Patent EA-002638-B1 (EA)
Title: Method of re-refining waste oil by distillation and extraction
Inventor: DASPIT ALEXANDER D B
IPC: C10M175/00
Filed: 1998-09-08
Abstract: 1. A process for recovering base oil of lubricating viscosity from used oil, said process comprising the steps of: distilling said used oil in a distillation apparatus; withdrawing at least a portion of at least one distillate fraction from said distillation apparatus for further finishing; delivering at least a portion of said at least one withdrawn distillation fraction for further finishing; extracting impurities from at least one said withdrawn distillate fraction with a liquid extractant; removing at least a major portion of said extractant, and impurities dissolved therein, from said withdrawn distillate fraction; wherein said distillation apparatus has more theoretical plates than distillate fractions being withdrawn from said distillation apparatus for further finishing. 2. A process as in claim 1, wherein said distillation apparatus comprises a vacuum column operating under reduced pressure. 3. A process as in claim 2, wherein said vacuum column comprises at least one of a random packing and a structured packing. 4. A process as in claim 1, further comprising a step of pretreating said used oil to remove entrained water and volatile low boiling components from said used oil. 5. A process as in claim 1, further comprising a step of pretreating said used oil to reduce said used oil's propensity to foul said distillation apparatus. 6. A process as in claim 5, wherein said step of pretreating said used oil to reduce fouling comprises a chemical treatment of the oil. 7. A process as in claim 5, wherein said step of pretreating said used oil to reduce fouling comprises thermal treatment of the oil at a temperature in excess of 400 degree F (204.4 degree C) for an average residence time of at least ten minutes. 8. A process as in claim 1, wherein the liquid extractant comprises a polar organic solvent. 9. A process as in claim 8, wherein the polar organic solvent is N-Methyl-2-Pyrrolidone. 10. A process as in claim 1, wherein said distillation apparatus has more than one and one half theoretical plates per distillate fraction being withdrawn from said distillation apparatus. 11. A process as in claim 1, wherein said distillation apparatus has more than two theoretical plates per distillate fraction being withdrawn from said distillation apparatus. 12. A process as in claim 1, wherein said distillation apparatus has more than three theoretical plates per distillate fraction being withdrawn from said distillation apparatus. 13. A process for recovering base oil of lubricating viscosity from used oil, said process comprising the steps of: distilling said used oil in a distillation apparatus;  withdrawing at least a portion of at least two distillate fractions from said distillation apparatus for further treatment; extracting impurities from at least one of said withdrawn distillate fractions with a liquid extractant; removing at least a major portion of said extractant, and impurities dissolved therein, from said at least one of said withdrawn distillate fractions; wherein said distillation apparatus has more than one theoretical plate interposed between any two immediately adjacent distillate fractions withdrawn from said distillation apparatus. 14. A process as in claim 13, wherein said distillation apparatus comprises a vacuum column operating under reduced pressure. 15. A process as in claim 14, wherein said vacuum column comprises at least one of a random packing and a structured packing. 16. A process as in claim 13, further comprising a step of pretreating said used oil to remove entrained water and volatile low boiling components from said used oil. 17. A process as in claim 13, further comprising a step of pretreating said used oil to reduce said used oil's propensity to foul said distillation apparatus. 18. A process as in claim 17, wherein said step of pretreating said used oil to reduce fouling comprises a chemical treatment of the oil. 19. A process as in claim 17, wherein said step of pretreating said used oil to reduce fouling comprises thermal treatment of the oil at a temperature in excess of 400 degree F (204.4 degree C) for an average residence time of at least ten minutes. 20. A process as in claim 13, wherein the liquid extractant comprises a polar organic solvent. 21. A process as in claim 20, wherein the polar organic solvent is N-Methyl-2-Pyrrolidone. 22. A process as in claim 13, wherein said distillation apparatus has more than one and one half theoretical plates interposed between any two immediately adjacent distillate fractions being withdrawn from said distillation apparatus. 23. A process as in claim 13, wherein said distillation apparatus has more than two theoretical plates interposed between any two immediately adjacent distillate fractions being withdrawn from said distillation apparatus. 24. A process as in claim 13, wherein said distillation apparatus has more than three theoretical plates interposed between any two immediately adjacent distillation fractions being withdrawn from said distillation apparatus. 25. A process for recovering base oil of lubricating viscosity from used oil, said process comprising the steps of: distilling said used oil in a distillation apparatus; withdrawing at least one distillate fraction and a bottoms fraction from said distillation apparatus; extracting impurities from at least one said distillate fraction with a liquid extractant; removing at least a major portion of said extractant, and impurities dissolved therein, from at least one of said withdrawn distillate fractions; wherein said distillation apparatus has more than one theoretical plate for separating the bottoms fraction from the heaviest distillate fraction from which impurities are extracted using said liquid extractant. 26. A process as in claim 25, wherein said distillation apparatus comprises a vacuum column operating under reduced pressure. 27. A process as in claim 26, wherein said vacuum column comprises at least one of a random packing and a structured packing. 28. A process as in claim 25, further comprising a step of pretreating said used oil to remove entrained water and volatile low boiling components from said used oil. 29. A process as in claim 25, further comprising a step of pretreating said used oil to reduce said used oil's propensity to foul said distillation apparatus. 30. A process as in claim 29, wherein said step of pretreating said used oil to reduce fouling comprises a chemical treatment of the oil. 31. A process as in claim 29, wherein said step of pretreating said used oil to reduce fouling comprises thermal treatment of the oil at a temperature in excess of 400 degree F (204.4 degree C) for an average residence time of at least ten minutes. 32. A process as in claim 25, wherein the liquid extractant comprises a polar organic solvent. 33. A process as in claim 32, wherein the polar organic solvent is N-Methyl-2-Pyrrolidone. 34. A process as in claim 25, wherein said distillation apparatus has more than one and one half theoretical plates for separating the bottoms fraction from the heaviest distillate fraction withdrawn from said distillation apparatus. 35. A process as in claim 25, wherein said distillation apparatus has more than two theoretical plates for separating the bottoms fraction from the heaviest distillate fraction withdrawn from said distillation apparatus. 36. A process as in claim 25, wherein said distillation apparatus has more than three theoretical plates for separating the bottoms fraction from the heaviest distillate fraction withdrawn from said distillation apparatus. 37. A process for recovering base oil of lubricating viscosity from used oil, said process comprising the steps of: distilling said used oil in a distillation apparatus; withdrawing at least two distillate fractions from said distillation apparatus; extracting impurities from at least one said withdrawn distillate fractions with a liquid extractant; removing at least a major portion of said extractant, and impurities dissolved therein, from at least one said withdrawn distillate fractions; wherein said distillation apparatus has more than one theoretical plate for separating the lightest withdrawn distillate fraction from the immediately adjacent heavier distillate fraction from which impurities are extracted using said liquid extractant. 38. A process as in claim 37, wherein said distillation apparatus comprises a vacuum column operating under reduced pressure. 39. A process as in claim 38, wherein said vacuum column comprises at least one of a random packing and a structured packing. 40. A process as in claim 37, further comprising a step of pretreating said used oil to remove entrained water and volatile low boiling components from said used oil. 41. A process as in claim 37, further comprising a step of pretreating said used oil to reduce said used oil's propensity to foul said distillation apparatus. 42. A process as in claim 41, wherein said step of pretreating said used oil to reduce fouling comprises a chemical treatment of the oil. 43. A process as in claim 41, wherein said step of pretreating said used oil to reduce fouling comprises thermal treatment of the oil at a temperature in excess of 400 degree F (204.4 degree C) for an average residence time of at least ten minutes. 44. A process as in claim 37, wherein the liquid extractant comprises a polar organic solvent. 45. A process as in claim 44, wherein the polar organic solvent is N-Methyl-2-Pyrrolidone. 46. A process as in claim 37, wherein said distillation apparatus has more than one and one half theoretical plates for separating the lightest withdrawn distillate fraction from the immediately adjacent heavier distillate fraction from which impurities are extracted using said liquid extractant. 47. A process as in claim 37, wherein said distillation apparatus has more than two theoretical plates for separating the lightest withdrawn distillate fraction from the immediately adjacent heavier distillate frac