Falling film evaporator for a vapor compression refrigeration chiller

• US 6,293,112 B1
• Filed: 12/17/1999
• Issued: 09/25/2001
• Est. Priority Date: 12/17/1999
• Status: Expired due to Term

• Current Assignee: Trane International Inc. (Trane Technologies plc)
• Original Assignee: American Standard International Inc (Trane Technologies plc)
• Inventors: Ring, Harry K., Larson, James W., Moeykens, Shane A., Hartfield, Jon P.
• Primary Examiner(s): WAYNER, WILLIAM E
• Application Number:
  US09/466,397
• Time in Patent Office: 648 Days
• Field of Search: 62/84, 625/25, 165/DIG.175, 165/172, 165/115, 165/117
• US Class Current: 62/84
• CPC Class Codes: F25B 2339/0242 having tubular elements
• CPC Class Codes: F25B 2500/01 Geometry problems, e.g. for reducing size
• CPC Class Codes: F25B 39/02 Evaporators
• CPC Class Codes: F28D 3/02 with tubular conduits
• CPC Class Codes: F28D 3/04 Distributing arrangements

Abstract

A falling film evaporator for use in a vapor compression refrigeration chiller preferably employs a two-phase refrigerant distributor that overlies the tube bundle in the evaporator shell. The tube bundle defines at least one vapor lane which facilitates the conduct of refrigerant vapor from the interior of the tube bundle to the exterior thereof in a manner which does not substantially affect the vertically downward flow of liquid refrigerant through the tube bundle and across the vapor lane.

Claims

1. A refrigeration system comprising:

a refrigerant gas compressor;

a condenser, said condenser receiving compressed gas from said compressor and condensing said gas to the liquid state;

a first expansion device, said expansion device being downstream of said condenser and creating a two-phase mixture of refrigerant gas and liquid refrigerant; and

a falling film evaporator, said evaporator having a shell, a tube bundle, a vapor outlet and a refrigerant distributor, said vapor outlet being connected for flow to said compressor and the tubes of said tube bundle running horizontally in said shell, said refrigerant distributor being disposed above said tube bundle within said shell and receiving liquid refrigerant from said expansion device, said distributor depositing liquid refrigerant vertically downward, generally unassisted by pressure, onto the top of said tube bundle, said tube bundle having at least two tube sections and defining at least one vapor lane, said vapor lane being an essentially unobstructed flow path between said tube sections that is sized to facilitate the conduct of refrigerant gas out of the interior of said tube bundle to an exterior side thereof at a velocity and in a manner such that the flow of liquid refrigerant downward through said tube bundle and across said vapor lane is generally unaffected by the cross-flow of refrigerant vapor out of the interior of said tube bundle through said vapor lane.

2. The refrigeration system according to claim 1 wherein a portion of the liquid refrigerant deposited by said distributor onto the top of said tube bundle makes its way to the bottom of and pools in said evaporator, the majority of the tubes of said tube bundle being disposed above said pool.

3. The refrigeration system according to claim 2 wherein said at least one vapor lane is sized so that the downward flow of liquid refrigerant across said vapor lane within said tube bundle is substantially unaffected by the conduct of refrigerant gas through said vapor lane to an exterior side of said tube bundle.

4. The refrigeration system according to claim 3 wherein said distributor is positioned in said shell so that refrigerant conducted out of the interior of said tube bundle to an exterior side thereof by said vapor lane flows to said vapor outlet generally unobstructed by said refrigerant distributor.

5. The refrigeration system according to claim 4 wherein said refrigerant distributor is a two-phase refrigerant distributor which receives both liquid refrigerant and refrigerant gas from said first expansion device, said distributor depositing liquid refrigerant in generally controlled and predictable quantities across the length and width of the portion of the top of the tube bundle that is overlain by said distributor.

6. The refrigeration system according to claim 5 wherein one quarter or fewer of the tubes in said tube bundle are unimmersed in said pool at the bottom of said evaporator.

7. The refrigeration system according to claim 5 wherein said at least one vapor lane is defined within said tube bundle so as to provide a generally unobstructed flow path from the interior of said tube bundle to two exterior sides thereof and wherein liquid refrigerant is deposited in generally uniform quantities across the length and width of the portion of the top of the tube bundle that is overlain by said distributor.

8. The refrigeration system according to claim 5 wherein the flow of liquid refrigerant out of said distributor is generally in droplet form and wherein said refrigerant distributor and said tube bundle define a vapor space therebetween, the vertical dimension of said vapor space being the distance between the underside of said distributor and the top of said tube bundle, said distance being predetermined to facilitate the lateral flow of refrigerant gas out of said vapor space at a velocity which does not substantially disrupt the generally vertically downward deposit of liquid refrigerant droplets from said distributor onto the top of said tube bundle.

9. The refrigeration system according to claim 8 wherein said at least one vapor lane provides a generally continuous flow path from the interior of said tube bundle to two exterior sides thereof from where said refrigerant gas flows from said two exterior sides of said tube bundle to said vapor outlet via flow paths that are essentially unobstructed by said distributor.

10. The refrigeration system according to claim 5 wherein refrigerant flowing from said compressor, to and through said condenser, to and through said first expansion device and to and through said distributor carries with it oil that becomes entrained in said refrigerant within said compressor, said oil making its way into said pool of liquid refrigerant at the bottom of said evaporator shell, said refrigeration system further comprising apparatus for returning oil that makes its way into said pool of liquid refrigerant at the bottom of said evaporator to said compressor.

11. The refrigeration system according to claim 10 wherein said distributor overlies the majority of the length and width of the top of said tube bundle and wherein said at least one vapor lane facilitates the conduct of refrigerant gas from the interior of said tube bundle to first and second exterior sides thereof, said distributor depositing liquid refrigerant in generally uniform quantity across the length and width of the top of the tube bundle which is overlain by said distributor.

12. The refrigeration system according to claim 11 wherein a majority of the tubes in said tube bundle are oriented in a rotated triangular-pitch configuration.

13. The refrigeration system according to claim 12 wherein a minority portion of the tubes in said tube bundle are oriented in a triangular-pitch configuration, the tubes in the uppermost portion of said tube bundle being oriented in said triangular-pitch configuration.

14. The refrigeration system according to claim 10 wherein said first expansion device is disposed adjacent the entrance to said distributor so as to reduce stratification in the two-phase refrigerant mixture received by said distributor from said first expansion device and wherein said refrigerant distributor and said tube bundle define a vapor space therebetween, the vertical dimension of said vapor space being the distance between the underside of said distributor and the top of said tube bundle, said distance being predetermined to facilitate the lateral flow of refrigerant gas out of said vapor space at a velocity which does not substantially disrupt the vertically downward deposit of liquid refrigerant by said distributor onto the top of said tube bundle.

15. The refrigeration system according to claim 10 further comprising an oil concentrator, said oil concentrator being disposed in the bottom of said evaporator, at least one tube of said tube bundle being disposed in said oil concentrator, a portion of the mixture of liquid refrigerant and oil that pools at the bottom of said evaporator entering said oil concentrator, a portion of the liquid refrigerant that enters said concentrator being vaporized by heat exchange contact with said at least one tube, refrigerant vaporized in said concentrator exiting said concentrator and being returned into the interior of said evaporator shell and the remaining portion of the liquid refrigerant and oil in said concentrator being delivered from said oil concentrator to said compressor by said oil return apparatus.

16. The refrigeration system according to claim 5 wherein said evaporator has a tube sheet and includes a waterbox, said waterbox and said tube bundle being disposed on opposite sides of said tube sheet, the ends of the tubes of said tube bundle penetrating said tube sheet, said waterbox having a baffle, said waterbox baffle, by its abutment with said tube sheet, being determinative of which of the tubes in said tube bundle initially receive the heat transfer medium that flows into said evaporator, said waterbox baffle abutting said tube sheet in a location that corresponds to a vapor lane defined by said tube bundle on the other side of said tube sheet.

17. The refrigeration system according to claim 5 wherein said tube bundle defines at least two vapor lanes, each of said at least two vapor lanes being generally unobstructed flow paths running from the interior to first and second exterior sides of said tube bundle.

18. The refrigeration system according to claim 17 wherein each of said at least two vapor lanes are sized so that the downward flow of liquid refrigerant thereacross within said tube bundles is substantially unaffected by the conduct of refrigerant gas out of the interior of said tube bundle through said vapor lanes and wherein a portion of at least one of said at least two vapor lanes has a vertically upward bias.

19. The refrigeration system according to claim 17 further comprising a baffle for regulating the flow to said vapor outlet of refrigerant gas which is conducted to the exterior sides of said tube bundle through said vapor lanes, said baffle supporting said distributor within said shell.

20. The refrigeration system according to claim 5 further comprising a baffle, said baffle being interposed between the vapor outlet of said evaporator and the location at the exterior side of said tube bundle to which said vapor lane conducts refrigerant gas from interior of said tube bundle, said baffle regulating the flow of refrigerant gas to said vapor outlet.

21. The refrigeration system according to claim 20 wherein said baffle supports said distributor within said shell.

22. The refrigeration system according to claim 21 wherein said baffle defines a plurality of apertures through which refrigerant gas flows enroute from said tube bundle to said vapor outlet.

23. The refrigeration system according to claim 21 wherein said tube bundle defines at least two vapor lanes, each of said at least two vapor lanes providing a generally unobstructed flow path from the interior of said tube bundle to two exterior sides thereof and at least one of said vapor lanes having a vertically upward bias.

24. The refrigeration system according to claim 1 wherein said evaporator has at least two refrigerant distributors, each of said distributors receiving a two-phase refrigerant mixture from said expansion device.

25. The refrigeration system according to claim 24 wherein said tube bundle has at least two horizontally adjacent tube banks, each of said tube banks being overlain by at least one two-phase refrigerant distributor and cooperating to define a generally vertically running space therebetween, each of said tube banks defining at least one vapor lane to facilitate the flow of refrigerant gas from interior thereof into said vertically running space, the flow path for refrigerant gas from said vertically running space to said vapor outlet being generally unobstructed by a refrigerant distributor.

26. The refrigeration system according to claim 25 wherein said distributors are supported in said shell by a baffle, said baffle regulating the flow of refrigerant gas to the vapor outlet of said evaporator.

27. The refrigeration system according to claim 1 wherein said evaporator has a waterbox and a tube sheet, said tube bundle and said first waterbox being disposed on opposite sides of said tube sheet, said tube sheet being penetrated by the ends of the tubes of said tube bundle, the portion of said tube sheet that is unpenetrated by said tube ends and which corresponds to the location of a vapor lane defined by said tube bundle being generally solid and continuous, said waterbox including a baffle, said baffle abutting said generally solid and continuous portion of said tube sheet that corresponds to the location of a vapor lane defined by said tube bundle and directing the flow of said heat transfer medium, as it enters said evaporator, into said first portion of the tubes.

28. The refrigeration system according to claim 27 wherein said first portion of the tubes of said tube bundle is generally vertically below said second portion of the tubes of said tube bundle so that the flow of said heat transfer medium into, through and out of said evaporator is from the bottom to the top of said tube bundle.

29. The refrigeration system according to claim 1 further comprising an economizer and a second expansion device and wherein said refrigerant distributor is a two-phase refrigerant distributor that overlies the majority of the length and width of the top of said tube bundle and deposits liquid refrigerant in generally uniform quantity thereover, said second expansion device receiving liquid refrigerant from said condenser and creating a two-phase mixture of liquid refrigerant and refrigerant gas that is communicated to said economizer, the gaseous portion of said two-phase mixture being communicated from said economizer to said compressor and the liquid portion thereof being communicated to said first expansion device.

30. A falling film evaporator for a vapor compression refrigeration system comprising:

a shell, said shell having a vapor outlet;

a tube bundle, the tubes of said tube bundle running horizontally in said shell, said tube bundle having at least one vapor lane and at least two tube sections, said vapor lane being an essentially unobstructed flow path that is defined between said at least two tube sections through which refrigerant gas flows from the interior to an exterior side of said tube bundle and thence to said vapor outlet, said vapor lane being sized so that the flow of refrigerant gas therethrough to said exterior side of said tube bundle is at a velocity which generally does not disrupt the downward flow of liquid refrigerant through said tube bundle and across said vapor lane; and

a refrigerant distributor, said refrigerant distributor being mounted vertically above said tube bundle within said shell and depositing liquid refrigerant, in generally predictable and controlled quantities, onto the top of said tube bundle by force of gravity and generally unassisted by pressure so that said liquid refrigerant falls out of said distributor generally vertically downward onto the top of said tube bundle.

31. The falling film evaporator according to claim 30 wherein a portion of the liquid refrigerant issuing from said distributor makes its way to the bottom of and pools in said evaporator, the majority of the tubes of said tube bundle of said evaporator being disposed vertically above said pool.

32. The falling film evaporator according to claim 31 wherein said refrigerant distributor is a two-phase distributor and is positioned so that the flow of refrigerant gas out of said vapor lane to said vapor outlet is generally unobstructed by said refrigerant distributor.

33. The falling film evaporator according to claim 32 wherein said at least one vapor lane is sized so that the velocity of refrigerant gas flowing therethrough from the interior of said tube bundle to said exterior side thereof does not substantially affect the vertically downward flow of liquid refrigerant across said vapor lane within said tube bundle.

34. The falling film evaporator according to claim 33 wherein the liquid refrigerant deposited onto the top of said tube bundle by said distributor is generally in droplet form and is in generally uniform quantity across the length and width of the portion of the top of the tube bundle which is overlain by said distributor.

35. The falling film evaporator according to claim 34 wherein said at least one vapor lane provides a generally continuous and unobstructed flow path for refrigerant gas from the interior of said tube bundle to two exterior sides thereof from where said refrigerant gas flows to said vapor outlet essentially unobstructed by said distributor.

36. The falling film evaporator according to claim 35 wherein said refrigerant distributor, in addition to receiving and distributing liquid refrigerant and refrigerant vapor internal of said shell, receives oil that makes its way thereto from the compressor of said vapor compression refrigeration system, said oil making its way into said pool of liquid refrigerant at the bottom of said evaporator shell.

37. The falling film evaporator according to claim 35 wherein said refrigerant distributor and said tube bundle define a vapor space therebetween, the vertical dimension of said vapor space being the distance between the underside of said distributor and the top of said tube bundle, said distance being predetermined so as to facilitate the lateral flow of refrigerant gas out of said vapor space at a velocity which essentially does not disrupt the generally vertically downward fall of liquid refrigerant droplets from said distributor onto the top of said tube bundle, said at least one vapor lane likewise being sized so that the velocity of refrigerant gas flowing therethrough from the interior to the exterior of said tube bundle does not substantially affect the vertically downward flow of liquid refrigerant through said tube bundle and across said vapor lane.

38. The falling film evaporator according to claim 35 further comprising a baffle, said baffle being interposed between said vapor outlet and the locations at the exterior sides of said tube bundle to which said at least one vapor lane delivers refrigerant gas from the interior thereof and regulating the flow of refrigerant gas from the exterior sides of said tube bundle to said vapor outlet.

39. The falling film evaporator according to claim 38 wherein said baffle supports said distributor within said shell.

40. The falling film evaporator according to claim 35 further comprising an oil concentrator, said oil concentrator being disposed in the bottom of said evaporator, at least one tube of said tube bundle being disposed in said oil concentrator, a mixture of liquid refrigerant and oil entering said oil concentrator from the pool of liquid refrigerant and oil that is found at the bottom of said evaporator, a portion of the liquid refrigerant in said mixture that enters said concentrator being vaporized within said concentrator, the vaporized refrigerant exiting said concentrator and being returned into the interior of said evaporator shell, the remaining portion of said mixture in said concentrator containing an increased concentration of oil as a result of the vaporization of liquid refrigerant within said oil concentrator.

41. The falling film evaporator according to claim 35 wherein a majority of the tubes in said tube bundle are oriented in a rotated triangular-pitch configuration so that liquid refrigerant flowing downward through the majority of the tubes in said tube bundle falls generally from a first horizontal row of tubes in said tube bundle onto tubes in the horizontal row of tubes immediately below.

42. The falling film evaporator according to claim 41 wherein a minority portion of the tubes in said tube bundle are oriented in a triangular-pitch configuration.

43. The falling film evaporator according to claim 35 wherein said evaporator has a tube sheet and a waterbox, said tube bundle and said waterbox being on opposite sides of said tube sheet, the ends of the tubes of said tube bundle penetrating said tube sheet, said waterbox having a baffle which, by its abutment with said tube sheet, determines which of the tubes in said tube bundle initially receive the heat transfer medium that flows into said evaporator, said waterbox baffle abutting said tube sheet in a location that corresponds to a vapor lane defined by said tube bundle on the other side of said tube sheet.

44. The falling film evaporator according to claim 35 wherein said evaporator has at least two refrigerant distributors, each of said distributors being two-phase refrigerant distributors.

45. The falling film evaporator according to claim 35 wherein said tube bundle has at least two tube banks, each of said tube banks being overlain by at least one refrigerant distributor, said tube tanks cooperating to define a generally vertically running space therebetween and each of said tube banks defining at least one vapor lane to facilitate the flow of refrigerant gas from the interiors thereof into said vertically running space, the flow path for refrigerant gas to said vapor outlet from said vertically running space being generally unobstructed by a refrigerant distributor.

46. The falling film evaporator according to claim 35 wherein said tube bundle defines at least two vapor lanes, both of said vapor lanes defining a generally continuous and unobstructed flow path from the interior of said tube bundle to two exterior sides thereof.

47. The falling film evaporator according to claim 35 further comprising an expansion device, said expansion device being disposed adjacent the inlet to said refrigerant distributor and delivering two-phase refrigerant thereinto.

48. A method for managing vapor flow internal of a falling film evaporator which employs a two-phase refrigerant distributor and which is used in a vapor compression refrigeration system comprising the steps of:

positioning said refrigerant distributor vertically above the tube bundle within the shell of said evaporator;

delivering a two-phase mixture of liquid refrigerant and refrigerant gas into said distributor;

flowing said two-phase refrigerant mixture internal of said distributor so that at least the liquid portion of said two-phase mixture is made available for distribution generally throughout the length and width thereof;

depositing, in a generally vertically downward direction and in relatively low-energy droplet form, the liquid refrigerant portion of said two-phase mixture across the portion of the top of said tube bundle that is overlain by said distributor;

flowing liquid refrigerant deposited onto the top of said tube bundle generally vertically downward therethrough;

defining at least one generally unobstructed vapor lane within said tube bundle that runs from the interior to an exterior side thereof, said vapor lane dividing said tube bundle generally into two tube sections and being sized to conduct refrigerant gas from the interior to an exterior side of said tube bundle at a velocity which generally does not disrupt the downward flow of liquid refrigerant through said tube bundle and across said vapor lane; and

flowing the refrigerant gas conducted via said vapor lane out of the interior of said tube bundle to the vapor outlet of said evaporator by a path that is generally unobstructed by said distributor.

49. The method according to claim 48 comprising the further step of collecting at least a portion of the liquid refrigerant that is deposited onto the top of and flows downward through said tube bundle in a pool at the bottom of said evaporator shell.

50. The method according to claim 49 disposing a minority portion of the tubes of said tube bundle in said pool of liquid refrigerant that is collected in the bottom of said evaporator shell.

51. The method according to claim 50 comprising the further step sizing said vapor lane so that the downward flow of liquid refrigerant across said vapor lane is substantially unaffected by the conduct of refrigerant gas from the interior of said tube bundle through said vapor lane to an exterior side thereof.

52. The method according to claim 51 wherein said step of defining said vapor lane includes the step of providing a generally unobstructed and continuous flow path for the conduct of refrigerant gas out of the interior of said tube bundle to two exterior sides thereof.

53. The method according to claim 52 wherein said step of depositing liquid refrigerant onto the top of said tube bundle includes the step of depositing generally uniform quantities of liquid refrigerant across the length and width of said tube bundle that is overlain by said distributor.

54. The method according to claim 53 comprising the further step of defining a vapor space between said distributor and the top of said tube bundle, the vertical dimension of said vapor space being the distance between the underside of said distributor and the top of said tube bundle, said distance being predetermined to facilitate the lateral flow of refrigerant gas out of said vapor space at a velocity which does not substantially disrupt the generally vertically downward deposit of liquid refrigerant from said distributor to the top of said tube bundle.

55. The method according to claim 53 comprising the further step of orienting a majority of the tubes of said tube bundle that are located vertically above said pool in said evaporator in a rotated triangular-pitch configuration so that the downward flow of liquid refrigerant through said majority of tubes located above said pool is from the tubes in one horizontal row of tubes in said tube bundle downward onto corresponding vertically aligned tubes in the horizontal row of tubes immediately below said one horizontal row.

56. The method according to claim 53 comprising the further step of regulating the flow of refrigerant gas from said tube bundle to said vapor outlet by a use of a baffle.

57. The method according to claim 56 comprising the further step of supporting said distributor in said evaporator shell with said baffle.

58. The method according to claim 53 comprising the further step of reducing the stratification in the two-phase mixture of refrigerant received into said distributor by disposing an expansion device adjacent the entry to said refrigerant distributor.

59. The method according to claim 53 comprising the further step of defining a plurality of vapor lanes in said tube bundle.

60. The method according to claim 53 wherein said evaporator includes a tube sheet and a waterbox, the ends of the tubes of said tube bundle penetrating said tube sheet and said tube bundle and waterbox being disposed on opposite sides of said tube sheet, and further comprising the step of directing the heat transfer medium that flows through said evaporator into a first portion of the tubes of said tube bundle by the use of a waterbox baffle that abuts said tube sheet in a location that corresponds to a vapor lane defined by said tube bundle.

61. The method according to claim 53 wherein said tube bundle has at least two tube banks, each of said tube banks being overlain by a refrigerant distributor, and comprising the further steps of defining a generally vertically running space between said tube banks;

defining at least one vapor lane in each of said tube banks that opens into said generally vertically running space;

conducting refrigerant gas out of the interior of each of said tube banks into said vertically running space; and

, conducting refrigerant gas from said vertically running space to the vapor outlet of said evaporator through a flow path that is generally unobstructed by a refrigerant distributor.

62. The method according to claim 53 comprising the further steps of receiving oil as well as two-phase refrigerant into said distributor;

flowing said oil out of said distributor and downward through said tube bundle into said pool of liquid refrigerant at the bottom of said evaporator shell; and

returning a mixture of liquid refrigerant and oil from said pool at the bottom of said evaporator to the compressor of said vapor compression refrigeration system.

63. The method according to claim 62 comprising the further steps of increasing the concentration of oil in the mixture of liquid refrigerant and oil that is returned from said evaporator pool to said compressor in said returning step by vaporizing a portion of the liquid refrigerant in said mixture within said shell.

64. The method according to claim 53 comprising the further steps of reducing the pressure of liquid refrigerant received from the condenser a first time so as to create a lower pressure mixture of liquid and gaseous refrigerant;

delivering said gaseous refrigerant portion of said lower pressure refrigerant mixture to the compressor of said refrigeration system;

lowering the pressure of the liquid portion of said lower pressure refrigerant mixture a second time so as to create a second and still lower pressure mixture of liquid refrigerant and refrigerant gas; and

wherein the two-phase mixture of refrigerant delivered in said delivering step is said second and still lower pressure mixture of liquid refrigerant and refrigerant gas.