The present invention relates to a plate heat exchanger that traps sludge and a refrigeration cycle apparatus that traps sludge.
Sludge contained in refrigerant circulating through a refrigeration cycle apparatus may cause, for example, wear of pipes, clogging of an expansion device, and failure of a compressor. For example, a related-art refrigeration cycle apparatus includes a strainer including a fibrous filter located in a refrigerant cycle path, through which refrigerant circulates, to capture sludge (refer to Patent Literature 1, for example).
Patent Literature 1: Japanese Unexamined Patent Application Publication No. 2011-226729
Disadvantageously, such a configuration, in which the strainer is added to the refrigerant cycle path, of the related-art refrigeration cycle apparatus disclosed in Patent Literature 1 results in increased cost. Furthermore, the fibrous filter in the configuration described in Patent Literature 1 may be clogged with captured sludge, leading to obstruction to the circulation of the refrigerant.
The present invention has been made in view of the above-described disadvantages. The present invention aims to provide a plate heat exchanger and a refrigeration cycle apparatus that are capable of trapping sludge contained in refrigerant with a simple configuration to reduce or eliminate the likelihood of clogging of a refrigerant circuit.
A plate heat exchanger according to an embodiment of the present invention includes a plate stack including a plurality of heat transfer plates stacked with each other, each of the heat transfer plates including a heat medium inflow hole serving as an inlet for a heat medium, a heat medium outflow hole serving as an outlet for the heat medium, a refrigerant inflow hole serving as an inlet for refrigerant, and a refrigerant outflow portion located below the refrigerant inflow hole and serving as an outlet for the refrigerant, the heat transfer plates defining a plurality of heat medium passages, through each of which the heat medium flowing from the heat medium inflow hole flows, and a plurality of refrigerant passages, through each of which the refrigerant flowing from the refrigerant inflow hole flows downward, each of the heat medium passages and the refrigerant passages being defined between adjacent ones of the heat transfer plates such that the heat medium passage and the refrigerant passage are arranged alternately with one another; and a refrigerant outlet nozzle attached to the plate stack and projecting from the plate stack along a stacking direction of the heat transfer plates, the refrigerant outlet nozzle being configured to let therethrough the refrigerant, leaving the refrigerant outflow portion, out of the plate stack, the refrigerant outlet nozzle including a projection projecting upward from an inner surface of the refrigerant outlet nozzle.
A refrigeration cycle apparatus according to an embodiment of the present invention includes a refrigerant circuit, through which refrigerant circulates, including a compressor, the refrigerant passages of the above-described plate heat exchanger, an expansion device, and an evaporator connected in a loop by refrigerant pipes. The apparatus further includes a heat medium circuit, through which a heat medium circulates, including a pump, the heat medium passages of the plate heat exchanger, and a load side heat exchanger connected in a loop by heat medium pipes. The plate heat exchanger functions as a condenser that condenses the refrigerant.
According to the embodiments of the present invention, the projection on the inner surface of the refrigerant outlet nozzle inhibits flow of sludge out of the plate heat exchanger. According to the embodiments of the present invention, therefore, sludge contained in the refrigerant can be trapped with a simple configuration, and the likelihood of clogging of the refrigerant circuit can be reduced or eliminated.
Embodiments of the present invention will be described below with reference to the drawings. In the drawings, the same components or equivalents are designated by the same reference signs, and a description thereof is omitted or simplified as appropriate. Furthermore, for example, the shapes, sizes, and arrangement of components illustrated in each drawing can be appropriately changed within the scope of the present invention.
The refrigerant circuit 10, through which refrigerant is circulated, includes a compressor 1, refrigerant passages 206 of a plate heat exchanger 2, an expansion device 3, and a heat source side heat exchanger 4, which are connected in a loop by refrigerant pipes. The refrigerant used in Embodiment 1 contains, as at least one component, a substance having a double bond in its molecule, such as HFO-1123, HFO-1234yf, or HFO-1234ze. Refrigerant containing no substance having a double bond may be used.
The compressor 1 compresses the refrigerant and is, for example, an inverter compressor that is capable of changing its operation frequency to any value to change a rate at which the refrigerant is sent per unit time. The plate heat exchanger 2 includes the refrigerant passages 206 through which the refrigerant flows and heat medium passages 209 through which the heat medium flows and allows the refrigerant flowing through the refrigerant passages 206 to exchange heat with the heat medium flowing through the heat medium passages 209. The expansion device 3 expands the refrigerant passing through the expansion device 3. For example, the expansion device 3 includes an expansion valve whose opening degree can be adjusted or a capillary tube having a simple configuration in which the opening degree cannot be adjusted. The heat source side heat exchanger 4 allows, for example, the refrigerant flowing through the heat source side heat exchanger 4 to exchange heat with air. For example, a fan (not illustrated) that sends the air to the heat source side heat exchanger 4 is disposed close to the heat source side heat exchanger 4.
An exemplary operation of the refrigerant circuit 10 will now be described. High-temperature, high-pressure refrigerant compressed through the compressor 1 flows into the refrigerant passages 206 of the plate heat exchanger 2. The refrigerant that has flowed into the refrigerant passages 206 exchanges heat with the heat medium flowing through the heat medium passages 209, so that the refrigerant condenses. Specifically, the plate heat exchanger 2 in Embodiment 1 functions as a condenser that condenses the refrigerant. The refrigerant that has flowed through the refrigerant passages 206 and condensed is expanded by the expansion device 3. The refrigerant expanded by the expansion device 3 is subjected to heat exchange in the heat source side heat exchanger 4, so that the refrigerant evaporates. The refrigerant evaporated in the heat source side heat exchanger 4 is sucked into the compressor 1, where the refrigerant is again compressed.
The heat medium circuit 11, through which the heat medium, such as water or brine, is circulated, includes a pump 12, the heat medium passages 209 of the plate heat exchanger 2, and a load side heat exchanger 13, which are connected in a loop by heat medium pipes. The pump 12 circulates the heat medium through the heat medium circuit 11. The load side heat exchanger 13 allows, for example, the heat medium flowing through the load side heat exchanger 13 to exchange heat with air. For example, a fan (not illustrated) that sends the air to the load side heat exchanger 13 is disposed close to the load side heat exchanger 13.
An exemplary operation of the heat medium circuit 11 will now be described. The operation of the pump 12 causes the heat medium to be circulated through the heat medium circuit 11. The heat medium flowing through the heat medium passages 209 of the plate heat exchanger 2 exchanges heat with the refrigerant flowing through the refrigerant passages 206, so that the heat medium is heated. The heat medium that has flowed through the heat medium passages 209 and has been heated flows to the load side heat exchanger 13. The heat medium transfers heat to the air while flowing through the load side heat exchanger 13. Then, the heat medium flows through the heat medium passages 209 of the plate heat exchanger 2, so that the heat medium is again heated.
The plate stack 20 includes a front side plate 202, a rear side plate 203, heat transfer plates 220, and heat transfer plates 230 such that the heat transfer plates 220 and 230 are alternately stacked between the side plates 202 and 203. The side plate 202, the side plate 203, the heat transfer plates 220, and the heat transfer plates 230 are plate-shaped metals having, for example, a rectangular shape. The side plate 202, the side plate 203, the heat transfer plates 220, and the heat transfer plates 230 are joined at contacts by, for example, brazing. The side plate 202, the side plate 203, the heat transfer plates 220, and the heat transfer plates 230 are stacked, positioned, and brazed such that outer ends of the plates overlap as illustrated in
Referring to
The heat transfer plates 220 and the heat transfer plates 230 are made by using, for example, different dies, and have different surface geometries. For the surface geometries of the heat transfer plates 220 and the heat transfer plates 230, for example, the heat transfer plates have a corrugated surface having corrugation depths varying in a stacking direction H in which the heat transfer plates 220 and 230 are stacked. The surface geometries cause the refrigerant flowing through the refrigerant passages 206 and the heat medium flowing through the heat medium passages 209 to flow in a complex manner, thus promoting heat exchange between the refrigerant and the heat medium.
Referring to
As illustrated in
The refrigerant outflow portions 242 are aligned to form a passage that allows an outflow of the refrigerant. The refrigerant outflow portions 242 are arranged so as to be aligned with the refrigerant outlet nozzle 205. As illustrated in
Referring to
The bottom portion 260 is located below the lower part of the inner surface of the refrigerant outlet nozzle 205. The partitions 212 project above the lower part of the refrigerant outlet nozzle 205. The partitions 212 each have an upper end that defines part of the refrigerant outflow hole 242A. The refrigerant outflow hole 242A is located above the bottom portion 260. The partitions 212, the side plates 202 and 203, and the bottom portion 260 define spaces 211 such that adjacent ones of the partitions 212 define a space 211, the partition 212 and the side plate 202 define a space 211, and the partition 212 and the side plate 203 define a space 211.
The refrigerant outlet nozzle 205 includes a projection 215 projecting upward from its inner surface. For example, the projection 215 is formed of a separate from the refrigerant outlet nozzle 205. The projection 215 is fixed to the inner surface of the refrigerant outlet nozzle 205 by brazing, for example. The projection 215 can be formed integrally with the refrigerant outlet nozzle 205 by, for example, cutting the inner surface of the refrigerant outlet nozzle 205.
As described above, the plate heat exchanger 2 in the example of Embodiment 1 includes the plate stack 20 including the heat transfer plates 220 and 230 stacked. The heat transfer plates 220 and 230 define the refrigerant passages 206 and the heat medium passages 209 arranged alternately with one another such that each of the refrigerant passages 206 and the heat medium passages 209 is defined between the adjacent heat transfer plates 220 and 230. The refrigerant flowing downward through the refrigerant passages 206 in a gravity direction G exchanges heat with the heat medium flowing through the heat medium passages 209, so that the refrigerant condenses. The heat transfer plates 220 and 230 each have the refrigerant outflow hole 242A that allows the refrigerant to flow out of the refrigerant passage 206. The refrigerant that has flowed downward through the refrigerant passages 206 in the gravity direction G and condensed is redirected in the stacking direction H and flows substantially horizontally. The refrigerant flowing in the stacking direction H flows substantially horizontally through the refrigerant outflow passage 210, formed by aligning the refrigerant outflow holes 242A, and then flows out of the plate stack 20 through the refrigerant outlet nozzle 205. In the plate heat exchanger 2 in the example of Embodiment 1, the bottom portion 260 defining the bottoms of the refrigerant passages 206 is located below the lower parts of the refrigerant outflow holes 242A and the lower part of the inner surface of the refrigerant outlet nozzle 205. The spaces 211 are arranged below the refrigerant outflow holes 242A and the refrigerant outlet nozzle 205. In the plate heat exchanger 2 in the example of Embodiment 1, therefore, sludge can be efficiently trapped in the spaces 211. The reason is as follows. When the direction of flow of the refrigerant containing sludge is changed from the downward direction to the horizontal direction, the sludge is more likely to travel downward than the refrigerant because the sludge has greater mass than the refrigerant. Furthermore, the sludge sinks downward under the influence of gravity while the refrigerant containing the sludge is flowing substantially horizontally through the refrigerant outflow passage 210. In other words, the plate heat exchanger 2 in the example of Embodiment 1 uses inertial force and the gravity to efficiently trap the sludge in the spaces 211.
In addition, since the plate heat exchanger 2 in the example of Embodiment 1 includes the projection 215 projecting upward from the inner surface of the refrigerant outlet nozzle 205, this arrangement inhibits flow of the sludge out of the plate heat exchanger 2. In Embodiment 1, the projection 215 can be omitted.
Additionally, since the sludge is separated from the condensed liquid refrigerant and is trapped in the plate heat exchanger 2 in the example of Embodiment 1, the sludge can be efficiently trapped. The reason is that the liquid refrigerant flows at a lower velocity than gaseous refrigerant. Furthermore, the refrigerant flows in the plate heat exchanger 2 at a lower velocity than in another typical heat exchanger, such as a cross-fin type heat exchanger. Allowing the plate heat exchanger 2 to have a configuration for trapping sludge can efficiently trap the sludge.
In addition, the plate heat exchanger 2 in the example of Embodiment 1 is configured such that the refrigerant flows downward as a downward flow through the refrigerant passages 206 and the heat medium flows upward as an upward flow through the heat medium passages 209. Such a configuration increases the efficiency of heat exchange. Furthermore, this configuration ensures liquefaction of the refrigerant flowing out of the refrigerant passages 206. Consequently, the sludge can be trapped with certainty.
In the plate heat exchanger 2 in the example of Embodiment 1, the lower part of each refrigerant outflow hole 242A is positioned above the lower part of the inner surface of the refrigerant outlet nozzle 205. Therefore, the partitions 212 project above the lower part of the refrigerant outlet nozzle 205. The plate heat exchanger 2 in the example of Embodiment 1 is configured such that the sludge can be trapped between the partitions 212. Such a configuration reduces or eliminates the likelihood that the flow of the refrigerant may raise the sludge trapped in the spaces 211. Therefore, the plate heat exchanger 2 in Embodiment 1 inhibits the flow of the sludge out of the plate heat exchanger 2.
In the example of Embodiment 1, the spaces 211 for trapping sludge are arranged below the refrigerant outflow passage 210 and the refrigerant outlet nozzle 205. If sludge accumulates in the spaces 211, the refrigerant can flow through the refrigerant outflow passage 210 located above the spaces 211. This arrangement does not hinder the refrigerant from flowing.
If the refrigerant used in Embodiment 1 contains a substance having a double bond in its molecular structure, the above-described advantages will become more apparent. Specifically, a substance having a double bond may form a solid polymer. The circulation of refrigerant containing a solid polymer through the refrigerant circuit 10 may, for example, accelerate wear of the pipes, cause clogging of the expansion device 3, and accelerate wear of sliding parts of the compressor 1. According to Embodiment 1, if a solid polymer is formed, the solid polymer can be trapped in the spaces 211. This reduces or eliminates the likelihood that a formed solid polymer may cause failure of the refrigerant circuit 10.
The refrigeration cycle apparatus 100 in the example of Embodiment 1 is configured such that a polymer is trapped in the plate heat exchanger 2 that condenses high-temperature, high-pressure refrigerant discharged from the compressor 1. Such a configuration further reduces or eliminates the likelihood that a formed solid polymer may cause failure of the refrigerant circuit 10. The reason is as follows. A substance having a double bond tends to form a polymer, particularly under high-temperature and high-pressure conditions. In the example of Embodiment 1, a polymer can be trapped in the plate heat exchanger 2 that condenses high-temperature, high-pressure refrigerant discharged from the compressor 1. In other words, a polymer can be trapped immediately after the formation of the polymer in Embodiment 1, leading to enhanced reliability of the refrigeration cycle apparatus 100.
Embodiment 1 is not limited to the above-described example. Embodiment 1 includes the following modification. In the following description of the modification, a description of the previously described details is omitted.
As illustrated in
Embodiment 2 is not limited to the above-described example. For example, Embodiment 2 includes the following modifications. In the following description of the modifications, a description of the previously described details is omitted.
The present invention is not limited to Embodiments 1 and 2 described above and can be variously modified within the scope of the invention. Specifically, the configurations according to Embodiments 1 and 2 described above may be appropriately modified and an equivalent may be substituted for at least one element thereof. Furthermore, a component whose location is not particularly limited does not necessarily have to be disposed at the location described in Embodiment 1 or 2, and may be disposed at any location that enables the component to achieve its function.
For example, the heat transfer plates 220 and 230 each have the refrigerant outflow hole 242A in Embodiment 1 described with reference to
Furthermore, the design according to Modification 3 may be applied to the configuration of the plate heat exchanger 2 according to Embodiment 1 described with reference to
The example in which the plate heat exchanger functions as a condenser has been described. If the refrigerant circuit includes a flow switching device, such as a four-way valve, the direction of flow of the refrigerant can be changed to cause the plate heat exchanger to function as an evaporator. In the case where the plate heat exchanger is caused to function as an evaporator, for example, the refrigerant may be circulated through the compressor, the heat source side heat exchanger, the expansion device, and the refrigerant passages of the plate heat exchanger in that order.
This application is a U.S. national stage application of International Application No. PCT/JP2015/084854, filed on Dec. 11, 2015, the contents of which are incorporated herein by reference.
Filing Document | Filing Date | Country | Kind |
---|---|---|---|
PCT/JP2015/084854 | 12/11/2015 | WO | 00 |