This application is a “national phase” application and claims priority to International Patent Application PCT/CN2011/073845 filed on May 9, 2011, which, in turn, is based upon and claims priority to Chinese Patent Application 201010208091.X filed on Jun. 21, 2010 and entitled “Heat Exchanger,” which is hereby incorporated by reference in its entirety.
1. Field of Invention
The indention relates to, in general, a hear exchanger and, more particularly, a micro-channel heat exchanger.
2. Description of Related Art
When a micro-channel heat exchanger is used as an evaporator, a gaseous and liquid (two-phase) refrigerant enters into a plurality of flat tubes from an inlet header of the micro-channel heat exchanger, exchanges heat with the air in the environment, and then is discharged cot of the micro-channel heat exchanger from an outlet header. If the refrigerant is completely evaporated into a gaseous refrigerant after passing through the evaporator, a part of gaseous refrigerant may generally exist in a portion of each flat tube adjacent to the outlet of the flat tube such that the heat-exchange capability of the evaporator may not be given fully play to. In other words, the refrigerant has been completely evaporated into the gaseous refrigerant before flowing out of the flat tubes such that the gaseous refrigerant in a portion of each flat tube connected to the outlet header may not exchange heat with the air in the environment and, consequently, the heat-exchange capability of the evaporator may not be given fully play to. If the evaporated refrigerant is not completely evaporated into the gaseous refrigerant (that is, the evaporated refrigerant contains a part of liquid refrigerant), although the heat-exchange capability of the evaporator may be given fully play to, the compressor may suck the gaseous refrigerant containing the liquid refrigerant, which is disadvantageous for the compressor, and even the refrigerating system cannot run.
The invention seeks to solve at least one of the problems existing in the related art to at least some extent. Accordingly, an object of the invention is to provide a heat exchanger with good heat-exchange capability, and the gaseous refrigerant sucked by the compressor does not contain the liquid refrigerant. Another object of the invention is to provide a refrigeration system comprising the heat exchanger.
Embodiments of a first broad aspect of the invention overcome disadvantages in the related art in a heat exchanger comprising a first header, a second header spaced apart from the first header by a predetermined distance, a plurality of flat tubes each of which defines two ends connected to the first and second headers, respectively, to communicate the first and second headers, a plurality of fins interposed between adjacent flat tubes, and a flow member defining a fluid-flow passage and forming a partition-wall-type heat-exchanging unit with the second header.
Embodiments of a second broad aspect of the invention overcome disadvantages in the related art also in a refrigeration system comprising a compressor, a condenser, a throttle device, and an evaporator that is the heat exchanger. The compressor, condenser, throttle device, and evaporator are connected sequentially, and at least part of refrigerant flowing out of an outlet of the condenser enters into the flow member to exchange heat with a refrigerant flowing out of an outlet of the evaporator.
When the heat exchanger according to embodiments of the invention is used as an evaporator, the gaseous refrigerant flowing out of an outlet of the evaporator contains a part of liquid refrigerant and may exchange heat with the liquid refrigerant flowing out of an outlet of a condenser of a refrigeration system. On one hand, the under-cooling degree of the liquid refrigerator flowing out of the outlet of the condenser may be further increased. On the other hand, the liquid refrigerant contained in the gaseous refrigerant flowing out of the outlet of the evaporator and partly evaporated in the evaporator may be completely evaporated so that the heat-exchange capability of the heat exchanger is improved and no liquid refrigerant enters into the compressor. In addition, the ideal design of the evaporator is that the refrigerant flowing out of the flat tubes is completely gaseous refrigerant. However, this has high requirements for the design of the evaporator, and this may be hard to realize under different running conditions. However, with the heat exchanger according to embodiments of the invention, the evaporator is simple to design and high in applicability.
In one embodiment, the flow member includes a first partition plate disposed in the second header along an axial direction of the second header to divide an inner chamber of the second header into first, second, and third chambers, the first chamber is communicated with the plurality of flat tubes and isolated from the second and third chambers, and the second and third chambers are communicated with each other. The second and third chambers are communicated with each other at rear ends thereof, the second chamber is formed with an inlet in a front-end surface thereof, and the third chamber is formed with an outlet in a front-end surface thereof. The first partition plate is substantially T-shaped.
In another embodiment, the flow member includes a flow tube disposed in the second header along an axial direction of the second header and defining inlet and outlet ends that are extended out of the second header.
In one embodiment, the flow tube is disposed at a lower portion of an inner chamber of the second header, and the inlet and outlet ends of the flow tube are extended out from front and rear-end surfaces of the second header, respectively.
In another embodiment, the flow member includes further a second partition plate dividing an inner chamber of the second header into upper and lower chambers communicated with each other, the flow tube is disposed in the lower chamber, and the outlet end of the flow tube is extended into the first header. The upper and lower chambers are communicated with each other at rear ends thereof, the inlet end of the flow tube is extended out of the second header from a lower side of a front portion of the second header along a radial direction of the second header, and the outlet end of the flow tube is extended out of the second header from a rear-end surface of the lower chamber. A throttle mechanism is disposed in a portion of the flow tube extended between the first and second headers.
In still another embodiment, the flow tube has a circular cross-section.
In yet another embodiment, the flow tube is a micro-channel tube defining a plurality of micro-channels therein. The micro-channel tube has a circular arc cross-section. The flow member includes further inlet and outlet manifolds that are connected to two ends of the micro-channel tube, respectively, and inner chambers of inlet and outlet manifolds are communicated with the plurality of micro-channels of the micro-channel tube, respectively.
In still another embodiment, the micro-channel tube is U-shaped, and a plurality of corrugated sub-fins are interposed between two side walls of the U-shaped micro-channel tube.
In another embodiment, the flow member includes a plurality of capillary tubes.
In still another embodiment, the heat exchanger comprises further a third header communicated with an upper portion of an inner chamber of the second header, and a gas-outlet pipe is disposed and communicated with an inner chamber of the third header. The third header is communicated with the inner chamber of the second header via a plurality of first connection tubes.
In yet another embodiment, the flow member includes a flow tube, third and fourth partition plates are disposed in the flow tube and divide an inner chamber of the flow tube into fourth, fifth and sixth chambers, the fourth chamber is communicated with an inner chamber of the second header, and the fifth and sixth chambers are communicated with each other and isolated from the fourth chamber. The fifth and sixth chambers are communicated with each other at rear ends thereof, the fifth chamber is formed with an inlet in a front-end surface thereof, and the sixth chamber is formed with an outlet in a front-end surface thereof. The fourth chamber is communicated with the inner chamber of the second header via a plurality of second connection tubes connected between the flow tube and the second header.
In another embodiment, the heat exchanger comprises further a third header communicated with an upper portion of an inner chamber of the second header, a gas-outlet pipe is disposed and communicated with an inner chamber of the third header, and the flow member includes a flow tube disposed in the third header and defining inlet and outlet ends that are extended out of the third header. The inlet end of the flow tube is extended out from a front portion of the third header along a radial direction of the third header, and the outlet end of the flow tube is extended out from a rear-end surface of the third header. The outlet end of the flow tube is extended into the first header. A throttle mechanism is disposed in a portion of the flow tube extended between the first header and the third header.
In an alternative embodiment, each flat tube includes a bent segment and straight segments connected to first and second ends of the bent segment, respectively, the bent segment is twisted relative to the straight segments by a predetermined angle, and the fins are interposed between adjacent straight segments.
With the refrigeration system according to an embodiment of the invention, the gaseous refrigerant flowing out of an outlet of the evaporator contains a part of liquid refrigerant and may exchange heat with the liquid refrigerant flowing out of an outlet of the condenser of the refrigeration system. On one hand, the under-cooling degree of the liquid refrigerator flowing out of the outlet of the condenser may be further increased. On the other hand, the liquid refrigerant contained in the gaseous refrigerant flowing out of the outlet of the evaporator and partly evaporated in the evaporator may be completely evaporated so that the heat-exchange capability of the heat exchanger is improved and no liquid refrigerant enters into the compressor. As described above, the ideal design of the evaporator is that the refrigerant flowing out of the flat tubes is completely gaseous refrigerant. However, this has high requirements for the design of the evaporator, and this may be hard to realize under different running conditions. However, with the heat exchanger according to embodiments of the invention, the evaporator is simple to design and high in applicability.
Other objects, features, and advantages of the invention are readily appreciated as the same becomes better understood while the subsequent detailed description of embodiments of the invention is read taken in conjunction with the accompanying drawing thereof.
Reference is made in detail to embodiments of the invention. The embodiments described herein with reference to the drawing are explanatory and illustrative and used to generally understand the invention. The embodiments shall not be construed to limit the invention. The same or similar elements and the elements having the same or similar functions are denoted by like reference numerals throughout the description.
Unless specified or limited otherwise, relative terms such as “central,” “longitudinal,” “lateral,” “front,” “rear,” “right,” “left,” “inner,” “outer,” “lower,” “upper,” “horizontal,” “vertical,” “above,” “below,” “up,” “top,” and “bottom” as well as derivatives thereof (e.g., “horizontally,” “downwardly,” “upwardly,” etc.) should be construed to refer to the orientation as then described or as shown in the figure(s) under discussion. These relative terms are for convenience of description and do not require that the invention be constructed or operated in a particular orientation. In addition, the terms “outlet” and “outlet tube” have the same meaning, and the terms “inlet” and “inlet tube” have the same meaning. The terms “first refrigerant” and “second refrigerant” are used for distinguishing the source of the refrigerant and for convenience of description, but shall not be construed to limit the invention.
In the following description, the heat exchanger according to embodiments of the invention is described by taking the use of the heat exchanger as an evaporator (as an example), wherein a first header is used as the inlet header, a second header is used as the outlet header, a refrigerant evaporated in the evaporator is referred to as a “first refrigerant” (may also be referred to as a “cold refrigerant”), and a refrigerant in a flow member is referred to as a “second refrigerant” (may also be referred to as a “hot refrigerant”).
The heat exchanger according to embodiments of the first aspect of the invention is described below with reference to
Each flat tube 3 defines two ends connected to the first and second headers 1, 2, respectively, to communicate the first and second headers 1, 2 via micro-channels in each flat tube 3. The fins 4 are interposed between adjacent flat tubes 3, respectively. The flow member defines a fluid-flow passage therein and forms a partition-wall-type heat-exchanging unit (also referred as “surface heat-exchanging unit”) with the second header 2. The flow passage of the flow member is configured as a first fluid-flow passage (e.g., a hot-fluid-flow passage) of the partition-wall-type heat-exchanging unit, and an inner chamber of the second header 2 is configured as a second fluid-flow passage (e.g., a cold-fluid-flow passage) of the partition-wall-type heat-exchanging unit such that a second refrigerant in the flow member may exchange heat with a first refrigerant in the second header 2.
In one embodiment, each flat tube 3 is flat-plate-shaped such that a flat-plate type heat exchanger is formed.
In another embodiment, as shown in
When the heat exchanger according to embodiments of the invention is used as an evaporator, the gaseous refrigerant flowing out of the outlet of the evaporator contains a part of liquid refrigerator and may exchange heat with the refrigerant flowing out of the outlet of a condenser of a refrigeration system. On one hand, the under-cooling degree of the liquid refrigerator flowing out of the outlet of the condenser may be further increased. On the other hand, the liquid refrigerant contained in the gaseous refrigerant partly evaporated in the evaporator may be completely evaporated so that the heat-exchange capability of the heat exchanger is improved significantly and no liquid refrigerant enters into the compressor in addition, the evaporator is simple to design and high in applicability.
The heat exchanger having different types of flow members according to embodiments of the invention are described below in detail with reference to the drawing.
Embodiment 1
As shown in
As shown in
In one example, the second and third chambers 22, 23 are communicated with each other at rear ends (i.e., left ends in
As shown in
In some examples, the heat exchanger according to the first embodiment of the invention comprises further a third header 5. The third header 5 is communicated with an upper portion (e.g., the first chamber 21) of the inner chamber of the second header 2, and a gas-outlet pipe 51 is disposed on the third header 5 and communicated with an inner chamber of the third header 5. For example, the gas-outlet pipe 51 is disposed on a front-end surface of the third header 5. Alternatively, the third header 5 is communicated with the first chamber 21 of the second header 2 via a plurality of first connection tubes 6. After the first refrigerant in the first chamber 21 exchanges heat with the second refrigerant in the second and third chambers 22, 23, the liquid part of the first refrigerant may be evaporated into a gaseous refrigerant by heat exchange, and then the gaseous first refrigerant enters into the third header 5 through the first connection tubes 6, is discharged out of the third header 5 from the gas-outlet pipe 51, and then, for example, enters into a compressor.
When the heat exchanger according to the first embodiment of the invention is used as an evaporator, the gaseous and liquid (two-phase) first refrigerant enters into the first header 1 from the inlet tube 111 and then enters into the flat tubes 3 to exchange heat with the air in the environment and be evaporated into the gaseous and liquid first refrigerant containing a part of unevaporated liquid refrigerant, and the gaseous and liquid (two-phase) first refrigerant containing a part of unevaporated liquid refrigerant enters into the first chamber 21 of the second header 2. A part of the second refrigerator flowing out of an outlet of a condenser of a refrigeration system enters into the second chamber 22 of the second header 2 from the inlet 220 of the second chamber 22, flows toward the rear end of the second chamber 22, enters into the third chamber 23 from the rear end of the second chamber 22, and then flows out of the third chamber 23 from the outlet 230. When flowing in the second and third chambers 22, 23, the second refrigerant exchanges heat with the first refrigerant in the first chamber 21 such that the temperature of the first refrigerant in the first chamber 21 is increased and the liquid refrigerant in the first refrigerant is completely evaporated into a gaseous refrigerant. The gaseous first refrigerant enters into the third header 5 through the first connection tubes 6, is discharged out of the third header 5 from the gas-outlet pipe 51, and then, for example, is sucked into the compressor. The second refrigerant, after heat exchange, may return back to the inlet header 1 of the evaporator through an external throttle mechanism. Therefore, the liquid refrigerant contained in the first refrigerant may be completely evaporated, no liquid refrigerant enters into the compressor, and the heat-exchange capacity may be improved. Meanwhile, the under-cooling degree of the liquid refrigerant flowing out of the outlet of the condenser may be further increased, thus further improving the heat-exchange capacity of the heat exchanger significantly.
In addition, by dividing the second header 2 into the first, second, and third chambers 21, 22, 23 using the first partition plate 7, the second refrigerant in the second and third chambers 22, 23 mainly exchanges heat with the liquid refrigerant contained in the first refrigerant, thus further enhancing the “evaporation” effect of the liquid refrigerant contained in the first refrigerant.
Embodiment 2
As shown in
As shown in
In some examples, the heat exchanger according to the second embodiment of the invention comprises further a third header 5. The third header 5 is communicated with an upper portion of the inner chamber of the second header 2. A gas-outlet pipe 51 is disposed on the front-end surface of the third header 5. Alternatively, the third header 5 is communicated with the inner chamber of the second header 2 via a plurality of first connection tubes 6.
When the heat exchanger according to the second embodiment of the invention is used as an evaporator, for example, a second refrigerator flowing out of an outlet of a condenser of a refrigeration system flows into the flow tube 10 from the inlet end 101, flows toward the outlet end 102, and then flows out of the flow tube 10 from the outlet end 102. When flowing in the flow tube 10, the second refrigerant exchanges heat with the evaporated first refrigerant in the second header 2. The first refrigerant, after heat exchange, enters into the third header 5 from the second header 2, flows out of the third header 5 from the gas-outlet pipe 51, and then, for example, is sucked into a compressor. Therefore, the liquid refrigerant contained in the first refrigerant may be completely evaporated. Meanwhile, the under-cooling degree of the liquid refrigerant flowing out of the outlet end 102 of the flow tube 10 may be further increased, thus improving the heat-exchange capacity of the heat exchanger significantly. Moreover, the flow member has simple structure and is disposed in the second header 2, thus evaporating the liquid refrigerant contained in the first refrigerant more effectively.
Embodiment 3
The heat exchanger according to a third embodiment of the invention is formed by improving the heat exchanger according to the second embodiment of the invention. As shown in
The second partition plate 11 divides an inner chamber of the second header 2 into upper and lower chambers 24, 25 communicated with each other. In one example, the upper and lower chambers 24, 25 are communicated with each other at rear ends (i.e., left ends in
In another example, a throttle mechanism 12 is disposed in a portion of the flow tube 10 extended between the first and second headers 1, 2. Alternatively, the throttle mechanism 12 may be an expansion valve such that the second refrigerant that exchanges heat with the first refrigerant is throttled by the throttle mechanism 12 and then supplied to the first header 1 of the evaporator.
When the heat exchanger according to the third embodiment of the invention is used as an evaporator, the second refrigerator flowing out of an outlet of a condenser of a refrigeration system flows into the flow tube 10 from the inlet end 101, exchanges heat with the evaporated first refrigerant in the second header 2, flows out of the flow tube 10 from the outlet end 102, is throttled by the expansion valve 12, and then supplied to the first header 1. The evaporated first refrigerant, after heat exchange, flows out of the second header 2 from an outlet 211 of the second header 2 and then, for example, enters into the compressor.
In the second and third embodiments of the invention, as shown, in
Embodiment 4
As shown in
In one example, the flow member includes further inlet and outlet manifolds 13, 14 that are connected to two ends of the micro-channel tube, respectively, and inner chambers of inlet and outlet manifolds 13, 14 are communicated with the plurality of micro-channels 1001 of the micro-channel tube, respectively, as shown in
In one example, the heat exchanger comprises further a third header 5. The third header 5 is communicated with an upper portion of the inner chamber of the second header 2, and a gas-outlet pipe 51 is disposed on the third header 5 and communicated with an inner chamber of the third header 5. Alternatively, the third header 5 is communicated with the inner chamber of the second header 2 via a plurality of first connection tubes 6.
When the heat exchanger according to the fourth embodiment of the invention is used as an evaporator, the second refrigerator flowing out of an outlet of a condenser of a refrigeration system flows into the plurality of micro-channels 1001 of the micro-channel tube from the inlet manifold 13, exchanges heat with the evaporated first refrigerant in the second header 2, and then flows out of the plurality of micro-channels 1001 of the micro-channel tube from the outlet manifold 14. After exchanging heat with the second refrigerant, the first refrigerant enters into the third header 5 through the first connection tubes 6, is discharged out of the third header 5 from the gas-outlet pipe 51, and then, for example, is sucked into a compressor. Because the flow tube 10 is a micro-channel tube, the heat-exchange efficiency between the first refrigerant and the second refrigerant is, thus, enhanced.
Embodiment 5
The heat exchanger according to a fifth embodiment of the invention is an improvement of the heat exchanger according to the fourth embodiment of the invention. As shown in
As shown in
As shown in
When the heat exchanger according to the fifth embodiment of the invention is used as an evaporator, as shown in
Embodiment 6
As shown in
As shown in
When the heat exchanger according to the sixth embodiment of the invention is used as an evaporator, as shown in
Embodiment 7
As shown in
As shown in
When the heat exchanger according to the seventh embodiment of the invention is used as an evaporator, a second refrigerator flowing out of an outlet of a condenser of a refrigeration system flows into the fifth chamber 113 from the inlet 1131 of the fifth chamber 113, flows backwardly into the sixth chamber 114, and finally flows out of the sixth chamber 114 from the outlet 1141 of the sixth chamber 114. When flowing in the fifth and sixth chambers 113, 114, the second refrigerant exchanges heat with a first refrigerant that enters into the fourth chamber 112 from the second header 2 through the second connection tubes 18. The first refrigerant, after heat exchange, may be completely evaporated into a gaseous refrigerant to flow out of the second header 2 from the outlet tube 211 of the second header 2 and then, for example, to be sucked into a compressor.
Embodiment 8
As shown in
The flow member includes a flow tube 10, and the flow tube 10 is disposed in the third header 5 and defines inlet and outlet ends 101, 102 that are extended out of the third header 5. As shown in
As shown in
Embodiment 9
As shown in
In one example, a throttle mechanism 12, such as an expansion valve, is disposed in a portion of the flow tube 10 extended between the first header 1 and the third header 5 such that the first refrigerant may return back to the first header 1 after throttled by the expansion valve.
As shown in
The refrigeration system according to embodiments of a second aspect of the invention (for example, a refrigeration system in an air conditioner) is described below.
The refrigeration system according to embodiments of the second aspect of the invention comprises a compressor, a condenser, a throttle device, and an evaporator that are connected sequentially, wherein the evaporator is the heat exchanger according to embodiments descried above and at least part of refrigerant (i.e., the second refrigerant) flowing out of an outlet of the condenser enters info the flow member to exchange heat with the first refrigerant flowing out of an outlet of the evaporator. Because the operation and other members of the refrigeration system are known to those ordinarily skilled in the related art, a detailed description thereof is omitted here.
With the refrigeration system according to an embodiment of the invention, the first refrigerant flowing out of the outlet of the evaporator may exchange heat with the second refrigerant flowing out of the outlet of the condenser. On one hand, the under-cooling degree of the second refrigerator flowing out of the outlet of the condenser may be further increased. On the other hand, the liquid refrigerant in the first refrigerant in the evaporator may be completely evaporated in the evaporator so that no liquid refrigerant enters into the compressor and the heat-exchange capability of the heat exchanger is improved. Therefore, the entire efficiency of the refrigeration system may be enhanced.
Reference throughout this specification to “an embodiment,” “some embodiments,” “one embodiment,” “another example, ” “an example,” or “some examples” means that a particular feature, structure, material, or characteristic described in connection with the embodiment or example is included in at least one embodiment or example of the invention. Thus, appearance of phrases such as “in some embodiments,” “in one embodiment,” “in an embodiment,” “in another example,” “in an example,” or “in some examples” in various places herein are not necessarily referring to the same embodiment or example of the invention. Furthermore, the particular features, structures, materials, or characteristics may be combined in any suitable manner in one or more embodiments or examples.
The invention has been described above in an illustrative manner. It is to be understood that the terminology that has been used above is intended to be in the nature of words of description rather than of limitation. Many modifications and variations of the invention are possible in light of the above teachings. Therefore, within the scope of the appended claims, the invention may be practiced other than as specifically described above.
Number | Date | Country | Kind |
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2010 1 0208091 | Jun 2010 | CN | national |
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/CN2011/073845 | 5/9/2011 | WO | 00 | 7/10/2014 |
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WO2011/160501 | 12/29/2011 | WO | A |
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