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Heat transfer surface having a high boiling heat transfer coefficient

阅读:561发布:2022-10-31

专利汇可以提供Heat transfer surface having a high boiling heat transfer coefficient专利检索,专利查询,专利分析的服务。并且A heat transfer surface comprising a heat conductive base member and a plurality of spaced apart fins extending therefrom, each of said fins being bent over towards the next adjacent fin so as to form therebetween elongated, re-entrant cavities. The gap between the tip of one of said fins and the next adjacent fin is sufficiently small to promote and sustain nucleate boiling of a fluid in contact with said fins and said base member.,下面是Heat transfer surface having a high boiling heat transfer coefficient专利的具体信息内容。

1. A heat exchange comprising: a heat conductive base member for transferring heat from a heat source on one side thereof to a boiling fluid on the other side thereof; a plurality of spaced apart fins having substantially smooth and uninterrupted side surfaces extending From said other side of said base member, each of said fins having a base portion joined to said base member and a tip portion, said tip portions being bent over toward the next adjacent one of said fins to form a a continuous gap having a width of from 0.001 to 0.005 inches, the gaps between said tip portions and said next adjacent one of said fins being less than the spaces between said base portions, whereby a continuous reentrant shaped cevity sufficient to promote nucleate boiling of a given liquid is formed between adjacent ones of said fins; said boiling fluid selected from the group of refrigerant fluids consisting of trichloromonofluoromethane, monochlorodifluoromethane, dichlorodifluoromethane, trichlorotrifluoroethane, dichlorotetrafluoroethane and a 48.8/51.2 weight percent azeotropic mixture of monochlorodifluoromethane and monochloropentafluoroethane, respectively.
2. A heat exchanger as defined in claim 1 wherein: said bent fins are of curvilinear cross-section over substantially their entire height.
3. A heat exchanger as defined in claim 1 wherein: said tip portions overlap said base portion of said next adjacent one of said fins by a distance of from one-half to one and one-half times the thickness of one of said fins.
4. A heat exchanger as defined in claim 1 wherein: said boiling fluid comprises trichloromonofluoromethane and said gaps between said tip portions and said next adjacent one of said fins are within a range of from 0.0015 to 0.0035 inches.
5. A heat exchanger as defined in claim 1 wherein: said fins are formed integrally with said base member.
6. A heat exchanger as defined in claim 1 wherein: said tip portions overlap said base portion of said next adjacent fins. 7 In a refrigeration system comprising a compressor, condensor, pressure reducing means and an evaporator of the shell-and-tube type interconnected in refrigerant flow relationship, an improved heat transfer surface for said evaporator comprising: a plurality of tubular members through which a relatively warm fluid to be cooled passes; a plurality of spaced apart fins having substantially smooth and uninterrupted side surfaces extending from each of said tubular members, the outside of said tubular members and said fins being in contact with refrigerant fluid flowing through said evaporator; and each of said fins having a base portion joined to one of said tubular members and a tip portion, each of said tip portions being bent over toward the next adjacent one of said fins to overlap said base portion of said next adjacent one of said fins and being separated therefrom by a gap sufficiently narrow to promote and sustain nucleate boiling of said refrigerant fluid; said boiling fluid selected from the group consisting of trichloromonofluoromethane, monochlorodifuloromethane, dichlorotetrafluoroethane and a 48.8/51.2 weight percent azeotropic mixture of monochlorodifuloromethane and monochloropentafluoroethane, respectively; said gaps between said tip portions and said next adjacent one of said fins being in the range of from 0.001 to 0.005 inches.
8. Apparatus as defined in claim 7 wherein: each of said fins is curved over its entire height towards said next adjacent one of said fins.
9. Apparatus as defined in claim 7 wherein: said refrigerant fluid comprises trichloromonofluoromethane and said gap is between 0.0015 and 0.0035 inches wide.
10. A heat exchanger comprising a plurality of tubes for conducting a relatively warm fluid to be cooled by transferring heat to a boiling fluid surrounding said tubes, helical heat transfer fins on said tubes and extending outwardly from said tube, said helical heat transfer fins having base portions integral with the outer surface of said tube and having substantially smooth and uninterrupted side surfaces and tip portions, said tip portions being bent over toward the next adjacent one of said heat transfer fins, the spAces between said heat transfer fins at their outer ends being less than the spaces between said heat transfer fins at their bases whereby continuous re-entrant shaped cavities are provided to enhance boiling.
11. A heat exchanger as defined in claim 10 wherein the spaces between the fins are of substantially uniform cross-section along substantially the length of the fins.
12. A heat exchanger comprising a plurality of tubes for conducting a relatively warm fluid to be cooled by transferring heat to a boiling fluid surrounding said tubes, helical heat transfer fins on the outer surface of said tubes, said helical fins having base portions integral with the outer surface of said tubes, said fins having substantially smooth and uninterrupted side surfaces and extending outwardly from their base portions to distal portions, the distal portions being curved toward the next adjacent fins, the spaces between the distal portions and the next adjacent fins being less than the spaces between the base portions of the fins whereby substantially continuous re-entrant shaped cavities are provided to enhance boiling.
13. A heat exchanger as defined in claim 12 wherein the spaces between the helical heat transfer fins at their outer ends are substantially uniform in width along substantially the length of the fin.
14. A heat exchanger as defined in claim 12 wherein said helical heat transfer fins are curved in cross-section over substantially their entire height.
15. A heat exchanger comprising a tube for conducting a relatively warm fluid to be cooled by transferring heat to a boiling fluid surrounding said tube, helical heat transfer fins at the outer surface of and substantially co-axially disposed with respect to said tube, said helical fins having base portions integral with the outer surface of said tube, said fins having substantially smooth and uninterrupted side surfaces and extending outwardly from their base portions to distal portions, the distal portions being curved toward one end of the tube and terminating in closely spaced relation with the next adjacent fin to define substantially uniform helical gaps between the distal portions and the next adjacent fins which are substantially less in width than the spaces between the base portions of the fins whereby substantially continuous helically shaped re-entrant cavities are provided to enhance boiling.
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