Method and apparatus for controlling freezing nucleation and propagation
View Patent ↗An apparatus and method of controlling freezing in a liquid system is disclosed. The apparatus includes a heat exchanger having a initial zone characterized by a surface area to volume ratio. The apparatus also includes means for initiating freezing of a fluid from the initial zone to facilitate volume expansion during freezing in the direction of a final zone characterized by a final zone surface area to volume ratio. The apparatus can further include a plurality of zones located between the initial zone and the final zone, wherein a zone surface area to volume ratio is calculated for each zone. Preferably, the zone surface area to volume ratio of each zone progressively decreases from the initial zone in the direction of the final zone. Preferably, the final freezing zone has the lowest surface area to volume ratio and has sufficient elasticity to accommodate the volume expansion of all the fluid that has frozen from the initial zone.
1. An apparatus for controlling freezing nucleation and propagation in a liquid system, comprising:
a. a member having an initial zone characterized by an initial surface area to volume ratio; and
b. means for initiating freezing of a fluid from the initial zone to facilitate volume expansion during freezing in a direction that progresses through a series of subzones, each characterized by calculated surface area to volume ratio, to a final zone characterized by a final zone surface area to volume ratio, wherein the final zone surface area to volume ratio is lower than the initial surface area to volume ratio.
2. The apparatus of claim 1 wherein the member comprises a heat exchanger.
3. The apparatus of claim 2 wherein the heat exchanger includes an inlet port extending through a first opening of the heat exchanger for conveying the fluid to a plurality of channels and passages and an outlet port extending through a second opening for discharging the fluid from the plurality of channels and passages.
4. The apparatus of claim 3 wherein the heat exchanger includes multiple inlet ports and multiple outlet ports.
5. The apparatus of claim 1 , wherein the final zone accommodates an expanded volume when the fluid freezes.
6. The apparatus of claim 1 wherein the calculated zone surface area to volume ratio of each subzone progressively decreases from the initial zone in the direction of the final zone.
7. The apparatus of claim 1 further including one or more compressible objects coupled to the final zone wherein pressure exerted on the compressible object by the freezing fluid increases a volume of the final zone.
8. The apparatus of claim 7 wherein the compressible objects are confined within the final zone.
9. The apparatus of claim 7 wherein the compressible objects are made of one of the following: sponge, foam, air-filled bubbles, sealed tubes and balloons.
10. The apparatus of claim 9 wherein the sponge is hydrophobic.
11. The apparatus of claim 9 wherein the foam is hydrophobic.
12. The apparatus of claim 1 further including at least one air pocket disposed in the final zone wherein the air pocket accommodates the expansion by the freezing fluid.
13. The apparatus of claim 1 further including at least one air pocket disposed along a freezing path in at least one of the zones and subzones.
14. A heat exchanger, comprising:
a. an initial zone characterized by a initial surface area to volume ratio; and
b. means for initiating freezing of a fluid from the initial zone to accommodate volume expansion during freezing in the direction of a final zone characterized by a final zone surface area to volume ratio, wherein the final zone surface area to volume ratio is lower than the initial surface area to volume ratio.
15. The heat exchanger of claim 14 wherein the final zone accommodates an expanded volume when the fluid freezes.
16. The heat exchanger of claim 14 wherein the heat exchanger includes an inlet port extending through a first opening of the heat exchanger for conveying the fluid to a plurality of microstructures and an outlet port extending through a second opening for discharging the fluid from the plurality of channels and passages.
17. The heat exchanger of claim 16 wherein the heat exchanger includes multiple inlet ports and multiple outlet ports.
18. The heat exchanger of claim 14 wherein the final zone elasticity is sufficient to expand outwardly to accommodate the volume expansion caused by the freezing of the fluid.
19. The heat exchanger of claim 14 further including a plurality of subzones located between the initial zone and the final zone, wherein a zone surface area to volume ratio of each subzone progressively decreases from the initial zone in the direction of the final zone.
20. The heat exchanger of claim 19 wherein at least one of the subzones is constructed of a structure to obtain a predetermined surface area to volume ratio.
21. The heat exchanger of claim 20 wherein the structure is a copper foam.
22. The heat exchanger of claim 14 wherein at least one of the zones is constructed of a structure to obtain a predetermined surface area to volume ratio.
23. The heat exchanger of claim 22 wherein the structure is a copper foam.
24. The heat exchanger of claim 14 further including one or more compressible objects coupled to the tubular member wherein pressure exerted on the compressible object by the freezing fluid increases a volume of the final zone.
25. The heat exchanger of claim 24 wherein the compressible objects are made of one of the following: sponge, foam, air-filled bubbles, sealed tubes and balloons.
26. The heat exchanger of claim 25 wherein the sponge is hydrophobic.
27. The heat exchanger of claim 25 wherein the foam is hydrophobic.
28. The heat exchanger of claim 14 further including at least one air pocket disposed in the final zone wherein the air pocket accommodates the expansion by the freezing fluid.
29. The heat exchanger of claim 14 further including at least one air pocket disposed along a freezing path in at least one of the zones and subzones.
30. A heat exchanger, comprising:
a. an inlet port extending through a first opening of the heat exchanger for conveying a fluid to a plurality of channels and passages;
b. an outlet port extending through a second opening for discharging the fluid from the plurality of channels and passages; and
c. means for initiating freezing from an initial zone of the heat exchanger characterized by an initial zone surface area to volume ratio to facilitate volume expansion during freezing in the direction of the inlet and outlet ports to a tubular member having a final zone characterized by a final zone surface area to volume ratio lower than the initial zone surface area to volume ratio.
31. The heat exchanger of claim 30 wherein the final zone elasticity is sufficient to expand outwardly to accommodate the volume expansion caused by the freezing of the fluid.
32. The heat exchanger of claim 30 further including a plurality of subzones located between the initial zone and the final zone, wherein a zone surface area to volume ratio of each subzone progressively decreases from the initial zone in the direction of the final zone.
33. The heat exchanger of claim 32 wherein at least one of the subzones is constructed of a structure to obtain a predetermined surface area to volume ratio.
34. The heat exchanger of claim 33 wherein the structure is a copper foam.
35. The heat exchanger of claim 30 wherein at least one of the zones is constructed of a structure to obtain a predetermined surface area to volume ratio.
36. The heat exchanger of claim 35 wherein the structure is a copper foam.
37. The heat exchanger of claim 30 wherein the heat exchanger includes multiple inlet ports and multiple outlet ports.
38. A method of controlling freezing nucleation and propagation in a liquid system, comprising the steps of:
a. initiating freezing of fluid from an initial zone of a heat exchanger and characterized by a an initial zone surface area to volume ratio; and
b. directing the frozen fluid to a final zone characterized by a final, lower, surface area to volume ratio.
39. The method of claim 38 wherein the final zone accommodates an expanded volume when the fluid freezes.
40. The method of claim 38 wherein the heat exchanger includes an inlet port extending through a first opening of the heat exchanger for conveying the fluid to a plurality of channels and passages and an outlet port extending through a second opening for discharging the fluid from the plurality of channels and passages.
41. The method of claim 40 wherein the heat exchanger includes multiple inlet ports and multiple outlet ports.
42. The method of claim 38 wherein the final zone elasticity is sufficient to expand outwardly to accommodate the volume expansion caused by the freezing of the fluid.
43. The method of claim 38 wherein a plurality of subzones are located between the initial zone and the final zone, and wherein a zone surface area to volume ratio of each subzone progressively decreases from the initial zone in the direction of the final zone.
44. An apparatus for controlling freezing nucleation and propagation in a liquid system, comprising:
a. a member having an initial zone characterized by an initial surface area to volume ratio; and
b. means for initiating freezing of a fluid from the initial zone to facilitate volume expansion during freezing in a direction that progresses through a series of subzones, each characterized by calculated surface area to volume ratio, to a final zone characterized by a final zone surface area to volume ratio, wherein at least one of the subzones is constructed of a copper foam to obtain a predetermined surface area to volume ratio.
45. The apparatus of claim 44 further including one or more compressible objects coupled to the final zone wherein pressure exerted on the compressible object by the freezing fluid increases a volume of the final zone.
46. The apparatus of claim 44 further including at least one air pocket disposed in the final zone wherein the air pocket accommodates the expansion by the freezing fluid.
47. The apparatus of claim 44 further including at least one air pocket disposed along a freezing path in at least one of the zones and subzones.
48. An apparatus for controlling freezing nucleation and propagation in a liquid system, comprising:
a. a member having an initial zone characterized by an initial surface area to volume ratio; and
b. means for initiating freezing of a fluid from the initial zone to facilitate volume expansion during freezing in a direction that progresses through a series of subzones, each characterized by calculated surface area to volume ratio, to a final zone characterized by a final zone surface area to volume ratio, wherein the final zone alone expands to accommodate an expanded volume when the fluid freezes.
49. The apparatus of claim 48 wherein the compressible objects are confined within the final zone.
50. The apparatus of claim 49 wherein the sponge is hydrophobic.
51. The apparatus of claim 49 wherein the foam is hydrophobic.
52. The apparatus of claim 48 wherein the compressible objects are made of one of the following: sponge, foam, air-filled bubbles, sealed tubes and balloons.