Process for recovering semiconductor industry cleaning compounds

• US 5,779,763 A
• Filed: 03/07/1997
• Issued: 07/14/1998
• Est. Priority Date: 03/07/1997
• Status: Expired due to Term

• Current Assignee: Membrane Technology and Research, Inc.
• Original Assignee: Membrane Technology and Research, Inc.
• Inventors: He, Zhenjie, Goakey, Shannon, Wijmans, Johannes G., Pinnau, Ingo, Baker, Richard W.
• Primary Examiner(s): SPITZER, ROBERT H
• Application Number:
  US08/813,520
• Time in Patent Office: 494 Days
• Field of Search: 95/45, 95/47-55, 95/39
• US Class Current: 95/39
• CPC Class Codes: B01D 2257/2066 Fluorine
• CPC Class Codes: B01D 53/002 by condensation
• CPC Class Codes: B01D 53/229 Integrated processes (Diffusion and at least one other process, e.g. adsorption, absorption)
• CPC Class Codes: Y02C 20/20 of methane
• CPC Class Codes: Y02C 20/30 of perfluorocarbons [PFC], hydrofluorocarbons [HFC] or sulfur hexafluoride [SF6]

Abstract

A process for separating perfluoro compound gas or vapor from another gas, typically nitrogen, in a gas mixture. The process involves a combination of membrane separation and condensation, and is particularly useful in the semiconductor industry, for treating exhaust gases from cleaning of chemical vapor deposition chambers. Operation of the condensation step at temperatures no lower than about -30° C. reduces the need for refrigeration equipment and controls the amount of gas dissolved in the recovered perfluoro compound.

Claims

1. A process for separating a perfluoro compound from a second gas in a gas mixture, said process comprising the steps of:

(a) providing a first membrane having a first feed side and a first permeate side, and being selective for said second gas over said perfluoro compound;

(b) passing said gas mixture across said first feed side;

(c) withdrawing from said first feed side a first residue stream depleted in said second gas and enriched in said perfluoro compound compared with said gas mixture;

(d) withdrawing from said first permeate side a first permeate stream enriched in said second gas and depleted in said perfluoro compound compared with said gas mixture;

(e) providing a second membrane having a second feed side and a second permeate side, and being selective for said second gas over said perfluoro compound;

(f) passing said first residue stream across said second feed side;

(g) withdrawing from said second feed side a second residue stream depleted in said second gas and enriched in said perfluoro compound compared with said first residue stream;

(h) withdrawing from said second permeate side a second permeate stream enriched in said second gas and depleted in said perfluoro compound compared with said first residue stream;

(i) passing said second residue stream to a condensation step carried out at a temperature no lower than about -30°

C. to liquefy at least a portion of said second residue stream, thereby forming a liquefied perfluoro compound product;

(j) recirculating said second permeate stream to said first feed side.

2. The process of claim 1, further comprising compressing said gas mixture prior to passing said gas mixture across said first feed side.

3. The process of claim 2, wherein said compressing raises said gas mixture to a pressure no greater than about 500 psia.

4. The process of claim 2, wherein said compressing raises said gas mixture to a pressure no greater than about 200 psia.

5. The process of claim 1, further comprising subjecting an uncondensed gas stream from said condensation step (i) to treatment to separate said second gas from said perfluoro compound.

6. The process of claim 1, further comprising recirculating an uncondensed gas stream from said condensation step (i) to said second feed side.

7. The process of claim 1, further comprising passing an uncondensed gas stream from said condensation step (i) across a third membrane for treatment.

8. The process of claim 1, wherein said condensation step (i) further includes compressing said second residue stream.

9. The process of claim 8, wherein said compressing raises said second residue stream to a pressure no greater than about 500 psia.

10. The process of claim 1, wherein said temperature is no lower than about 0°

C.

11. The process of claim 1, wherein said temperature is no lower than about 15°

C.

12. The process of claim 1, wherein said first membrane exhibits a transmembrane pressure-normalized flux of said second gas of at least about 1×

10^-5 cm³ (STP)/cm² ·

s·

cmHg.

13. The process of claim 1, wherein said first membrane comprises a polymer characterized by a fractional free volume of at least about 0.16.

14. The process of claim 1, wherein said first membrane comprises a substituted polyacetylene.

15. The process of claim 1, wherein said first membrane comprises poly(4-methyl-2-pentyne).

16. The process of claim 1, wherein said first membrane comprises a polymer of perfluoro-2,2-dimethyl-1,3-dioxole.

17. The process of claim 1, wherein said first membrane exhibits a selectivity for said second gas over said perfluoro compound of at least about 10 when in use in said process.

18. The process of claim 1, wherein said first membrane exhibits a selectivity for said second gas over said perfluoro compound of at least about 30 when in use in said process.

19. The process of claim 1, wherein said perfluoro compound is a perfluorocarbon.

20. The process of claim 1, wherein said perfluoro compound is selected from the group consisting of perfluoromethane, perfluoroethane, perfluoropropane, methyl fluoride, nitrogen trifluoride and sulfur hexafluoride.

21. The process of claim 1, wherein said perfluoro compound is perfluoroethane.

22. The process of claim 1, wherein said second gas is selected from the group consisting of nitrogen, air, hydrogen, argon and helium.

23. The process of claim 1, wherein said second gas is nitrogen.

24. The process of claim 1, wherein said second gas is hydrogen.

25. The process of claim 1, wherein said second membrane exhibits a transmembrane pressure-normalized flux of said second gas of at least about 1×

10^-5 cm³ (STP)/cm² ·

s·

cmHg.

26. The process of claim 1, wherein said second membrane comprises a polymer characterized by a fractional free volume of at least about 0.16.

27. The process of claim 1, wherein said second membrane comprises a substituted polyacetylene.

28. The process of claim 1, wherein said second membrane comprises poly(4-methyl-2-pentyne).

29. The process of claim 1, wherein said second membrane comprises a polymer of perfluoro-2,2-dimethyl-1,3-dioxole.

30. The process of claim 1, wherein said second membrane exhibits a selectivity for said second gas over said perfluoro compound of at least about 10 when in use in said process.

31. The process of claim 1, wherein said second membrane exhibits a selectivity for said second gas over said perfluoro compound of at least about 20 when in use in said process.

32. The process of claim 1, further comprising subjecting said gas mixture to additional treatment to separate said second gas from said perfluoro compound prior to passing said gas mixture to said first feed side.

33. The process of claim 32, wherein said second permeate stream is recirculated to an inlet side of said additional treatment.

34. The process of claim 32, wherein said additional treatment comprises additional membrane separation.

35. The process of claim 34, wherein said second permeate stream is recirculated to an inlet side of said additional membrane separation.

36. The process of claim 1, wherein said gas mixture is from a chemical vapor deposition chamber.

37. The process of claim 1, wherein at least about 90% of said perfluoro compound in said gas mixture is recovered in said liquefied perfluoro compound product.

38. The process of claim 1, wherein at least about 95% of said perfluoro compound in said gas mixture is recovered in said liquefied perfluoro compound product.

39. A process for separating a perfluoro compound from a second gas in a gas mixture, said process comprising the steps of:

(a) providing a first membrane having a first feed side and a first permeate side, and being selective for said second gas over said perfluoro compound;

(b) passing said gas mixture across said first feed side;

(c) withdrawing from said first feed side a first residue stream depleted in said second gas and enriched in said perfluoro compound compared with said gas mixture;

(d) withdrawing from said first permeate side a first permeate stream enriched in said second gas and depleted in said perfluoro compound compared with said gas mixture;

(e) passing said first residue stream to a condensation step carried out at a temperature no lower than about -30°

C. to liquefy at least a portion of said first residue stream, thereby forming a liquefied perfluoro compound product;

(f) providing a second membrane having a second feed side and a second permeate side;

(g) passing an uncondensed gas stream from said condensation step across said second feed side;

(h) withdrawing from said second feed side a second residue stream depleted in said second gas and enriched in said perfluoro compound compared with said uncondensed gas stream;

(i) withdrawing from said second permeate side a second permeate stream enriched in said second gas and depleted in said perfluoro compound compared with said uncondensed gas stream;

(j) recirculating said second permeate stream to said first feed side;

(k) recirculating said second residue stream to said condensation step.

40. The process of claim 39, further comprising compressing said gas mixture prior to passing said gas mixture across said first feed side.

41. The process of claim 40, wherein said compressing raises said gas mixture to a pressure no greater than about 500 psia.

42. The process of claim 40, wherein said compressing raises said gas mixture to a pressure no greater than about 200 psia.

43. The process of claim 39, wherein said temperature is no lower than about 0°

C.

44. The process of claim 39, wherein said temperature is no lower than about 15°

C.

45. The process of claim 39, wherein said first membrane exhibits a transmembrane pressure-normalized flux of said second gas of at least about 1×

10^-5 cm³ (STP)/cm² ·

s·

cmHg.

46. The process of claim 39, wherein said first membrane comprises a polymer characterized by a fractional free volume of at least about 0.16.

47. The process of claim 39, wherein said first membrane comprises a substituted polyacetylene.

48. The process of claim 39, wherein said first membrane comprises poly(4-methyl-2-pentyne).

49. The process of claim 39, wherein said first membrane comprises a polymer of perfluoro-2,2-dimethyl-1,3-dioxole.

50. The process of claim 39, wherein said first membrane exhibits a selectivity for said second gas over said perfluoro compound of at least about 10 when in use in said process.

51. The process of claim 39, wherein said first membrane exhibits a selectivity for said second gas over said perfluoro compound of at least about 30 when in use in said process.

52. The process of claim 39, wherein said perfluoro compound is a perfluorocarbon.

53. The process of claim 39, wherein said perfluoro compound is selected from the group consisting of perfluoromethane, perfluoroethane, perfluoropropane, methyl fluoride, nitrogen trifluoride and sulfur hexafluoride.

54. The process of claim 39, wherein said perfluoro compound is perfluoroethane.

55. The process of claim 39, wherein said second gas is selected from the group consisting of nitrogen, air, hydrogen, argon and helium.

56. The process of claim 39, wherein said second gas is nitrogen.

57. The process of claim 39, wherein said second gas is hydrogen.

58. The process of claim 39, wherein said second membrane exhibits a transmembrane pressure-normalized flux of said second gas of at least about 1×

10^-5 cm³ (STP)/cm² ·

s·

cmHg.

59. The process of claim 39, wherein said second membrane comprises a polymer characterized by a fractional free volume of at least about 0.16.

60. The process of claim 39, wherein said second membrane comprises a substituted polyacetylene.

61. The process of claim 39, wherein said second membrane comprises poly(4-methyl-2-pentyne).

62. The process of claim 39, wherein said second membrane comprises a polymer of perfluoro-2,2-dimethyl-1,3-dioxole.

63. The process of claim 39, wherein said second membrane exhibits a selectivity for said second gas over said perfluoro compound of at least about 10 when in use in said process.

64. The process of claim 39, wherein said second membrane exhibits a selectivity for said second gas over said perfluoro compound of at least about 20 when in use in said process.

65. The process of claim 39, further comprising subjecting said gas mixture to additional treatment to separate said second gas from said perfluoro compound prior to passing said gas mixture to said first feed side.

66. The process of claim 65, wherein said second permeate stream is recirculated to an inlet side of said additional treatment.

67. The process of claim 65, wherein said additional treatment comprises additional membrane separation.

68. The process of claim 67, wherein said second permeate stream is recirculated to an inlet side of said additional membrane separation.

69. The process of claim 39, wherein said gas mixture is from a chemical vapor deposition chamber.

70. The process of claim 39, wherein at least about 90% of said perfluoro compound in said gas mixture is recovered in said liquefied perfluoro compound product.

71. The process of claim 39, wherein at least about 95% of said perfluoro compound in said gas mixture is recovered in said liquefied perfluoro compound product.