This disclosure relates generally to heat exchangers and, more particularly, to providing a more uniform distribution of fluid amongst a plurality of parallel, fluid conveying passages of a parallel flow heat exchanger.
Parallel flow heat exchangers include a plurality of spaced parallel passages for conveying a first fluid in heat exchange relationship with a second fluid. A type of parallel flow heat exchanger commonly used as refrigerant evaporators, condensers, and gas coolers in refrigeration and air conditioning applications, as well as used as fluid heating and cooling heat exchangers in other applications, includes a plurality of tubes defining the fluid conveying passages. The tubes are disposed in spaced parallel relationship and open into a common manifold for receiving fluid. Typically, it is desirable that each tube, and even channel for multi-channel tubes receive an equal flow of fluid a fluid chamber within to the manifold into which the inlet end of the tubes open. However, conventional parallel flow heat exchangers, in particular parallel flow heat exchangers having multi-channel tubes, such as mini-channel or micro-channel tubes, suffer from fluid maldistribution, that is from a lack of uniformity in the amount of fluid distributed to each individual multi-channel tube.
Flow maldistribution is particularly problematic in applications where a two-phase fluid is delivered to the fluid chamber of the manifold for distribution amongst an aligned array of the plurality of tubes opening into the fluid chamber of the manifold at spaced intervals along the length of the manifold. For example, in a conventional refrigeration/air conditioning cycle, refrigerant is expanded in an expansion valve and then delivered into the manifold of the evaporator as a two-phase mixture of refrigerant vapor and refrigerant liquid. It is generally accepted that flow maldistribution in two-phase flow heat exchangers may primarily be attributed to the difference in densities of liquid phase and the vapor phase. Additionally, gravity forces may separate the liquid and vapor phases as the two-phase mixture passes along the length of the manifold.
It has been recognized that the maldistribution of the refrigerant flow amongst the tubes of a parallel flow heat exchanger may adversely impact evaporator performance and degrade overall system performance. U.S. Pat. Nos. 8,113,270 and 8,171,987, for example, each disclose the use of an elongated distributor tube inserted within and extending along the longitudinal axis of an inlet manifold of a heat exchanger for distributing a two-phase flow along the length of the manifold.
Although the concept of an elongated distribution tube within the inlet header of heat exchanger has been successful in reducing two-phase flow maldistribution, the need still exists for a two-phase flow distributor and heat exchanger that address the maldistribution of the liquid-phase and the vapor-phase in the fluid flow distribution amongst a plurality of flow passages opening to an inlet manifold of a parallel flow heat exchanger.
A parallel flow heat exchanger includes a distribution manifold having a manifold inner wall enclosing a manifold volume, a plurality of longitudinally spaced tubes having inlet ends opening into the manifold volume, and a longitudinally extending distributor body disposed within the manifold volume. The distributor body has a first surface juxtaposed in spaced relationship with the inlet ends of the plurality of tubes and a second surface interfacing with the manifold inner wall. A plurality of discrete flow passages extend from a first end of the distributor body and opening through the first surface of the distributor body. The plurality of discrete flow passages includes a plurality of longitudinally extending passages formed along the interface of the second surface of the distributor body with the inner wall of the distributor manifold. The plurality of discrete flow passages may further include a plurality of transversely extending flow passages, each longitudinally extending flow passage being in fluid flow communication with a respective subplurality of said plurality of transversely extending flow passages. Each respective subplurality of the transversely extending flow passages comprises a continuous sequential subplurality of the transversely extending flow passages distinct from all other subpluralities of the transversely extending flow passages.
A fluid flow distributor includes a longitudinally elongated distributor manifold, a longitudinally elongated distributor body disposed within the distributor manifold, and a plurality of discrete flow passages. The distributor manifold has a bounding wall defining an interior manifold volume and has an array of a plurality of longitudinally spaced slots extending through the bounding wall. The distributor body has a first surface juxtaposed in spaced relationship with and facing the array of slots and a second surface interfacing with the bounding wall of the distributor manifold. The plurality of discrete flow passages extend from a first end of the distributor body to open through the first surface. The plurality of discrete flow passages include a plurality of longitudinally extending flow passages and a plurality of transversely extending flow passages opening through the first surface at longitudinally spaced intervals. Each longitudinally extending flow passage of the plurality of longitudinally extending flow passages is in fluid flow communication with at least one transversely extending flow passage of the plurality of transversely extending flow passages.
In an embodiment, a plurality of channels are formed in the second surface of the distributor body, the plurality of channels forming, in cooperation with the bounding wall of the distribution manifold, the plurality of discrete longitudinally extending flow passages. In an embodiment, a plurality of channels are formed in an inner surface of the bounding wall of the distribution manifold, said plurality of channels forming, in cooperation with the second surface of the distributor body, the plurality of discrete longitudinally extending flow passages. In an embodiment, the manifold may have a circular cross section and the distributor body may have a generally D-shaped semi-circular cross-section. In an embodiment, the distributor manifold may have a non-circular cross-section and the second surface of the distributor body may conform to an interfacing section of an inner surface of the bounding manifold wall.
In an embodiment, a plurality of discharge ports are formed in the first surface of the distributor body opening to the manifold volume, each respective discharge port of the plurality of discharge ports in fluid flow communication with a respective one of the plurality of discrete fluid flow passages. Each fluid flow passage of the plurality of discrete fluid flow passages communicates in fluid flow communication with a selected grouping of a subplurality of the plurality of longitudinally spaced discharge ports. The plurality of discharge ports may be arranged in a single longitudinally extending column or in a plurality of longitudinally extending columns, or the plurality of discharge ports may be arranged in an array of a plurality of longitudinally spaced rows and a plurality of laterally spaced columns.
In an embodiment, a longitudinally extending discharge slot is formed in the first surface of the distributor body opening to the manifold, the plurality of discrete fluid flow passages in fluid flow communication with the discharge slot. In an embodiment, the distributor body includes a longitudinally extending trench in fluid flow communication with each of the plurality of fluid flow passages and in fluid flow communication with a longitudinally elongated discharge slot.
A method is provided for distributing a two-phase fluid flow amongst a plurality of heat exchange tubes of a heat exchanger having a fluid distribution manifold having an inner wall bounding an interior volume, the heat exchange tubes having inlet ends opening into the interior volume of said fluid distribution manifold. The method includes: providing a distributor body having a first surface and a second surface, the second surface configured to conform to a section of the inner wall of the fluid distribution manifold; disposing the distributor body within the interior volume of the distribution manifold with the first surface facing the inlet ends of the heat exchanges tubes and the second surface interfacing with the inner wall of the distribution manifold; and providing a plurality of fluid flow passages extending from an inlet end of the distributor body to open through the first surface of the distributor body, each fluid flow passage including a longitudinally extending passage extending along the interface between the second surface of the distributor body and the inner wall of the distribution manifold and a plurality of transversely extending passages opening through the first surface of the distributor body, each fluid flow passage of said plurality of fluid flow passages delivering fluid flow to a respective region of the heat exchanger.
For a further understanding of the disclosure, reference will be made to the following detailed description which is to be read in connection with the accompanying drawings, wherein:
Referring now to
The invention disclosed herein will be further described with the reference to the heat exchanger 10 in application as an evaporator heat exchanger in a direct expansion refrigeration system (not shown) wherein refrigerant flowing through the refrigeration system passes in heat exchange relationship with a heating fluid, for example air to be cooled, and is evaporated as the refrigerant traverses the heat exchanger 10. Prior to entering the interior chamber 18 of the fluid distribution manifold 12, the refrigerant traverses an expansion device 22, for example a thermostatic expansion valve, an electronic expansion valve, a capillary tube, or other expansion device. As the refrigerant passes through the expansion device 22, the refrigerant is expanded from a higher pressure liquid to a lower pressure two-phase mixture of refrigerant liquid and refrigerant vapor.
Referring now to
The first surface 26 of the distributor body 24 has a plurality of discharge ports 32 therein opening to the interior chamber 18 of the fluid distribution manifold 12. A plurality of flow passages 36 extend from an inlet end 34 of the distributor body 24 to the discharge ports 32 in the first surface 26 of the distributor body 24. Each flow passage 36 includes a longitudinally extending passage 38 and a plurality of transversely extending flow passages 40. The plurality of transversely extending passages 40 extend through the otherwise solid extrusion forming the distributor body 24 to open through a corresponding number of the plurality of discharge ports 32 to the region of the interior volume 18 bounding the first surface 26 of the distributor body 24. The discharge ports 32 and the transversely extending flow passages 40 may be drilled into the solid distributor body 24 and may, for example, have a diameter on the order of 1 to 2 millimeters, although other diameters may be used. The number of discharge ports 32 need not be equal in number to the number of fluid passes 16 of heat exchanger 10. In an embodiment, a single discharge slot extending longitudinally the length of the first surface 26 of the distributor body 24 may replace and constitute the equivalent of the plurality of discrete ports 32. In an embodiment, a plurality of longitudinally extending discharge slots spaced along the length of the first surface 26 of the distributor body 24 may replace and constitute an equivalent of the plurality of discrete ports 32.
The plurality of longitudinally extending passages 38 may extend longitudinally from the inlet end 34 of the distributor body 24 along the interface between the second surface 28 of the distributor body 24 and the inner wall 30 of the fluid distribution manifold 12. In an embodiment, the longitudinally extending passages 38 may comprise channels formed in the second surface 28. In an embodiment, the channels formed in the second surface 28 may comprise longitudinally extending grooves 42 having a generally semi-circular cross-section, such as depicted in
In another embodiment, the longitudinally extending passages 38 may comprise channels, such as semi-circular grooves 46 as depicted in
Accordingly, in each of the embodiments depicted in
As noted hereinbefore, a plurality of transversely extending flow passages 40 extend through the distributor body 24. Each transversely extending flow passage 40 opens at a first end to the interior volume 18 through a respective one of the discharge ports 32 formed in the first surface 26 of the distributor body 24 at longitudinally spaced intervals. Each transversely extending flow passage 40 opens at its other end into one of the longitudinally extending passages 38, thereby providing a fluid flow path extending from the interior volume 18 of the fluid distribution manifold 12 upstream of the inlet end 34 of the distributor body 24, through the distributor body 24 to open through a respective one of the discharge ports 32 into the portion of the interior volume 18 lying between the first surface 26 of the distributor body 24 and the inlet ends of the heat exchanger tubes 14.
Referring now to
An end plate 48 disposed at the upstream end of the distributor body 24 extends across interior volume 18 of the distributor body 24 so that fluid must flow into the channels 42, 44, 46, and cannot flow directly along the first surface 26 of the distributor body 24. The end plate 48 includes a plurality of ports 60 commensurate in number to the number of longitudinally extending flow passages 38 and positioned in alignment with the openings to the channels forming the longitudinally extending flow passages 38. The ports 60 may comprise flow control orifices for allowing a degree of selective adjustment of the flow area opening to the individual flow passages 38 to precisely apportion the flow of the homogenous two-phase mixture amongst the fluid flow passages 38 to account for differences in frictional losses due to the different lengths of the fluid flow passages 38. End plate 48 may be formed integrally with the upstream/inlet end of the distributor body 24 or may be a separate piece that is simply positioned in abutting relationship to the upstream/inlet end of the distributor body 24.
Each longitudinally extending flow passage 38 is in fluid flow communication with a respective subset of the plurality of transversely extending flow passages 40. Each respective subset of the plurality of transversely extending flow passages 40 comprises a continuous sequential grouping of a selected subplurality of the plurality of transversely extending flow passages 40 distinct from all other subsets of the transversely extending flow passages 40. Therefore, each longitudinally extending flow passage 38 is in fluid flow communication with a unique subset of the plurality of transversely extending flow passages 40 relative to all other longitudinally extending flow passages 38.
For example, in the embodiment of the distributor body 24 depicted in
Referring now to
As noted previously, in an embodiment of the distributor 20 disclosed herein, a longitudinally extending discharge slot may be provided in the first surface 26 of the distributor body 24, rather than a plurality of discharge ports 32, for delivering the fluid flow to the interior volume bounding the first surface 26 of the distributor body 24. In the embodiment of the distributor 20 depicted in
Generally, if the number of longitudinally extending passages 38 is “n”, each longitudinally extending passage 38 will be in fluid flow communication with “1/n” of the transversely extending passages 40. However, it is not necessary that all longitudinally extending flow passages 38 be in fluid flow communication with the same number of transversely extending flow passages 40. If desired, one or more of the longitudinally extending flow passages 38 may be in fluid flow communication with a greater number or a lesser number of transversely extending flow passages 40 as compared to the other longitudinally extending flow passages 38. The number of longitudinally extending passages 38 provided depends on the fluid flow requirements for a particular application, the size of the distributor body, and structural considerations. Typically, the number of longitudinally extending passages 38 will range from 3 to 9.
The distributor 20 may further include a nozzle plate 50 disposed upstream of and in spaced relationship with the distributor body 24 forming a mixing chamber 52 within the interior volume 18 of the fluid distribution manifold 12 between the end plate 48 at the inlet end 34 of the distributor body 24 and the nozzle plate 50. In an embodiment, the nozzle plate 50 may be disposed at an inlet end of the fluid distribution manifold 12. In an embodiment, the nozzle plate 50 may comprise a fixed flow area orifice plate. In an embodiment, the nozzle plate 50 may comprise a convergent-divergent nozzle or a venturi nozzle. As the liquid and vapor phase mixture passing into the distribution manifold 12 traverses the nozzle plate 50, the velocity of the mixture increases which ensures that a uniform homogenous two-phase mixture exists within the mixing chamber 52 prior to entering the discrete fluid flow passages.
In the depicted embodiments, the fluid distribution manifold 12 has a circular cross section and the distributor body 24 has a generally D-shaped semi-cylindrical cross section. However, it is to be understood that the fluid distribution manifold 12 and the distributor body 24 may have a non-circular cross-section so long as the second surface 28 of the distributor body 24 conforms to the inner wall of the fluid distribution manifold 12. Although the distributor body 24 is depicted in
In the depicted embodiments, the longitudinally extending flow passages 38 extend along the interface of the distributor body 24 with the fluid distribution manifold 12. However, in another embodiment, the longitudinally extending flow passages 38 may be formed internally within the distributor body 24, for example during extrusion of the distributor body 24 or by a drilling operation subsequent to formation of the distributor body, rather than along the interface of the distributor body 24 with the fluid distribution manifold 12. In a further embodiment of the fluid flow distributor 20, the distributor body 24 and the fluid distribution manifold 12 may be formed as an integral body, for example as a single piece extrusion.
The fluid flow distributor 20 disclosed herein is particularly useful in distributing a two-phase fluid amongst the heat exchange tubes of a heat exchanger so as to minimize maldistribution of the liquid and vapor phases resulting in improved heat exchanger performance, In air conditioning/refrigeration units employing evaporator heat exchangers incorporating the fluid flow distributor as disclosed herein will likely result in improved unit performance, including improving the coefficient of performance, reducing power consumption, and allowing for smaller and lighter evaporators.
The terminology used herein is for the purpose of description, not limitation. Specific structural and functional details disclosed herein are not to be interpreted as limiting, but merely as basis for teaching one skilled in the art to employ the present invention. Those skilled in the art will also recognize the equivalents that may be substituted for elements described with reference to the exemplary embodiments disclosed herein without departing from the scope of the present invention.
While the present invention has been particularly shown and described with reference to the exemplary embodiments as illustrated in the drawing, it will be recognized by those skilled in the art that various modifications may be made without departing from the spirit and scope of the invention. Therefore, it is intended that the present disclosure not be limited to the particular embodiment(s) disclosed as, but that the disclosure will include all embodiments falling within the scope of the appended claims.
Filing Document | Filing Date | Country | Kind |
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PCT/US14/40995 | 6/5/2014 | WO | 00 |
Number | Date | Country | |
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61864756 | Aug 2013 | US |