripping; and

(d) tetrahydrofurfuryl alcohol is removed from the light oil raffinate by distilling and steam stripping.

16. The process as recited in claim 15 further comprising:

distilling and steam stripping the light oil tetrahydrofurfuryl extract and the heavy oil tetrahydrofurfuryl extract to remove the tetrahydrofurfuryl alcohol therefrom.

17. The process as recited in claim 16 further comprising:

(a) combining the tetrahydrofurfuryl alcohol removed from the light oil raffinate, the heavy oil raffinate and the heavy and light oil tetrahydrofurfuryl extracts; and

(b) distilling the water present in the mixture set forth in part (a) of this claim to produce dry tetrahydrofurfuryl alcohol that is suitable for use in step (c) of claim 1 or step (b) of claim 9.

18. The process as recited in claim 16 wherein the volume ratio of the heavy lube oil to tetrahydrofurfuryl alcohol is between about 0.5 and 2.0 and the volume ratio of the light lube oil fraction to tetrahydrofurfuryl alcohol is between about 0.5 and 2.0.

19. The process as recited in claim 16 wherein each of the heavy and light lube oil fractions are heated to a temperature in the range between about 125.degree. F. and 250.degree. F. prior to mixing with tetrahydrofurfuryl alcohol.

20. The process as recited in claim 19 wherein the tetrahydrofurfuryl alcohol is heated to a temperature of between about 125.degree. F. and 250.degree. F. prior to mixing with the lube oil fraction.

21. The process as recited in claim 16 wherein the distilling and steam stripping of the heavy and light oil raffinates occurs at reduced pressure.

22. The process as recited in claim 21 wherein the reduced pressure is between about 10 millimeters mercury and 100 millimeters mercury absolute.

23. The process as recited in claim 22 wherein the reduced pressure is about 20 millimeters mercury absolute at a temperature of about 160.degree. F.

24. A method of rerefining used lubricating oil comprising:

(a) removing from the used oil a volatile forecut to provide a resulting oil that contains lubricating oil;

(b) evaporating the resulting oil in an evaporator at reduced pressure in the range of about 2.0 to 5.0 millimeters of mercury absolute and within a temperature range of about 265.degree. F. to 500.degree. F. to form a heavy fraction and a light lube oil fraction, said light lube fraction having a viscosity of between about 60 and 200 SSU at 100.degree. F., with a portion of said light lube oil fraction being recycled and mixed into the resulting oil, prior to evaporation thereof, in a quantity effective for lowering the vaporization temperature of the resulting oil to reduce the tendency of fouling, coking and cracking of the resulting oil during evaporation;

(c) evaporating the heavy fraction in an evaporator obtained from the evaporation of the resulting oil to form a heavy lube fraction and a residual fraction, the evaporation of the heavy fraction occurring at reduced pressure within a range of between about 0.5 millimeters of mercury and 3.0 millimeters of mercury absolute and within a temperature range of about 315.degree. F. and 600.degree. F., with a portion of the heavy lube fraction being recycled and mixed into the heavy fraction, prior to evaporation thereof, in a quantity effective for lowering the vaporization temperature of the heavy fraction to reduce the tendency of coking and cracking of the heavy fraction during evaporation thereof;

(d) separately mixing the light lube oil and heavy fractions not recycled with an effective amount of tetrahydrofurfuryl alcohol for removing impurities from the light lube oil and heavy fractions; and

(e) thereafter separating the tetrahydrofurfuryl alcohol from the light lube oil and heavy fractions.

25. The method as recited in claim 24 wherein the heavy fraction is evaporated with a wiped-film evaporator.

26. The method as recited in claim 24 wherein the amount of light lube oil fraction that is recycled is between about 5% and 300% by weight of the resulting oil and the amount of heavy lube fraction that is recycled is between about 5% and 300% by weight of the heavy fraction.

27. The process as recited in claim 24 wherein the volume ratio of the heavy lube fraction not recycled to tetrahydrofurfuryl alcohol is between about 0.5 and 2.0 and the volume ratio of the light lube oil fraction not recycled to tetrahydrofurfuryl alcohol is between about 0.5 and 2.0.

28. The process as recited in claim 24 wherein each of the heavy lube and light lube oil fractions are heated to a temperature in the range of between about 125.degree. F. and 250.degree. F. prior to mixing with tetrahydrofurfuryl alcohol.

29. The process as recited in claim 28 wherein the tetrahydrofurfuryl alcohol is heated to a temperature of between about 125.degree. F. and 250.degree. F. prior to mixing with the lube oil fractions.