Process and system for separation and recovery of perfluorocompound gases

• US 5,919,285 A
• Filed: 04/03/1998
• Issued: 07/06/1999
• Est. Priority Date: 07/17/1995
• Status: Expired due to Term

• Current Assignee: American Air Liquide Incorporated (L'Air Liquide SA), L'Air Liquide Societe Anonyme Pour L'Etude et L'Exploitation Des Procedes Georges Claude (L'Air Liquide SA)
• Original Assignee: American Air Liquide Incorporated (L'Air Liquide SA), L'Air Liquide Societe Anonyme Pour L'Etude et L'Exploitation Des Procedes Georges Claude (L'Air Liquide SA)
• Inventors: Paganessi, Joseph E., Li, Yao-En, Vassallo, David, Fleming, Gregory K.
• Primary Examiner(s): SPITZER, ROBERT H
• Application Number:
  US09/054,549
• Time in Patent Office: 459 Days
• Field of Search: 95/45, 95/47-49, 95/51-54, 95/90, 95/92, 95/149, 95/230, 95/237, 96/4, 96/7-14, 96/108, 96/134, 96/361
• US Class Current: 95/45
• CPC Class Codes: B01D 2257/204 Inorganic halogen compounds
• CPC Class Codes: B01D 2257/2066 Fluorine
• CPC Class Codes: B01D 53/22 by diffusion manufacturing semi-permeable membranes B01D67/00; form, structure or properties of semi-permeable membranes B01D69/00; material for semi-permeable membranes B01D71/00
• CPC Class Codes: B01D 53/225 Multiple stage diffusion
• CPC Class Codes: B01D 53/226 in serial connexion
• CPC Class Codes: B01D 53/228 characterised by specific membranes
• CPC Class Codes: B01D 53/229 Integrated processes (Diffusion and at least one other process, e.g. adsorption, absorption)
• CPC Class Codes: C07C 17/38 Separation; Purification; Stabilisation; Use of additives
• CPC Class Codes: C07C 19/08 containing fluorine
• CPC Class Codes: Y02C 20/30 of perfluorocarbons [PFC], hydrofluorocarbons [HFC] or sulfur hexafluoride [SF6]
• CPC Class Codes: Y02P 20/151 Reduction of greenhouse gas [GHG] emissions, e.g. CO2
• CPC Class Codes: Y02P 20/155 Perfluorocarbons [PFC]; Hydrofluorocarbons [HFC]; Hydrochlorofluorocarbons [HCFC]; Chlorofluorocarbons [CFC]

Abstract

Processes and systems to recover at least one perfluorocompound gas from a gas mixture are provided. In one embodiment the inventive process comprises the steps of a) providing a gas mixture comprising at least one perfluorocompound gas and at least one carrier gas, the gas mixture being at a predetermined pressure; b) providing at least one glassy polymer membrane having a feed side and a permeate side; c) contacting the feed side of the at least one membrane with the gas mixture; d) withdrawing from the feed side of the membrane as a non-permeate stream at a pressure which is substantially equal to the predetermined pressure a concentrated gas mixture comprising essentially the at least one perfluorocompound gas; and e) withdrawing from the permeate side of the membrane as a permeate stream a depleted gas mixture comprising essentially the at least one carrier gas.

Claims

1. A process to recover at least one perfluorocompound gas from a gas mixture, comprising the steps of:

a) providing a gas mixture comprising at least one perfluorocompound gas and at least one carrier gas, said gas mixture being at a first pressure and a first temperature, said at least one perfluorocompound gas devoid of components which include chlorine;

b) providing a first glassy polymer membrane having a feed side and a permeate side;

c) contacting the feed side of said first membrane with said gas mixture;

d) withdrawing from the feed side of the first membrane as a first non-permeate stream at a pressure which is substantially equal to said first pressure a concentrated gas mixture comprising essentially the at least one perfluorocompound gas; and

e) withdrawing from the permeate side of said first membrane as a first permeate stream a depleted gas mixture consisting essentially of the at least one carrier gas.

2. Process in accordance with claim 1 wherein said gas mixture pressure is supplied by compressing said gas mixture with a compressor.

3. Process in accordance with claim 2 wherein said compressor is oil-free and sealed.

4. Process in accordance with claim 2 wherein said gas mixture is treated prior to compression to substantially remove most of the species harmful for the compressor prior to compression.

5. A process according to claim 1 wherein said membrane comprises a plurality of hollow fibers.

6. A process according to claim 5, wherein said feed side of the membrane comprises a bore side of each of said plurality of hollow fibers, while the permeate side is an outside of each hollow fiber.

7. Process in accordance with claim 1 wherein said gas mixture comprises an effluent stream from a process selected from the group consisting of oxide etching, metal etching, dielectric etching, deposition, backetching, and dry chamber cleaning.

8. A process according to claim 1, wherein the perfluorocompound gas devoid of components which include chlorine is selected from the group consisting of fluorocarbons, NF₃, SF₆, C₃ F₈ and mixtures thereof.

9. A process according to claim 1, wherein the carrier gas is selected from the group consisting of Ar, N₂, Kr, Xe, Ne, O₂, He, H₂, CO, CO₂, H₂ O and mixtures thereof including air.

10. A process according to claim 1, wherein the glassy polymer membrane is made of at least one polymer selected from the group consisting of polyimides, polyamides, polyamides-imides, polyesters, polycarbonates, polysulfones, polyethersulfone, polyetherketone, alkyl substituted aromatic polyesters, blends of polyethersulfone, fluorinated aromatic polyimides, polyamides and polyamide-imides, copolymers thereof, substituted polymers thereof.

11. A process according to claim 1 wherein the membrane is an asymmetric hollow fiber membrane comprising a core and a skin which are made of different polymers, the permeability of the polymer of the skin being lower for perfluorocompound than for nitrogen.

12. A process according to claim 1 wherein the gas mixture which is contacted with the membrane comprises less than 1% vol. of each of gaseous components which are harmful for the membrane.

13. A process according to claim 1 wherein the gas mixture which is contacted with the membrane comprises less than 10 ppm of each gaseous component which is harmful for the membrane.

14. A process according to claim 1 wherein the gas mixture, which is contacted with the membrane comprises less than 1 ppm of each gaseous component which is harmful for the membrane.

15. A process according to claim 1 wherein the gas mixture prior to being fed to the membrane, is brought to a pressure which is effective for carrying out the separation of the perfluorocompound gas or gas mixture in order to recover a non-permeate stream which is concentrated in perfluorocompound species compared to the gas mixture, the perfluorocompound gas or gas mixture, and the perfluorocompound species all being devoid of components which include chlorine.

16. A process according to claim 1 wherein the pressure of the gas mixture ranges from about 10⁵ Pascal to about 10⁶ Pascal.

17. A process according to claim 1 wherein the first non-permeate stream is sent to a feed side of a second membrane which is similar to the first membrane, said second membrane producing a second non-permeate stream more concentrated in perfluorocompounds than said first non-permeate stream, said process continuing through N-stages.

18. A process according to claim 17 wherein the first permeate stream is vented and a second permeate stream from the second membrane is recycled to the feed side of the first membrane.

19. A process in accordance with claim 17 wherein N ranges from 3 to 10.

20. A process according to claim 17, wherein the second membrane has a selectivity for perfluorocompounds devoid of components which include chlorine which is more than a selectivity of the first membrane when measured at pressure and temperature of feed side of the second membrane.

21. A process according to claim 17, wherein the second membrane has a selectivity for perfluorocompounds devoid of components which include chlorine which is more than a selectivity of the first membrane when measured at pressure and temperature of the feed side of the first membrane.

22. Process in accordance with claim 17 wherein at least a portion of a Nth non-permeate stream from stage N is used as a sweep gas on the feed side of any previous membrane and/or on the feed side of membrane stage N.

23. Process in accordance with claim 17 wherein each stage is operated at a constant concentration set-point for one or more perfluorocompound gases devoid of components including chlorine in each stage.

24. A process according to claim 1, wherein the non-permeate stream is compressed and/or cooled, and stored in storage means for further processing.

25. A process according to claim 1, wherein at least a portion of the first non-permeate stream is recycled.

26. Process in accordance with claim 25 wherein the portion of the non-permeate stream which is recycled is routed to a surge tank prior to re-entering the process, or prior to being routed to storage.

27. A process according to claim 1, wherein the non-permeate stream comprises a mixture of perfluorocompound gases selected from the group consisting of SF₆, C₂ F₆, CHF₃, CF₄ and NF₃.

28. A process according to claim 27 wherein each of the perfluorocompounds devoid of components which include chlorine is successively separated from the non-permeate stream with a membrane system having a selectivity of at least 2 between two different perfluorocompounds devoid of components which include chlorine.

29. A process according to claim 1, wherein at least one of the perfluorocompound gases devoid of components which include chlorine of the non-permeate stream is further separated from other perfluorocompounds devoid of components which include chlorine in said non-permeate stream.

30. A process according to claim 29, wherein separation of at least one less volatile from more volatile perfluorocompound gases devoid of components which include chlorine is made by condensation in a heat exchanger using a cooling fluid at an effective temperature and flowrate.

31. A process according to claim 29, wherein the at least one perfluorocompound gas is devoid of components which include chlorine and is a mixture consisting essentially of NF₃ and CF₄, said mixture being routed to an adsorption system wherein NF₃ is adsorbed and CF₄ is not.

32. A process according to claim 29, wherein the at least one perfluorocompound gas is devoid of components which include chlorine and is a mixture consisting essentially of CHF₃ and C₂ F₆, and wherein the mixture consisting essentially of CHF₃ and C₂ F₆ is sent to an adsorption system wherein CHF₃ is adsorbed and C₂ F₆ is not.

33. A process according to claim 1 wherein the gas mixture first temperature as it enters the membrane ranges from about -40°

C. to 120°

C.

34. A process according to claim 1 wherein the gas mixture is heated to a second temperature before feeding the gas mixture on to the membrane, said second temperature ranging from about -40 to 120°

C.

35. A process according to claim 1 wherein the gas mixture is cooled to a second temperature before sending the gas mixture on to the membrane, said second temperature ranging from about -40 to about 120°

C.

36. Process in accordance with claim 1 wherein at least a portion of the first non-permeate stream is used as a sweep gas on the feed side of the first membrane.

37. Process in accordance with claim 1 wherein the process is operated at a constant concentration set-point for one or more perfluorocompound gases devoid of components including chlorine in said first non-permeate stream.

38. Process in accordance with claim 1 wherein the permeate stream is recycled to the process, or to storage.

39. Process in accordance with claim 1 wherein said gas mixture is treated with a pretreatment process prior to entry to the feed side of the first membrane to substantially remove most of species harmful for the membrane prior to feeding said gas mixture to the feed side of the membrane, said pretreatment process being selected from the group consisting of plasma decomposition, thermal decomposition, catalytic decomposition, scrubbing, and adsorption.

40. Process in accordance with claim 39 wherein a waste stream from said pretreatment process is used to generate perfluorocompounds.

41. Process in accordance with claim 1 wherein said non-permeate stream is treated in a post-treatment process to remove non-perfluorocompound gases and other materials which may be harmful to the membrane.

42. Process in accordance with claim 1 wherein said process is operated at a constant carrier gas flow rate.

43. A process to recover at least one perfluorocompound gas or gas mixture from a gas mixture flowing from a semiconductor manufacturing process, comprising the steps of:

a) providing a gas mixture comprising at least one perfluorocompound gas, at least one species harmful to a glassy polymer membrane, and at least one carrier gas, the perfluorocompound gas devoid of components including chlorine;

b) providing a glassy polymer membrane having a feed side and a permeate side;

c) pretreating said gas mixture in order to remove substantially all of said species harmful to said glassy polymer membrane or reduce the concentration of said species harmful to said glassy polymer membrane to an acceptable level and obtaining a treated gas mixture;

d) contacting the feed side of said membrane with said treated gas mixture at a first pressure;

e) withdrawing a concentrated gas mixture comprising a higher concentration of the at least one perfluorocompound gas devoid of components including chlorine than in the treated gas mixture, from the feed side of the membrane as a non-permeate stream at a pressure which is substantially equal to said first pressure; and

f) withdrawing a gas or gas mixture from the permeate side of said membrane permeate stream which is enriched in carrier gas.

44. A process to recover at least one perfluorocompound gas from a gas mixture, comprising the steps of:

a) providing a plurality of semiconductor tools arranged in parallel, each tool emitting a gas mixture comprising at least one perfluorocompound gas and at least one carrier gas, said gas mixture being at a first pressure and a first temperature;

b) providing a glassy polymer membrane separation unit for each tool, each glassy polymer membrane separation unit having a feed side and a permeate side;

c) contacting the feed side of each of said membrane units with gas mixture from its corresponding tool;

d) withdrawing from the feed side of each membrane separation unit as a first non-permeate stream at a pressure which is substantially equal to said first pressure, a concentrated gas mixture comprising essentially the at least one perfluorocompound gas; and

e) withdrawing from the permeate side of each membrane separation unit as a first permeate stream a depleted gas mixture consisting essentially of the at least one carrier gas.

45. A process to recover at least one perfluorocompound gas from a gas mixture, comprising the steps of:

a) providing a gas mixture comprising at least one perfluorocompound gas and at least one carrier gas, said gas mixture being at a first pressure and a first temperature;

b) providing a first glassy polymer membrane separation unit having a feed side and a permeate side;

c) contacting the feed side of said first glassy polymer membrane separation unit with said gas mixture;

d) withdrawing from the feed side of the first glassy polymer membrane separation unit as a first non-permeate stream at a pressure which is substantially equal to said first pressure, a concentrated gas mixture comprising essentially the at least one perfluorocompound gas;

e) withdrawing from the permeate side of said first glassy polymer membrane separation unit as a first permeate stream a depleted gas mixture consisting essentially of the at least one carrier gas; and

f) wherein there exists one or more spare membranes, which allow the first glassy polymer membrane separation unit to be serviced or otherwise by-passed.

46. A process to recover at least one perfluorocompound gas from a gas mixture, comprising the steps of:

a) providing a gas mixture comprising at least one perfluorocompound gas and at least one carrier gas, said gas mixture being at a first pressure and a first temperature;

b) providing a first glassy polymer membrane having a feed side and a permeate side;

c) pretreating said gas mixture by a pretreatment process prior to entry to the feed side of the first membrane to substantially remove most of species harmful for the first membrane prior to feeding said gas mixture to the feed side of the first membrane;

d) contacting the feed side of said first membrane with said gas mixture;

e) withdrawing from the feed side of the first membrane as a first non-permeate stream at a pressure which is substantially equal to said first pressure a concentrated gas mixture comprising essentially the at least one perfluorocompound gas; and

f) withdrawing from the permeate side of said first membrane as a first permeate stream a depleted gas mixture consisting essentially of the at least one carrier gas.

47. Process in accordance with claim 46 wherein said pretreatment process is selected from the group consisting of plasma decomposition, thermal decomposition, catalysis, scrubbing, and adsorption.

48. A semiconductor manufacturing system comprising:

a) at least one reactor chamber adapted to receive perfluorocompound gases, carrier gases, and the like, the reactor chamber having a reactor effluent gas conduit attached thereto, said perfluorocompound gases devoid of components including chlorine;

b) at least one glassy polymer membrane separation unit having a feed side and a permeate side, said membrane being permeable to at least one carrier gas and being substantially non-permeable to at least one perfluorocompound gas devoid of components including chlorine, said membrane unit connected to said reactor chamber via the reactor effluent conduit, said membrane unit having a permeate vent conduit and a non-permeate conduit; and

c) means to recycle at least a portion of said non-permeate stream from said membrane unit back to the at least one reactor chamber;

d) wherein said at least one glassy polymer membrane separation unit is a plurality of glassy polymer membrane separation units arranged in series.

49. System in accordance with claim 48 wherein a first permeate stream from a first membrane separation unit is vented through a vent conduit and a second permeate stream from a second membrane separation unit is recycled to the reactor chamber through a permeate recycle conduit.

50. A semiconductor manufacturing system comprising:

a) at least one reactor chamber adapted to receive perfluorocompound gases, carrier gases, and the like, the reactor chamber having a reactor effluent gas conduit attached thereto, said perfluorocompound gases devoid of components including chlorine;

b) at least one glassy polymer membrane separation unit having a feed side and a permeate side, said membrane being permeable to at least one carrier gas and being substantially non-permeable to at least one of said perfluorocompound gases devoid of components including chlorine, said membrane unit connected to said reactor chamber via the reactor effluent conduit, said membrane unit having a permeate vent conduit and a non-permeate conduit; and

c) means to recycle at least a portion of said non-permeate stream from said membrane unit back to the at least one reactor chamber;

d) wherein said at least one glassy polymer membrane separation unit is a plurality of glassy polymer membrane separation units arranged in parallel.

51. A system for recycling or recovering a perfluorocompound gas from a gas mixture, the system comprising:

a) an optional treatment means for creating a treated gas mixture suitable for compression;

b) a compressor for compressing the treated gas mixture to form a compressed gas mixture; and

c) at least one glassy polymer membrane separation unit having a feed side and a permeate side, said membrane being permeable to at least one carrier gas and being substantially non-permeable to at least one perfluorocompound gas, said membrane unit connected to said compressor via a conduit, said membrane unit having a permeate vent conduit and a non-permeate conduit, said at least one perfluorocompound gas devoid of components including chlorine.

52. System in accordance with claim 51 wherein said compressor is oil-free.

53. System in accordance with claim 51 wherein said the glassy polymer membrane is made of at least one polymer selected from the group consisting of polyimides, polyamides, polyamides-imides, polyesters, polycarbonates, polysulfones, polyethersulfone, polyetherketone, alkyl substituted aromatic polyesters, blends of polyethersulfone, fluorinated aromatic polyimides, polyamides and polyamide-imides, copolymers thereof, substituted polymers thereof.

54. System in accordance with claim 51 further including a vacuum pump in the non-permeate conduit.

55. System in accordance with claim 51 further including a recovery unit connected to said non-permeate conduit.

56. System in accordance with claim 51 further including a recycle conduit connected to said non-permeate conduit.

57. System in accordance with claim 51 further including a second membrane separation unit adapted to take as its feed a non-permeate stream flowing in said non-permeate conduit.

58. System in accordance with claim 57 wherein a permeate stream from said second membrane unit is adapted to be recycled to the feed of the at least one glassy polymer membrane unit.

59. System in accordance with claim 57 further including a third membrane separation unit adapted to take as its feed a permeate stream from said second membrane unit.

60. System in accordance with claim 59 wherein a non-permeate stream from said third membrane unit is adapted to be recycled to the feed of the at least one glassy polymer membrane unit.

61. System in accordance with claim 57 further including sweep gas means for sweeping a permeate side of said second membrane with a portion of a non-permeate stream from said second membrane separation unit.

62. A system for recovering or recycling a perfluorocompound gas, the system comprising:

a) compression means adapted to compress a gas mixture containing a carrier gas and a perfluorocompound gas, said perfluorocompound gas devoid of components including chlorine;

b) at least one glassy polymer membrane separation unit having a feed side and a permeate side, said membrane being permeable to at least one carrier gas and being substantially non-permeable to at least one of said perfluorocompound gases devoid of components including chlorine, said membrane unit connected to said compression means via a conduit, said membrane unit having a permeate vent conduit and a non-permeate conduit;

c) means to recycle at least a portion of a non-permeate stream flowing through said non-permeate conduit from said membrane unit back to a source of said gas mixture;

d) gas treatment means positioned prior to the gas mixture entering the membrane unit, said gas treatment means selected from the group consisting of plasma decomposition, thermal decomposition, catalytic removal, scrubbing, and adsorption;

e) the membrane unit comprising a sweep gas conduit connecting the non-permeate conduit and the permeate side of the membrane;

f) a damper or surge tank positioned in the non-permeate conduit; and

g) a compressor, heat exchanger, cryogenic pump or vacuum pump positioned in the non-permeate conduit upstream of the surge tank, allowing an enriched stream of perfluorocompounds devoid of components including chlorine to be stored in condensed form for future use if so desired.