Heat pump equipment

Abstract: Heat pump equipment (10) comprising at least three heat exchangers (16, 24, 28), one (24) of which is intended to be located in an enclosed region (44) and the other two (16, 28) of which are intended to be located outside the enclosed region (44). Each heat exchanger (16, 24, 28) has a delta connection end connected in heat-exchange fluid communication with a delta arrangement (20). The delta connection end of each heat exchanger (16, 24, 28) is connected to both of the delta connection ends of the other two heat exchangers via the delta arrangement (20). There are three fluid-expansion devices (32, 34, 36), one between the two connections of each pair of adjacent connections of the heat exchangers (16, 24, 28) to the delta arrangement (20). The present invention extends to heat pump equipment comprising at least three heat exchangers (214, 216, 218) connected in a heat-exchange fluid circuit, one (214) of which heat exchangers (214, 216, 218) is intended to be located in an enclosed region (228) and another of which is intended to be located outside the enclosed region (228). A third one (216) of the heat exchangers is arranged so that air which flows through an aperture (232) in a wall (230) which forms a boundary of the enclosed region (228) passes over the said third heat exchanger (216).

Description: The present invention relates to heat pump equipment. In previously proposed heat pump equipment, means have been provided to enable heat exchangers outside a building to be defrosted even while the equipment is being used to transfer heat from outside the building into its interior, in the form of more than one pressure drop and complex solenoid operated valve systems. This has made the equipment relatively expensive, and, because of its complexity, relatively difficult to diagnose any malfunction occurring within the equipment. Such equipment is disclosed in US-A-5 771 699. This has outside heat exchanger coils designed to change functions independently of one another from that of an evaporator to that of a condenser. This inhibits the accumulation of frost, and/or removes frost from an outside heat exchanger coil when the heat pump is operating in the heating mode without reversing the flow of refrigerant within, or impeding the flow of refrigerant to an inside heat exchanger coil. The present invention seeks to obviate this disadvantage. Accordingly, the present invention is directed to heat pump equipment comprising at least three heat exchangers, one of which is intended to be located in an enclosed region and the other two of which are intended to be located outside the enclosed region, in which the equipment further comprises a delta arrangement of expansion devices, and each heat exchanger has a delta connection end connected in heat-exchange fluid communication with the delta arrangement, such that the delta connection end of each heat exchanger is connected to both of the delta connection ends of the other two heat exchangers via the delta arrangement, in which arrangement there are three fluid-expansion devices, one between the two connections of each pair of adjacent connections of the heat exchangers to the delta arrangement. Such equipment has the advantage that heat-exchange fluid can be directed to flow from the two outside heat exchangers to the inside heat exchanger, or alternatively from the inside heat exchanger to the two outside heat exchangers, and for defrosting of either one of the outside heat exchangers, fluid can be directed to flow from both that one of the outside heat exchangers and the inside heat exchanger to the other outside heat exchanger via the delta arrangement. To achieve this, there is preferably one compressor connected to receive heat-exchange fluid from and to feed heat-exchange fluid to the heat exchangers via a valve arrangement. The valve arrangement may comprise a valve for each heat exchanger. Each valve may be a four-way valve. Equipment embodying the present invention may be easier to service than previously proposed equipment. Use of the gas phase to effect defrosting of the outside coils allows defrost rates to be unaffected by gravity especially defrost rates of each path of multiple path heat exchangers if these are used. This speeds defrosting by an even distribution of heat. The path length does not need to be reduced when one of the outside heat exchangers is defrosted. This increases the maximum performance in the event that a refrigerant with a glide is used. An example of heat pump equipment embodying the present invention is illustrated in Figure 1 of the accompanying drawings which shows, diagrammatically, a fluid circuit of the equipment. The heat-exchange equipment 10 shown in Figure 1 comprises a compressor 12 having its fluid output connected via a four-way valve 14 to a heat-exchange coil 16 at one end thereof, the other end of which is connected to an apex 18 of a delta arrangement 20. A second apex 22 of the delta arrangement 20 is connected to one end of a fluid exchange coil 24, the other end of which is connected to the input end of the compressor 15 via a further four-way valve 26. The output of the compressor 12 is also connected to one end of a heat-exchange coil 28 via a third four-way valve 30, and the other end of the heat-exchange coil 28 is connected to a third apex 31 of the delta arrangement 20. There is a first expansion device 32 between the apices 18 and 22 of the delta arrangement, a second expansion device 34 between the apices 22 and 31 of the delta arrangement 20, and a third expansion device 36 between the apices 18 and 31 of the delta arrangement 20. The heat-exchange coils 16, 24 and 28 are provided with respective fans 38, 40 and 42. These are arranged to direct air to flow over their respective coils. The heat-exchange coil 24 is located within an enclosed region 44, whilst the coils 16 and 28 are located outside of the enclosed region 44. A wall 46 of the region 44 creates an outside boundary between the enclosed region 44 and outside regions. With the arrangement connected in this way, the compressor 12 drives hot gases through the valves 14 and 30 into the exterior heat-exchange coils 16 and 28. As the hot gaseous heat-exchange fluid flow through the heat-exchange coils 16 and 28, it is cooled by the outside air, and this cooling is assisted by the operation of the fans 38 and 42 to result in condensation of the heat-exchange fluid in those coils. The liquid heat-exchange fluid from the heat-exchange coil 16 passes to the apex 18 of the delta arrangement 20 through the expansion device 32 to the apex 22 and from thence to one end of the heat-exchange coil 24. Likewise, the liquid heat-exchange fluid from the heat-exchange coil 28 flows from one end thereof to the apex 31 of the delta arrangement 20, through the expansion device 34 to the apex 22 and again onwards to the heat-exchange coil 24. Thus, it will be seen that liquid from the coils 16 and 28 meets at the apex 22. Because there is substantially no differential pressure across the expansion device 36 in this condition of the heat pump equipment, substantially no fluid flows between the apices 18 and 31 of the delta arrangement 20, so that in this particular condition of the heat pump equipment, it is as if there were no connection between those apices. At the heat-exchange coil 24, the liquid is warmed by the air within the enclosed region 44, and this exchange is assisted by the fan 40. It results in the cooling of the air in the enclosed region 44. After flowing through the heat-exchange coil 24, the heat-exchange fluid returns back to the compressor 12 via the four-way valve 26. The valves 14, 26 and 30 may be switched so that the output of the compressor 12 is now connected via the four-way valve 26 directly to the heat-exchange coil 24. The hot gaseous heat-exchange fluid is cooled in this coil 24 by the air within the enclosed region 44, which heat-exchange is assisted by the fan 40, so that the air in the enclosed region 44 is heated. The heat-exchange fluid continues from the coil 24 to the apex 22 of the delta arrangement 20 where it divides, some of it passing through the expansion device 32 and some of it passing through the expansion device 34. From these expansion devices, the fluid continues to the two outside heat-exchange coils 16 and 28 where the fluid is warmed and evaporated by the outside air, this heat-exchange being assisted by the fans 38 and 42 respectively. This effectively cools the outside area. Heat-exchange fluid from the coils 16 and 28 in this condition of the equipment then passes respectively to the four-way valves 14 and 30 and thence to the input of the compressor 12. Once again, in this condition of the equipment there is substantially no pressure differential across the apices 18 and 31 of the delta arrangement 20, so that no fluid flows between these apices and it is as if they were disconnected. Continued operation of the heat-exchange equipment in this second condition may ultimately result in the heat-exchange coils 16 and 28 becoming frosted up on their exteriors, resulting in reduced efficiency of the heat-exchange equipment. To remedy this, it is necessary for the coils to be warmed. Normally, this would prevent the heating effect of the heat pump equipment on the air of the enclosed region. However, with the delta arrangement described herein, it is possible to switch the valves 14, 26 and 30 so that the output of the compressor 12 is connected to deliver hot gaseous heat-exchange fluid to one of the outside coils, say, coil 16, as well as to the inside coil 24. The fan 38 associated with that coil 16 would then be switched off. As a result, the heat-exchange fluid gives out heat from both of these coils 24 and 16, although the fan 40 might be slowed in its rotational speed to take account of the fact that some of the heat from the fluid delivered by the compressor 12 is now passing out from the coil 16. Fluid from both the coils 24 and 16 reach the delta arrangement 20 at apices 22 and 18, respectively, and from thence pass through the expansion devices 34 and 36, respectively, before merging at the apex 31 of the delta arrangement 20. From here, the fluid flows through the coil 28 where it is heated and evaporated by the outside air. This heat-exchange is again assisted by the fan 42. The heat-exchange fluid continues on its course through the valve 30 and thence back to the compressor 12 on the input side thereof. In this third condition of the equipment, the pressure differential across the apices 18 and 22 is substantially zero so that substantially no fluid flows between those apices and it is as if they were disconnected and as if the expansion device 32 were absent. In a fourth switching condition of the heat pump equipment, the valves 14, 30 and 26 are arranged so that the compressor 12 feeds hot gaseous heat-exchange fluid from its output to the coils 24 and 28 via the valves 26 and 30, respectively. The fan 42 associated with the coil 28 would then switched off. The fluid continues to the delta arrangement 20 reaching it at apices 22 and 31 from where it flows through the expansion devices 32 and 36, respectively, and thence to merge at apex 18, from which it flows to the coil 16 via the four-way valve 14 back to the input of the compressor 12. In this condition of the heat pump equipment, the air of the enclosed region 44 is still heated, but the coil 28 is defrosted and the coil 16 is used to do all the heating of the heat-exchange fluid. It will be appreciated that one of the ports of each four-way valve is blocked off. In the event that the four-way valves are solenoid operated, the de-energised conditions are such that in the event that they are all de-energised, the compressor 12 is nonetheless connected to a viable circuit. Numerous variations and modifications to the equipment illustrated in Figure 1 will occur to the reader without taking the resulting construction outside the scope of the present invention. For example, whilst the delta arrangement 20 is illustrated as a triangular form, the delta is not to be taken as requiring the appearance of a triangle. It could be circular, or indeed it could have any other form provided it is topographically equivalent. The refrigerant may be provided with a glide. The expansion devices may comprise orifice or capillary devices or any other form of expansion device and may or may not be connected in parallel with respective bi-directional or one-way valves as appropriate. The heat exchangers may be multiple path or single path heat exchangers. In the event that the equipment illustrated in Figure 1 is for heating the air of the enclosed area only, for example, it is not necessary to provide the four-way valves. Whilst the enclosed region has been described with reference to Figure 1 as being filled with air, in other applications it might be filled with a different fluid, for example water.

Claims: Heat pump equipment (10) comprising at least three heat exchangers (16, 24, 28), one (24) of which is intended to be located in an enclosed region (44) and the other two (16, 28) of which are intended to be located outside the enclosed region (44), characterised in that the equipment (10) further comprises a delta arrangement (20) of expansion devices (32, 34, 36), and each heat exchanger (16, 24, 28) has a delta connection end connected in heat-exchange fluid communication with the delta arrangement (20), such that the delta connection end of each heat exchanger (16, 24, 28) is connected to the delta connection ends of the other two heat exchangers via the delta arrangement (20), in which arrangement there are three fluid-expansion devices (32, 34, 36), one in each arm of the delta arrangement between the two connections of each pair of adjacent connections of the heat exchangers (16, 24, 28) to the delta arrangement (20). Equipment according to claim 1, characterised in that there is one compressor (12) connected to receive heat-exchange fluid from and to feed heat-exchange fluid to the heat exchangers (16, 24, 28), and a valve arrangement (14, 26, 30) connected between the compressor (12) and the heat exchangers (16, 24, 28). Equipment according to claim 2, characterised in that the valve arrangement (14, 26, 30) comprises a valve (14, 26, 30) for each heat exchanger (16, 24, 28). Equipment according to claim 3, characterised in that each valve (14, 26,30) is a four-way valve.

Inventors: LOWES ALBERT ROBERT, LOWES, ALBERT ROBERT
Applicants: EATON WILLIAMS GROUP LTD, EATON-WILLIAMS GROUP LIMITED
Application year: 2001
Main classification: F25B13
IPC codes: F25B40, F25B13, F25B41