The present invention relates to cooling systems, and more specifically, to vapor-compression cooling systems.
Vapor compression cooling systems generally include a compressor, a condenser, an expansion device, and an evaporator, with a cooling fluid, such as a refrigerant, circulating between these components. The circulating refrigerant enters the compressor as a vapor and is compressed to a higher pressure, superheated vapor. The superheated vapor refrigerant is routed through the condenser. In the condenser, the refrigerant is cooled and condensed into a saturated liquid state. The liquid refrigerant is then routed to the expansion device. In the expansion device, pressure of the refrigerant is rapidly lowered, causing a portion of the refrigerant to evaporate. The refrigerant enters the evaporator as a liquid-vapor mixture, and evaporation continues through the evaporator, resulting in the cooling of fluids, such as circulating air, passing over the evaporator.
In order to increase the efficiency of a vapor-compression cooling system, it is desirable to maximize the quality of the liquid refrigerant entering the expansion device.
In one embodiment, the invention provides a heat exchanger assembly. The heat exchanger assembly includes a plurality of tubes, each having an inlet end and an outlet end. An inlet header is configured to receive a cooling fluid and to distribute the cooling fluid to the inlet ends of the plurality of tubes. An outlet header includes an outer shell and defines an outlet chamber. The outlet chamber is configured to receive cooling fluid discharged from the outlet ends of the plurality of tube. A supply conduit supplies the cooling fluid to the inlet header. The supply conduit includes a conduit portion extending through the outlet header.
In another embodiment, the invention provides a method of operating a heat exchanger assembly. A plurality of tubes are provided, each having an inlet end and an outlet end. A cooling fluid is supplied to the inlet ends through an inlet header. The cooling fluid is passed through each of the plurality of tubes from the inlet end to the outlet end. The cooling fluid is received from the outlet ends in an outlet header. A conduit portion of a supply conduit is routed through the outlet header. The supply conduit supplies cooling fluid to the inlet header after passing through the conduit portion.
In yet another embodiment, the invention provides a heat exchanger assembly. A plurality of tubes each extend from an inlet end to an outlet end. An inlet header is configured to receive a refrigerant and to distribute the refrigerant to the inlet ends of the plurality of tubes. A liquid to suction heat exchanger includes a suction header receiving vapor refrigerant discharged from the outlet ends of the plurality of tubes, and a liquid conduit fluidly connected to the inlet header upstream of the inlet header. The liquid conduit is thermally coupled to the suction header for heat transfer between liquid refrigerant in the liquid conduit and the vapor refrigerant in the suction header.
Other aspects of the invention will become apparent by consideration of the detailed description and accompanying drawings.
Before any embodiments of the invention are explained in detail, it is to be understood that the invention is not limited in its application to the details of construction and the arrangement of components set forth in the following description or illustrated in the following drawings. The invention is capable of other embodiments and of being practiced or of being carried out in various ways.
Referring to
The heat exchanger 18 also includes an inlet header 38 and an outlet header 42. Referring to
The inlet header 38 includes a cylindrical tube 46 having a first end 50 and a second end 54. The first end 50 is configured to receive a refrigerant. The inlet header 38 distributes the refrigerant to the inlet end 26 of the heat exchanger 18.
As shown in
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As illustrated in
The cooling assembly 10 of
Referring to 1, the condenser end 86 of the supply conduit 82 receives the liquid refrigerant from the condenser 134. The liquid refrigerant passes through the conduit portion 102 (
The liquid-vapor mixture is further routed in the supply conduit 82 from the thermal expansion valve 94 to the first end 50 of the inlet header 38. Within the inlet header 38, the liquid-vapor mixture is distributed to the inlet end 26 of the micro-channel tubes 22. The liquid-vapor mixture is routed from the first end 50 of the inlet header 38 through the plurality of micro-channel tubes 22 where it evaporates into a vapor.
The vapor refrigerant is discharged from the outlet 30 end of the micro-channel tubes 22 into the outlet chamber 126 of the outlet header 42. The vapor contained within the outlet header 42 is discharged through the outlet port 78 of the outer shell 58 to the compressor 130 (
Referring to
The outer shell 170 surrounds an outlet chamber tube 186. The outlet chamber tube 186 has an outer surface 190 and an inner surface 194. As shown in
An annular space between the inner surface 174 of the outer shell 174 and the outer surface 190 of the outlet chamber 186 defines a cooler portion 210 of a supply conduit 218. Referring to
Liquid refrigerant entering the annular cooler portion 210 is subcooled. by vapor contained within the outlet chamber 198. Vapor exits the outlet chamber 198 via a vapor outlet tube 230.
The cooling assembly 234 includes a dual pass heat exchanger 238. The heat exchanger 238 includes first pass tubes 242 and second pass tubes 246. The first pass tubes 242 have an inlet end 250 and an outlet end 254. The second pass tubes 246 have an inlet end 258 and outlet end 262 disposed, respectively, substantially laterally offset from the inlet end 250 and outlet end 254 of the first pass tubes 242.
The heat exchanger 238 also includes a combination header 266 and an intermediate header 270. The combination header 266 includes an inlet header portion 274 (also referred to as an inlet header 274) and an outlet header portion 278 (also referred to as an outlet header 278). The inlet header portion 274 and outlet header portion 278 are separated by a bulkhead or baffle 282. The first pass tubes 242 receive refrigerant from the inlet header portion 274 at the inlet end 250 and discharge refrigerant to the intermediate header 270 at the outlet end 254. The intermediate header 270 then redirects the refrigerant in a lateral direction to the inlet end 258 of the second pass tubes 246. Refrigerant passes through the second pass tubes 246 in a direction substantially opposite the direction of the first pass tubes 242, and is discharged to the outlet header portion 278.
A supply conduit 286 includes a conduit portion 290 extending through the outlet header portion 278. Liquid refrigerant passing through the conduit portion 290 is subcooled by vapor refrigerant contained within the outlet header portion 278, into a subcooled liquid refrigerant. The subcooled liquid refrigerant is then routed through the supply conduit 286 to a thermal expansion valve 294. Within the expansion valve 294, pressure of the refrigerant is rapidly lowered, such that the refrigerant forms a liquid vapor mixture. The liquid-vapor mixture is further routed in the supply conduit 286 from the thermal expansion valve 294 to the inlet header portion 274.
Thus, the invention provides, among other things, a cooling assembly. Various features and advantages of the invention are set forth in the following claims.