CN212481758U - Take trigeminy of heat recovery to supply heat pump set - Google Patents
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Abstract
The utility model discloses a triple co-generation heat pump unit with heat recovery, which comprises a triple co-generation component and a hot water component, wherein the triple co-generation component comprises a first compressor, a first four-way valve, a heat recovery heat exchanger, a first one-way valve, a second four-way valve, an air conditioner heat exchanger, a first liquid storage device and a fin heat exchanger; the hot water assembly comprises a second compressor, a third four-way valve and a second liquid storage device. The beneficial effects of the utility model are that, this trigeminy supplies heat pump set area is little, simple to operate, has air conditioner refrigeration, air conditioner heat, refrigeration and hot water, heat and hot water, single hot water, change modes such as frost, can effectual solution winter heat and hot water demand, compromise winter's quick frost problem simultaneously, also can be satisfying the energy-conserving effect of furthest's improvement under the hot water demand in transition season simultaneously.
Description
Technical Field
The utility model relates to an air source heat pump system technical field, especially a take trigeminy of heat recovery to supply heat pump set.
Background
The traditional air source heating heat pump can only singly meet the requirements of air conditioners or heating of buildings and can not meet the requirements of domestic hot water at the same time. The commonly adopted method is a comprehensive solution of a heat pump and a water heater, but the solution needs two kinds of equipment, the initial investment is large, the occupied area of the equipment is large, and the space of a household balcony or a roof is limited, so that the normal installation and use of the equipment are difficult to meet.
The triple supply system disclosed in the chinese patent "a triple supply air source heat pump system" (application number 201621200404.6) can realize the full recovery of condensation heat, and has the functional requirements of heating, refrigerating and domestic hot water at the same time. However, the triple co-generation has technical defects, when the air conditioner heating and the domestic hot water are required at the same time, and the heating and the domestic hot water are used under full load, the domestic hot water capacity requirement is high due to the fact that the domestic hot water inlet temperature is gradually reduced, the heat recovery cannot meet the hot water requirement, and the overheated refrigerant can gradually perform phase change heat exchange, so that the heating capacity of the air conditioner is possibly insufficient. In addition, when heating is needed in winter, the evaporator of the domestic hot water heating system needs to have a quick defrosting effect to ensure that the heating capacity is not excessively lost, when the domestic hot water is needed, the defrosting capacity of the domestic hot water heating system is reduced due to the heat recovery process of the domestic hot water heating system, the domestic hot water heating system cannot be defrosted cleanly in the shortest time, and finally the equipment heating capacity of the domestic hot water heating system is influenced.
At present, a triple co-generation system in the market generally takes indoor air regulation as a main part and takes a domestic hot water function as an auxiliary part. The equipment is selected and matched by indoor air conditioning, the hot water load is small, and the energy efficiency is low when the air conditioner is used for heating and hot water overload. In a transition season, when the refrigeration demand is low, most of the working capacity of the air conditioner cannot be fully utilized, so that the phenomenon of large carriage pulling is caused, and finally the operation cost of the air conditioner is not much different from that of a combined scheme of an air conditioning and air source heating heat pump water heater. In addition, the required temperature of the domestic hot water is higher, and the domestic hot water runs under the refrigeration and heating functions, so that the condensation temperature of the equipment is correspondingly increased, the compression ratio is increased, and the final running life of the equipment is not facilitated.
SUMMERY OF THE UTILITY MODEL
The to-be-solved technical problem of the utility model is to above-mentioned prior art not enough, a take trigeminy of heat recovery to supply heat pump set is provided.
In order to solve the technical problem, the utility model discloses the technical scheme who takes is: a triple co-generation heat pump unit with heat recovery comprises a triple co-generation assembly and a hot water assembly, wherein the triple co-generation assembly comprises a first compressor, a first four-way valve, a heat recovery heat exchanger, a first one-way valve, a second four-way valve, an air conditioner heat exchanger, a first liquid storage device and a fin heat exchanger; the hot water assembly comprises a second compressor, a third four-way valve and a second liquid storage device; the first four-way valve, the second four-way valve and the third four-way valve are all provided with an inlet, an outlet A, an outlet B and an outlet C; the heat recovery heat exchanger and the fin heat exchanger are both provided with 2 heat exchange pipelines;
the outlet end of the first compressor is connected with the inlet of the first four-way valve, the outlet C of the first four-way valve is connected with the inlet of the second four-way valve through the 1 st heat exchange pipeline and the second one-way valve of the heat recovery heat exchanger, the outlet A of the first four-way valve is connected with the inlet of the second four-way valve through the first one-way valve, and the outlet B of the first four-way valve is connected with the inlet end of the first compressor;
the outlet C of the second four-way valve is connected to one end of a first liquid storage device through an air conditioner heat exchanger, the other end of the first liquid storage device is connected to the outlet A of the second four-way valve through the 1 st heat exchange pipeline of the fin heat exchanger, and the outlet B of the second four-way valve is connected with the inlet end of the first compressor;
the outlet end of the second compressor is connected with the inlet of the third four-way valve, the outlet A of the third four-way valve is connected to one end of the second liquid storage device through the 2 nd heat exchange pipeline of the heat recovery heat exchanger, the other end of the second liquid storage device is connected to the outlet C of the third four-way valve through the 2 nd heat exchange pipeline of the finned heat exchanger, and the outlet B of the third four-way valve is connected with the inlet end of the second compressor.
In the above technical scheme, the triple co-generation assembly further includes a throttling device, the throttling device includes a first electronic expansion valve, a capillary tube and a third one-way valve, the first electronic expansion valve is connected between the fin heat exchanger and the first reservoir, the capillary tube is connected in series with the third one-way valve, the first electronic expansion valve is connected in parallel with the capillary tube and the third one-way valve which are connected in series, and the third one-way valve is in one-way conduction with the first reservoir.
Among the above-mentioned technical scheme, hot water component still includes second electronic expansion valve, and second electronic expansion valve connects between fin heat exchanger and second reservoir.
In the above technical scheme, the triple co-generation assembly further comprises a first gas-liquid separator, one end of the first gas-liquid separator is connected with the inlet end of the first compressor, and the other end of the first gas-liquid separator is connected with the outlet B of the first four-way valve and the outlet B of the second four-way valve.
In the above technical scheme, the hot water assembly further comprises a second gas-liquid separator, one end of the second gas-liquid separator is connected with the inlet end of the second compressor, and the other end of the second gas-liquid separator is connected with the outlet B of the third four-way valve.
In the above technical scheme, the first compressor is an inverter compressor.
In the above technical scheme, the heat recovery heat exchanger is a high-efficiency tank heat exchanger or a double-pipe heat exchanger.
The triple heat supply pump unit with heat recovery has an air conditioner refrigeration mode, an air conditioner heating mode, a refrigeration and hot water mode, a heating and hot water mode, a single hot water mode and a defrosting mode;
and (3) an air conditioner refrigeration mode: the method comprises the following steps that a first compressor is started, the inlet of a first four-way valve is communicated with the outlet A of the first four-way valve, the inlet of a second four-way valve is communicated with the outlet A of the second four-way valve, the outlet B of the second four-way valve is communicated with the outlet C of the second four-way valve, a high-temperature high-pressure refrigerant output by the first compressor is subjected to heat exchange through a fin heat exchanger and is condensed into a low-temperature low-pressure refrigerant, the low-temperature low-pressure refrigerant is subjected to heat exchange in an air conditioner heat exchanger to;
air conditioner heating mode: the method comprises the following steps that a first compressor is started, the inlet of a first four-way valve is communicated with the outlet A of the first four-way valve, the inlet of a second four-way valve is communicated with the outlet C of the second four-way valve, the outlet A of the second four-way valve is communicated with the outlet B of the second four-way valve, a high-temperature and high-pressure refrigerant output by the first compressor flows through an air-conditioning heat exchanger to prepare air-conditioning hot water, and the refrigerant returns to the first compressor through a first liquid storage device and a fin heat;
heating and hot water mode: the method comprises the following steps that a first compressor is started, the inlet of a first four-way valve is communicated with the outlet C of the first four-way valve, the inlet of a second four-way valve is communicated with the outlet C of the second four-way valve, the outlet A of the second four-way valve is communicated with the outlet B of the second four-way valve, a high-temperature and high-pressure refrigerant output by the first compressor flows through a heat recovery heat exchanger to prepare hot water, the refrigerant is condensed and subcooled through an air conditioner heat exchanger, and finally the refrigerant exchanges heat through a fin heat exchanger to absorb air source heat energy;
cooling and hot water modes: the method comprises the following steps that a first compressor is started, the inlet of a first four-way valve is communicated with the outlet C of the first four-way valve, the inlet of a second four-way valve is communicated with the outlet A of the second four-way valve, the outlet B of the second four-way valve is communicated with the outlet C of the second four-way valve, a high-temperature and high-pressure refrigerant output by the first compressor flows through a heat recovery heat exchanger to prepare hot water, the refrigerant is condensed and subcooled through a fin heat exchanger, the refrigerant is subjected to heat exchange through an air conditioner heat exchanger to prepare air conditioner cold water, and;
single hot water mode: the second compressor is started, the inlet of the third four-way valve is communicated with the outlet A of the third four-way valve, the outlet B of the third four-way valve is communicated with the outlet C of the third four-way valve, the high-temperature and high-pressure refrigerant output by the second compressor is used for preparing hot water through the heat recovery heat exchanger, and the refrigerant returns to the second compressor through the second liquid storage device and the fin heat exchanger to form a loop;
defrosting mode: the first compressor starts, the inlet of the first four-way valve is communicated with the A outlet of the first four-way valve, the inlet of the second four-way valve is communicated with the A outlet of the second four-way valve, the B outlet of the second four-way valve is communicated with the C outlet of the second four-way valve, a high-temperature and high-pressure refrigerant output by the first compressor directly flows to the frosted fin heat exchanger for heat exchange and defrosting, then returns to the first compressor through the first liquid storage device and the air conditioner heat exchanger to form a loop, and the air conditioner heat exchanger and the heat recovery heat exchanger are not started.
Preferably, the heating and hot water mode can also start the second compressor to assist in producing hot water, an inlet of the third four-way valve is communicated with an outlet A of the third four-way valve, an outlet B of the third four-way valve is communicated with an outlet C of the third four-way valve, a high-temperature and high-pressure refrigerant output by the second compressor is used for producing hot water through the heat recovery heat exchanger, and the refrigerant returns to the second compressor through the second liquid reservoir and the fin heat exchanger to form a loop.
Preferably, the second compressor can be started to assist in producing hot water in the cooling and hot water mode, an inlet of the third four-way valve is communicated with an outlet A of the third four-way valve, an outlet B of the third four-way valve is communicated with an outlet C of the third four-way valve, a high-temperature and high-pressure refrigerant output by the second compressor is used for producing hot water through the heat recovery heat exchanger, and the refrigerant returns to the second compressor through the second liquid storage device and the fin heat exchanger to form a loop.
The utility model has the advantages that: the triple heat supply pump unit is small in occupied area and convenient to install, has modes of air conditioner refrigeration, air conditioner heating, refrigeration and hot water, heating and hot water, single hot water, defrosting and the like, can effectively meet the requirements of winter heating and hot water, simultaneously considers the rapid defrosting problem in winter, and can also improve the energy-saving effect to the maximum extent under the condition of meeting the hot water requirement in a transition season.
Drawings
Fig. 1 is a schematic view of the overall structure of the present invention.
Fig. 2 is a schematic diagram of the flow of the refrigerant in the cooling mode of the air conditioner according to the present invention.
Fig. 3 is a schematic diagram of the flow of the refrigerant in the heating mode of the air conditioner according to the present invention.
Fig. 4 is a schematic diagram of the refrigerant flow in the heating and hot water mode according to the present invention.
Fig. 5 is a schematic diagram of the flow of the refrigerant in the cooling and heating modes according to the present invention.
Fig. 6 is a schematic diagram of the flow of the refrigerant in the single hot water mode according to the present invention.
Fig. 7 is a schematic diagram of the flow of the refrigerant in the defrosting mode according to the present invention.
Fig. 8 is a diagram of the entrance and exit marks of the first, second, and third four-way valves.
Reference numerals
1. A first compressor; 2. a first four-way valve; 3. a heat recovery heat exchanger; 4. a first check valve; 5. a second one-way valve; 6. a second four-way valve; 7. an air conditioner heat exchanger; 8. a first reservoir; 9. a first electronic expansion valve; 10. a capillary tube; 11. a third check valve; 12. a finned heat exchanger; 13. a first gas-liquid separator; 14. a second compressor; 15. a third four-way valve; 16. a second reservoir; 17. a second electronic expansion valve; 18. a second gas-liquid separator.
Detailed Description
The present invention will be described in further detail with reference to the accompanying drawings.
As shown in fig. 1, a triple co-generation heat pump unit with heat recovery mainly comprises a triple co-generation assembly and a hot water assembly, wherein the triple co-generation assembly comprises a first compressor 1, a first four-way valve 2, a heat recovery heat exchanger 3, a first one-way valve 4, a second one-way valve 5, a second four-way valve 6, an air-conditioning heat exchanger 7, a first liquid reservoir 8, a throttling device and a fin heat exchanger 12; the hot water assembly includes a second compressor 14, a third four-way valve 15, a second accumulator 16, and a second electronic expansion valve 17. The heat recovery heat exchanger 3 is equipped with 2 heat transfer pipelines, and the 1 st heat transfer pipeline supplies the subassembly to be connected with the trigeminy to carry out the heat transfer, and the 2 nd heat transfer pipeline is connected with the hot water component and is carried out the heat transfer. Similarly, the finned heat exchanger 12 is also provided with 2 heat exchange pipelines, the 1 st heat exchange pipeline is connected with the triple co-generation assembly for heat exchange, and the 2 nd heat exchange pipeline is connected with the hot water assembly for heat exchange. As shown in fig. 8, the first four-way valve 2, the second four-way valve 6 and the third four-way valve 15 are all provided with an inlet (shown as D), an outlet a, an outlet B and an outlet C; the connection states of the inlets and 3 outlets of the first four-way valve 2, the second four-way valve 6 and the third four-way valve 15 can be switched, wherein one state is that the inlet is communicated with the outlet A, and the outlet B is communicated with the outlet C; and the other state is that the inlet is communicated with the outlet C, the outlet A is communicated with the outlet B, and the switching of different heat exchange modes is carried out by switching the conduction states of the first four-way valve 2, the second four-way valve 6 and the third four-way valve 15.
As shown in fig. 1, the connection relationship of the components in the triple co-generation assembly is specifically described.
The first compressor 1 is provided with an inlet end and an outlet end, the outlet end of the first compressor 1 is connected with an inlet of the first four-way valve 2, an outlet C of the first four-way valve 2 is connected with a 1 st heat exchange pipeline of the heat recovery heat exchanger 3 firstly, then is connected with the second one-way valve 5 in series and is connected with an inlet of the second four-way valve 6, and the conduction direction of the second one-way valve 5 is the direction from the heat recovery heat exchanger 3 to the inlet of the second four-way valve 6. The outlet a of the first four-way valve 2 is connected in series with the first check valve 4 and to the inlet of the second four-way valve 6, the conduction direction of the first check valve 4 is the direction from the outlet a of the first four-way valve 2 to the inlet of the second four-way valve 6, and the outlet B of the first four-way valve 2 is connected to the inlet of the first compressor 1. The outlet C of the second four-way valve 6 is connected with the heat exchange pipeline of the air-conditioning heat exchanger 7 firstly and then is connected to one end of the first liquid storage device 8, the other end of the first liquid storage device 8 is connected to the outlet A of the second four-way valve 6 through the 1 st heat exchange pipeline of the fin heat exchanger 12, and the outlet B of the second four-way valve 6 is connected with the inlet end of the first compressor 1. The throttling device is connected between the fin heat exchanger 12 and the first liquid storage device 8, and in order to ensure that the triple-generation assembly has a good refrigeration effect and simultaneously cannot weaken the low-temperature heating capacity, the throttling device adopts a first electronic expansion valve 9, a capillary tube 10 and a third one-way valve 11. The first electronic expansion valve 9 is directly connected in series between the fin heat exchanger 12 and the first liquid storage device 8, the capillary tube 10 and the third one-way valve 11 are connected in series, the capillary tube 10 and the third one-way valve 11 which are connected in series are connected in parallel with the first electronic expansion valve 9, and the conduction direction of the third one-way valve 11 is the direction from the fin heat exchanger 12 to the first liquid storage device 8.
Preferably, the triple co-generation assembly further comprises a first gas-liquid separator 13, one end of the first gas-liquid separator 13 is connected to the inlet end of the first compressor 1, and the other end of the first gas-liquid separator 13 is connected to the B outlet of the first four-way valve 2 and the B outlet of the second four-way valve 6.
Preferably, the first compressor 1 adopts an inverter compressor, which can adapt to the change of the refrigeration and heating load to the maximum extent, and the inverter compressor can play a corresponding energy-saving function in a transition season.
Preferably, the heat recovery heat exchanger 3 is a high efficiency tank or double pipe heat exchanger.
The connection of the components of the hot water assembly is specifically illustrated in fig. 1.
The second compressor 14 is provided with an inlet end and an outlet end, the outlet end of the second compressor 14 is connected with an inlet of a third four-way valve 15, an outlet A of the third four-way valve 15 is connected with a 2 nd heat exchange pipeline of the heat recovery heat exchanger 3 and is connected to one end of a second liquid storage device 16, the other end of the second liquid storage device 16 is connected to an outlet C of the third four-way valve 15 through the 2 nd heat exchange pipeline of the finned heat exchanger 12, and an outlet B of the third four-way valve 15 is connected with the inlet end of the second compressor 14.
Preferably, the hot water assembly further comprises a second gas-liquid separator 18, one end of the second gas-liquid separator 18 is connected to the inlet end of the second compressor 14, and the other end of the second gas-liquid separator 18 is connected to the B outlet of the third four-way valve 15.
The utility model discloses a take trigeminy of heat recovery to supply heat pump set has air conditioner refrigeration mode, air conditioner heating mode, refrigeration and hot water mode, heats and hot water mode, single hot water mode, changes the frost mode.
As shown in fig. 2, it is a schematic diagram of the refrigerant flow of the triple heat pump unit in the air-conditioning refrigeration mode. Under the air conditioner refrigeration mode, the first compressor 1 is started, the second compressor 14 is not started, the inlet of the first four-way valve 2 is communicated with the outlet A of the first four-way valve 2, the inlet of the second four-way valve 6 is communicated with the outlet A of the second four-way valve 6, the outlet B of the second four-way valve 6 is communicated with the outlet C of the second four-way valve 6, a high-temperature high-pressure refrigerant output by the first compressor 1 is subjected to heat exchange through the fin heat exchanger 12 and is condensed into a low-temperature low-pressure refrigerant, the low-temperature low-pressure refrigerant is throttled through the first electronic expansion valve 9 and the capillary tube 10, then the heat exchange is carried out on the air conditioner heat exchanger 7.
As shown in fig. 3, it is a schematic diagram of the refrigerant flow of the triple heat pump unit in the air-conditioning heating mode. In the air-conditioning heating mode, the first compressor 1 is started, the second compressor 14 is not started, the inlet of the first four-way valve 2 is communicated with the outlet A of the first four-way valve 2, the inlet of the second four-way valve 6 is communicated with the outlet C of the second four-way valve 6, the outlet A of the second four-way valve 6 is communicated with the outlet B of the second four-way valve 6, a high-temperature and high-pressure refrigerant output by the first compressor 1 firstly flows through the air-conditioning heat exchanger 7 to prepare air-conditioning hot water, and the refrigerant returns to the first compressor 1 through the first liquid storage device 8, the first electronic expansion valve 9 and the fin heat exchanger 12 to form. When the air-conditioning hot water is prepared, the general unit operates at a lower ambient temperature, the evaporation temperature is lower, and the required refrigerant is less, so that the first liquid storage device 8 is used for storing redundant refrigerant, the refrigerant only passes through the first electronic expansion valve 9 in the throttling device and does not pass through the capillary tube 10 for throttling, the supercooling degree of the refrigerant can be effectively adjusted, and the optimal heating capacity of the unit is ensured.
Fig. 4 is a schematic diagram of refrigerant flow of the triple heat pump unit in heating and hot water modes. In a heating and hot water mode, the first compressor 1 is started, the inlet of the first four-way valve 2 is communicated with the C outlet of the first four-way valve 2, the inlet of the second four-way valve 6 is communicated with the C outlet of the second four-way valve 6, the A outlet of the second four-way valve 6 is communicated with the B outlet of the second four-way valve 6, a high-temperature and high-pressure refrigerant output by the first compressor 1 firstly flows through the heat recovery heat exchanger 3 to prepare hot water, the refrigerant is condensed and subcooled through the air conditioner heat exchanger 7, and finally the refrigerant is throttled by the first electronic expansion valve 9, and a heat exchange air source is carried out on the fin heat exchanger 12 to absorb heat energy and returns. The second compressor 14 can be started to assist in making hot water, the inlet of the third four-way valve 15 is communicated with the outlet a of the third four-way valve 15, the outlet B of the third four-way valve 15 is communicated with the outlet C of the third four-way valve 15, a high-temperature and high-pressure refrigerant output by the second compressor 14 firstly flows through the heat recovery heat exchanger 3 to make hot water, and the refrigerant returns to the second compressor 14 through the second liquid reservoir 16, the second electronic expansion valve 17 and the fin heat exchanger 12 to form a loop.
Fig. 5 is a schematic diagram of refrigerant flow of the triple heat pump unit in the cooling and hot water modes. In the refrigeration and hot water mode, the first compressor 1 is started, the inlet of the first four-way valve 2 is communicated with the C outlet of the first four-way valve 2, the inlet of the second four-way valve 6 is communicated with the A outlet of the second four-way valve 6, the B outlet of the second four-way valve 6 is communicated with the C outlet of the second four-way valve 6, a high-temperature and high-pressure refrigerant output by the first compressor 1 firstly flows through the heat recovery heat exchanger 3 to prepare hot water, the refrigerant then passes through the fin heat exchanger 12 to be condensed and supercooled, the refrigerant is throttled by the first electronic expansion valve 9 and the capillary tube 10, then exchanges heat in the air conditioner heat exchanger 7 to prepare air conditioner cold water, and the refrigerant. The second compressor 14 can be started to assist in making hot water, the inlet of the third four-way valve 15 is communicated with the outlet a of the third four-way valve 15, the outlet B of the third four-way valve 15 is communicated with the outlet C of the third four-way valve 15, a high-temperature and high-pressure refrigerant output by the second compressor 14 firstly flows through the heat recovery heat exchanger 3 to make hot water, and the refrigerant returns to the second compressor 14 through the second liquid reservoir 16, the second electronic expansion valve 17 and the fin heat exchanger 12 to form a loop.
Fig. 6 is a schematic diagram of refrigerant flow of the triple heat pump unit in the single hot water mode. In the single hot water mode, the first compressor 1 is not started, the second compressor 14 is started, the inlet of the third four-way valve 15 is communicated with the outlet A of the third four-way valve 15, the outlet B of the third four-way valve 15 is communicated with the outlet C of the third four-way valve 15, a high-temperature and high-pressure refrigerant output by the second compressor 14 firstly flows through the heat recovery heat exchanger 3 to prepare hot water, and the refrigerant returns to the second compressor 14 through the second liquid storage device 16, the second electronic expansion valve 17 and the fin heat exchanger 12 to form a loop.
Fig. 7 is a schematic diagram of refrigerant flow of the triple heat pump unit in the defrosting mode. Under the defrosting mode, the first compressor 1 is started, the inlet of the first four-way valve 2 is communicated with the outlet A of the first four-way valve 2, the inlet of the second four-way valve 6 is communicated with the outlet A of the second four-way valve 6, the outlet B of the second four-way valve 6 is communicated with the outlet C of the second four-way valve 6, a high-temperature and high-pressure refrigerant output by the first compressor 1 directly flows to the frosted fin heat exchanger 12 for heat exchange and defrosting, then returns to the first compressor 1 through the first electronic expansion valve 9 and the capillary tube 10, the first liquid storage device 8 and the air conditioner heat exchanger 7 to form a loop, and the air conditioner heat exchanger 7 and the heat recovery heat exchanger 3 are not started.
The above embodiments are merely illustrative and not restrictive, and all equivalent changes and modifications made by the methods described in the claims are intended to be included within the scope of the present invention.
Claims (7)
1. The utility model provides a take trigeminy of heat recovery to supply heat pump set which characterized in that: the system comprises a triple-generation component and a hot water component, wherein the triple-generation component comprises a first compressor, a first four-way valve, a heat recovery heat exchanger, a first one-way valve, a second four-way valve, an air conditioner heat exchanger, a first liquid storage device and a fin heat exchanger; the hot water assembly comprises a second compressor, a third four-way valve and a second liquid storage device;
the first four-way valve, the second four-way valve and the third four-way valve are all provided with an inlet, an outlet A, an outlet B and an outlet C;
the heat recovery heat exchanger and the fin heat exchanger are both provided with 2 heat exchange pipelines;
the outlet end of the first compressor is connected with the inlet of the first four-way valve, the outlet C of the first four-way valve is connected with the inlet of the second four-way valve through the 1 st heat exchange pipeline and the second one-way valve of the heat recovery heat exchanger, the outlet A of the first four-way valve is connected with the inlet of the second four-way valve through the first one-way valve, and the outlet B of the first four-way valve is connected with the inlet end of the first compressor;
the outlet C of the second four-way valve is connected to one end of a first liquid storage device through an air conditioner heat exchanger, the other end of the first liquid storage device is connected to the outlet A of the second four-way valve through the 1 st heat exchange pipeline of the fin heat exchanger, and the outlet B of the second four-way valve is connected with the inlet end of the first compressor;
the outlet end of the second compressor is connected with the inlet of the third four-way valve, the outlet A of the third four-way valve is connected to one end of the second liquid storage device through the 2 nd heat exchange pipeline of the heat recovery heat exchanger, the other end of the second liquid storage device is connected to the outlet C of the third four-way valve through the 2 nd heat exchange pipeline of the finned heat exchanger, and the outlet B of the third four-way valve is connected with the inlet end of the second compressor.
2. The triple co-generation heat pump unit with heat recovery of claim 1, characterized in that: the triple supply assembly further comprises a throttling device, the throttling device comprises a first electronic expansion valve, a capillary tube and a third one-way valve, the first electronic expansion valve is connected between the fin heat exchanger and the first liquid storage device, the capillary tube is connected with the third one-way valve in series, the first electronic expansion valve is connected with the capillary tube and the third one-way valve which are connected in series in parallel, and the third one-way valve is communicated with the first liquid storage device in a one-way mode.
3. The triple co-generation heat pump unit with heat recovery of claim 1, characterized in that: the hot water assembly further comprises a second electronic expansion valve, and the second electronic expansion valve is connected between the fin heat exchanger and the second liquid storage device.
4. The triple co-generation heat pump unit with heat recovery of claim 1, characterized in that: the triple co-generation component further comprises a first gas-liquid separator, one end of the first gas-liquid separator is connected with the inlet end of the first compressor, and the other end of the first gas-liquid separator is connected with the outlet B of the first four-way valve and the outlet B of the second four-way valve.
5. The triple co-generation heat pump unit with heat recovery of claim 1, characterized in that: the hot water assembly further comprises a second gas-liquid separator, one end of the second gas-liquid separator is connected with the inlet end of the second compressor, and the other end of the second gas-liquid separator is connected with the outlet B of the third four-way valve.
6. The triple co-generation heat pump unit with heat recovery of claim 1, characterized in that: the first compressor is a variable frequency compressor.
7. The triple co-generation heat pump unit with heat recovery of claim 1, characterized in that: the heat recovery heat exchanger is a high-efficiency tank heat exchanger or a sleeve heat exchanger.
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| CN202021751767.5U CN212481758U (en) | 2020-08-20 | 2020-08-20 | Take trigeminy of heat recovery to supply heat pump set |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111811166A (en) * | 2020-08-20 | 2020-10-23 | 广东瑞星新能源科技有限公司 | Take trigeminy of heat recovery to supply heat pump set |
| CN115235145A (en) * | 2022-07-21 | 2022-10-25 | 北京工业大学 | Heat pump system with sleeve pipe fin type heat exchanger |
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2020
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111811166A (en) * | 2020-08-20 | 2020-10-23 | 广东瑞星新能源科技有限公司 | Take trigeminy of heat recovery to supply heat pump set |
| CN111811166B (en) * | 2020-08-20 | 2024-06-11 | 广东瑞星新能源科技有限公司 | Triple heat supply pump unit with heat recovery function |
| CN115235145A (en) * | 2022-07-21 | 2022-10-25 | 北京工业大学 | Heat pump system with sleeve pipe fin type heat exchanger |
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Address after: 529727 No. 255, Hexiang East Road, Zone C, Heshan industrial city, Jiangmen City, Guangdong Province Patentee after: GUANGDONG LUCKINGSTAR NEW ENERGY Co.,Ltd. Address before: No.3, Xinpu Road, Jiuqu Industrial Zone, Daojiao Town, Dongguan City, Guangdong Province, 523000 Patentee before: GUANGDONG LUCKINGSTAR NEW ENERGY Co.,Ltd. |