阅读说明：本技术 带全热回收的双冷源空气源热泵 (Double-cold-source air source heat pump with total heat recovery ) 是由 章立标 唐进军 韩伟达 经武辉 梁书成 顾君丰 张佳丽 于 2021-06-14 设计创作，主要内容包括：本发明属于热泵机械技术领域,尤其涉及带全热回收的双冷源空气源热泵。本发明公开的带全热回收的双冷源空气源热泵包括连接在制冷循环中的压缩机、四通换向阀、复合式水冷冷凝器、壳管式换热器、翅片式换热器、第一单向阀、第二单向阀、第一电磁阀、第二电磁阀、第一节流阀、第二节流阀、气液分离器、冷却塔、冷却水泵、水路单向阀、水路阀门组。本发明通过四通换向阀、第一电磁阀、第二电磁阀、水路阀门组状态的控制以及复合式水冷冷凝器、壳管式换热器中水流动状态的控制,可实现制冷、制冷加全热回收、制热、热水、制热加热水五种功能及运行模式之间的切换。通过全热回收解决常规楼宇建筑或工业行业项目全年制冷、采暖、卫生或工艺热水需求。(The invention belongs to the technical field of heat pump machinery, and particularly relates to a double-cold-source air source heat pump with total heat recovery. The invention discloses a double-cold-source air source heat pump with total heat recovery, which comprises a compressor, a four-way reversing valve, a combined water-cooled condenser, a shell-and-tube heat exchanger, a finned heat exchanger, a first check valve, a second check valve, a first electromagnetic valve, a second electromagnetic valve, a first throttling valve, a second throttling valve, a gas-liquid separator, a cooling tower, a cooling water pump, a waterway check valve and a waterway valve group, wherein the compressor, the four-way reversing valve, the combined water-cooled condenser, the shell-and-tube heat exchanger, the finned heat exchanger, the first check valve, the second check valve, the first electromagnetic valve, the second electromagnetic valve, the first throttling valve, the second throttling valve, the gas-liquid separator, the cooling tower, the cooling water pump, the waterway check valve and the waterway valve group are connected in a refrigeration cycle. The invention can realize the switching among five functions of refrigeration, refrigeration and total heat recovery, heating, hot water and heating and water heating and operation modes by controlling the states of the four-way reversing valve, the first electromagnetic valve, the second electromagnetic valve and the water path valve group and controlling the water flowing state in the combined water-cooled condenser and the shell-and-tube heat exchanger. The requirement of the conventional building or industrial project for refrigerating, heating, sanitation or process hot water all year round is solved through the total heat recovery.)

1. The utility model provides a take full heat recovery's two cold source air source heat pump set which characterized in that: including connecting compressor (1) in the refrigeration cycle return circuit, compressor (1) high pressure outlet connects four-way reversing valve (2) interface d, connects combined type water cooled condenser (3) of four-way reversing valve (2) interface c connects finned heat exchanger (5) of four-way reversing valve (2) interface e connects vapour and liquid separator (12) of four-way reversing valve (2) interface s, connects first check valve (6) of combined type water cooled condenser (3) export, connects second check valve (7), first solenoid valve (8) of first check valve (6) export, the second electromagnetic valve (9), a first throttling valve (10) connected with the outlet of the first electromagnetic valve (8), a second throttling valve (11) connected with the outlet of the second electromagnetic valve (9), and a shell-and-tube heat exchanger (4) connected with the outlet of the second throttling valve (11); the outlet of the first throttling valve (10), the inlet of the second one-way valve (7) and the liquid side interface of the finned heat exchanger (5) are connected with each other; the outlet of the gas-liquid separator (12), the outlet of the shell-and-tube heat exchanger (4) and the air suction port of the compressor (1) are connected with each other; the unit has the functions of refrigerating in summer and heating in winter, and also has the function of total heat recovery, and can provide process or sanitary hot water all year round; and in addition, low-pressure gas coming out of the shell-and-tube heat exchanger (4) directly enters an air suction port of a compressor, so that the refrigerating capacity and the refrigerating efficiency of the unit are improved.

2. The double-cold-source air-source heat pump unit with total heat recovery of claim 1, characterized in that: the device also comprises a first three-way valve (16) connected with a cooling water outlet of the combined type water-cooled condenser (3), a cooling tower (13) connected with a connector q of the first three-way valve (16), a cooling water pump (14) connected with a water outlet of the cooling tower (13), a waterway one-way valve (15) connected with an outlet of the cooling water pump (14), a hot water pump (20) connected with a process/sanitary hot water inlet of the combined type water-cooled condenser (3), and a second three-way valve (17) connected with a water inlet of the shell-and-tube heat exchanger (4); the interface m of the first three-way valve (16) is connected with the water outlet of the shell-and-tube heat exchanger (4); and the interface i of the second three-way valve (17) is connected with a cooling water inlet of the connection composite water-cooled condenser (3) and a water outlet of the waterway one-way valve (15).

3. The double-cold-source air-source heat pump unit with total heat recovery of claim 2, characterized in that: the composite water-cooled condenser (3) is provided with a total heat recovery heat exchange tube bundle at the upper part, the process/sanitary hot water at the inner side of the heat exchange tube can absorb the heat discharged by the high-temperature and high-pressure gas refrigerant at the outer side of the heat exchange tube in the condensation process, and the process/sanitary hot water leaves the composite water-cooled condenser (3) after the temperature rises and leads to the tail end of a user needing heat; the lower part is provided with a cooling water heat exchange tube bundle, the cooling water at the inner side of the heat exchange tube can absorb the heat discharged by the high-temperature and high-pressure gas refrigerant at the outer side of the heat exchange tube in the condensation process, and the cooling water leaves the composite water-cooled condenser (3) after the temperature rises; the process/sanitary hot water loop at the inner side of the heat exchange tube of the total heat recovery heat exchange tube bundle and the cooling water loop at the inner side of the heat exchange tube of the cooling water heat exchange tube bundle are mutually independent, and the high-temperature high-pressure gas refrigerant entering the top of the composite water-cooled condenser (3) firstly flows through the total heat recovery heat exchange tube bundle and then flows through the cooling water heat exchange tube bundle, and is condensed into high-pressure liquid after heat is discharged to the process/sanitary hot water or the cooling water.

4. The double-cold-source air-source heat pump unit with total heat recovery of claim 3, characterized in that: the interface p of the first three-way valve (16) is connected with a cooling water outlet of the composite water-cooled condenser (3), the interface q is connected with an inlet of the cooling tower, the interface m is connected with an air-conditioning water outlet of the shell-and-tube heat exchanger (4), the interface j of the second three-way valve (17) is connected with air-conditioning return water flowing from the tail end of an air conditioner, the interface h is connected with the air-conditioning water inlet of the shell-and-tube heat exchanger (4), the interface i is connected with the cooling water inlet of the composite water-cooled condenser (3), and a water channel valve group (18) formed by the first three-way valve (16), the second three-way valve (17) and pipe sections connected with the cooling water and the air-conditioning water can be replaced by a mode of combining a plurality of two-way valves and three-way valves; the three-way valve and the two-way valve can adopt electric or pneumatic or manual valves.

5. The method for controlling the refrigeration mode of the double-cold-source air-source heat pump unit with the total heat recovery function according to claim 4, wherein the method comprises the following steps: high-temperature and high-pressure gas refrigerant discharged by the compressor (1) enters the composite water-cooled condenser (3) through the interfaces d and c of the four-way reversing valve (2), flows through the outer side of the heat exchange tube of the total heat recovery heat exchange tube bundle, exchanges heat with cooling water on the inner side of the heat exchange tube with relatively low temperature on the outer side of the heat exchange tube of the cooling water heat exchange tube bundle, discharges the condensation heat to the cooling water, and is condensed into high-pressure liquid; high-pressure liquid sequentially passes through the first check valve (6) and the second electromagnetic valve (9) and then enters the second throttle valve (11), is throttled and depressurized into a low-temperature low-pressure gas-liquid mixed refrigerant, enters the shell-and-tube heat exchanger (4), absorbs the heat of air conditioner chilled water to cool the refrigerant, evaporates the refrigerant into low-pressure gas, finally returns to the air suction port of the compressor (1), is compressed into a high-temperature high-pressure gas refrigerant by the compressor (1), and is repeatedly circulated in the way; cooling water with the temperature increased by absorbing condensation heat of a high-temperature and high-pressure gas refrigerant enters a cooling tower (13) through a first three-way valve (16) interface p and an interface q, the temperature is reduced after the heat is discharged to outdoor air in the cooling tower (13), then the cooling water is conveyed to the inner side of a heat exchange pipe of a cooling water heat exchange pipe bundle at the lower part of a combined water-cooled condenser (3) through a water way one-way valve (15) by a cooling water pump (14), the temperature of the condensation heat discharged by the high-temperature and high-pressure gas refrigerant outside the heat exchange pipe is increased and leaves the combined water-cooled condenser (3), and the process is repeated; the air-conditioning chilled water with lower temperature from the shell-and-tube heat exchanger (4) flows to the tail end of the air conditioner of a user, cools the circulating air flowing through the tail end of the air conditioner to release cold energy, then the temperature is increased, the air-conditioning chilled water is conveyed back to the shell-and-tube heat exchanger (4) through a three-way valve connector j and a connector h by an air-conditioning water pump, exchanges heat with the low-temperature low-pressure gas-liquid mixed refrigerant throttled by the throttle valve (6), the air-conditioning chilled water leaves the shell-and-tube heat exchanger (4) after the air-conditioning chilled water is cooled by the refrigerant, and the air-conditioning chilled water is repeatedly circulated.

6. The method for controlling the cooling and heating water modes of the double-cold-source air source heat pump unit with the total heat recovery function according to claim 4, wherein the method comprises the following steps: high-temperature and high-pressure gas refrigerant discharged by the compressor (1) enters the composite water-cooled condenser (3) through the interface d and the interface c of the four-way reversing valve (2), exchanges heat with process/sanitary hot water on the inner side of a heat exchange tube with relatively low temperature on the outer side of a total heat recovery heat exchange tube bundle, and is condensed into high-pressure liquid after being discharged to the process/sanitary hot water; high-pressure liquid flows through the outer side of the cooling water heat exchange tube bundle and then leaves the composite water-cooled condenser (3), then sequentially passes through the first one-way valve (6) and the second electromagnetic valve (9) and then enters the second throttling valve (11), is throttled and decompressed into low-temperature and low-pressure gas-liquid mixed refrigerant and then enters the shell-and-tube evaporator (4), absorbs the heat of air conditioner chilled water to cool the refrigerant, then evaporates the refrigerant into low-pressure gas, finally returns to an air suction port of the compressor (1), is compressed into high-temperature and high-pressure gas refrigerant by the compressor (1), and is repeatedly circulated; the process/sanitary hot water absorbing the condensation heat of the high-temperature and high-pressure gas refrigerant with the increased temperature is conveyed to the end needing heat of a user, the temperature is reduced after the heat is discharged to the end needing heat, then the process/sanitary hot water is conveyed to the inner side of the heat exchange tube of the total heat recovery heat exchange tube bundle at the upper part of the composite water-cooled condenser (3), the condensation heat absorbing the high-temperature and high-pressure gas refrigerant at the outer side of the heat exchange tube with the increased temperature leaves the composite water-cooled condenser (3), and the process/sanitary hot water is repeatedly circulated; the air-conditioning chilled water with lower temperature from the shell-and-tube heat exchanger (4) flows to the tail end of the air conditioner of a user, cools the circulating air flowing through the tail end of the air conditioner to release cold energy, then the temperature is increased, the air-conditioning chilled water is conveyed back to the shell-and-tube heat exchanger (4) through a three-way valve connector j and a connector h by an air-conditioning water pump, exchanges heat with the low-temperature low-pressure gas-liquid mixed refrigerant throttled by the throttle valve (6), the air-conditioning chilled water leaves the shell-and-tube heat exchanger (4) after the air-conditioning chilled water is cooled by the refrigerant, and the air-conditioning chilled water is repeatedly circulated.

7. The heating mode control method of the double-cold-source air-source heat pump unit with total heat recovery as claimed in claim 4, wherein: the high-temperature high-pressure gas refrigerant discharged by the compressor (1) enters the composite water-cooled condenser (3) through the interface d and the interface c of the four-way reversing valve (2), flows through the outer side of a heat exchange tube of a total heat recovery heat exchange tube bundle, exchanges heat with air-conditioning hot water at the inner side of the heat exchange tube with relatively low temperature at the outer side of the heat exchange tube of the cooling water heat exchange tube bundle, is condensed into high-pressure liquid after being discharged to the air-conditioning hot water, then enters the first throttling valve (10) through the first one-way valve (6) and the first electromagnetic valve (8), enters the finned heat exchanger (5) after being throttled and decompressed into low-temperature low-pressure gas-liquid mixed refrigerant, exchanges heat with outdoor air with relatively high temperature, is evaporated into low-pressure gas refrigerant after absorbing the outdoor air heat, then sequentially passes through the interface e and the interface s of the four-way reversing valve (2) and the gas-liquid separator (12) and finally returns to the air suction port of the compressor (1), compressed into high-temperature and high-pressure gas refrigerant by the compressor (1), and repeatedly circulated in the way; the air conditioner hot water with lower temperature enters the inner side of a heat exchange pipe of a cooling water heat exchange pipe bundle at the lower part of the composite water-cooled condenser (3), absorbs the condensation heat discharged by a high-temperature and high-pressure gas refrigerant outside the heat exchange pipe, the condensation heat is heated and leaves the composite water-cooled condenser (3), then the condensation heat is conveyed to the tail end of a user air conditioner, the heat is discharged to the circulating air flowing through the tail end of the air conditioner, the temperature is reduced, and then the circulating air is conveyed back to the cooling water heat exchange pipe bundle by the air conditioner water pump, so that the circulation is repeated; when the surface of the finned heat exchanger is frosted or frozen, high-temperature and high-pressure gas discharged by the compressor (1) enters the finned heat exchanger (5) through the interfaces d and e of the four-way reversing valve (2), a large amount of condensation heat is transferred to the frost or ice on the surface of the fins, so that the frost or ice is absorbed and melted into water to be separated from the surfaces of the fins to realize the defrosting function, high-pressure gas refrigerant is condensed into high-pressure liquid, then enters the second throttling valve (11) through the second one-way valve (7) and the second electromagnetic valve (9), is throttled and decompressed into low-temperature and low-pressure gas-liquid mixed refrigerant, then enters the shell-tube heat exchanger (4) to exchange heat with air-conditioning hot water with higher temperature, is evaporated into low-pressure gas after absorbing the heat of the air-conditioning hot water, finally returns to an air suction port of the compressor (1), and is compressed into the high-temperature and high-pressure gas refrigerant by the compressor (1), and the process of repeated circulation is carried out, until defrosting is finished.

8. The hot water mode control method of the double-cold-source air source heat pump unit with total heat recovery as claimed in claim 4, wherein: high-temperature high-pressure gas discharged by the compressor (1) enters the composite water-cooled condenser (3) through the interfaces d and c of the four-way reversing valve (2), exchanges heat with relatively-low-temperature process/sanitary hot water on the outer side of a heat exchange pipe of the total heat recovery heat exchange pipe bundle, discharges a large amount of condensation heat to the process/sanitary hot water, is condensed into high-pressure liquid after being heated and heated, then leaves the composite water-cooled condenser (3) after flowing through a cooling water heat exchange pipe beam at the lower part of the composite water-cooled condenser (3), then enters the first throttle valve (10) through the first check valve (6) and the first electromagnetic valve (8) in sequence, enters the finned heat exchanger (5) after being throttled and decompressed into low-temperature low-pressure gas-liquid mixed refrigerant, exchanges heat with relatively-high-temperature outdoor air, and is evaporated into low-pressure gas after absorbing outdoor air heat, then the refrigerant passes through a connector e and a connector s of the four-way reversing valve (2) and the gas-liquid separator (12) in sequence and finally returns to the suction port of the compressor (1), and the refrigerant is compressed into high-temperature and high-pressure gas refrigerant by the compressor (1), and the process is repeated; the process/sanitary hot water with lower temperature enters the inner side of a heat exchange tube of a total heat recovery heat exchange tube bundle at the upper part of the combined type water-cooled condenser (3), absorbs the condensation heat discharged by a high-temperature and high-pressure gas refrigerant at the outer side of the heat exchange tube, the condensation heat rises, leaves the combined type water-cooled condenser (3), is conveyed to the end needing heat of a user, discharges the heat to the end needing heat, reduces the temperature of the end needing heat, and is conveyed to the inner side of the heat exchange tube of the total heat recovery heat exchange tube bundle at the upper part of the combined type water-cooled condenser (3), and the process/sanitary hot water is circulated repeatedly in such a way; when the surface of the finned heat exchanger is frosted or frozen, a high-temperature high-pressure gas refrigerant discharged by the compressor (1) sequentially enters the finned heat exchanger (5) through the interfaces d and e of the four-way reversing valve (2), a large amount of condensation heat is discharged to the frost or ice on the surface of the fins, the frost or ice is melted into water to be separated from the surfaces of the fins so as to realize the defrosting function, the high-pressure gas is condensed into high-pressure liquid, then enters the second throttling valve (11) through the second one-way valve (7) and the second electromagnetic valve (9), is throttled and depressurized into a low-temperature low-pressure gas-liquid mixed refrigerant, then enters the shell-tube heat exchanger (4), is evaporated into low-pressure gas after absorbing the air conditioning water heat, finally returns to an air suction port of the compressor (1), is compressed into the high-temperature high-pressure gas refrigerant by the compressor (1), and the cycle is repeated; the air conditioning water entering the shell-and-tube heat exchanger (4) releases heat to the throttled low-temperature low-pressure gas-liquid mixed refrigerant, the temperature of the air conditioning water is reduced, the air conditioning water leaves the shell-and-tube heat exchanger (4), the air conditioning water is driven by an air conditioning water pump to return to the shell-and-tube heat exchanger (4) after passing through an air conditioning tail end and an air conditioning water loop, and the repeated circulation is carried out until defrosting is finished.

9. The heating and water heating mode control method of the double-cold-source air source heat pump unit with total heat recovery as claimed in claim 4, wherein: the process/sanitary hot water waterway and the air-conditioning hot water waterway can be operated simultaneously according to the requirement, or only the process/sanitary hot water waterway is operated, or only the air-conditioning hot water waterway is operated; when the process/sanitary hot water is selected as an optimized heating object, the operation of the air-conditioning hot water waterway can be stopped firstly, the operation of the process/sanitary hot water waterway is stopped after the temperature of the process/sanitary hot water reaches a set value, and the air-conditioning hot water waterway is put into an operating state; when the air-conditioning hot water is selected as an optimized heating object, the process/sanitary hot water waterway can stop running firstly, the air-conditioning hot water waterway stops running after the water temperature of the air-conditioning hot water reaches a set value, and the process/sanitary hot water waterway is put into a running state; when the air-conditioning hot water waterway is put into operation, the air-conditioning hot water enters the inner sides of the heat exchange tubes of the cooling water heat exchange tube bundles at the lower part of the composite condenser (3); the high-temperature high-pressure gas refrigerant discharged by the compressor (1) enters the composite water-cooled condenser (3) through the interface d and the interface c of the four-way reversing valve (2), flows through the outer side of a total heat recovery heat exchange tube bundle heat exchange tube and the outer side of a cooling water heat exchange tube bundle heat exchange tube in sequence, exchanges heat with relatively low-temperature process/sanitary hot water or air-conditioning hot water, is condensed into high-pressure liquid after being discharged to the process/sanitary hot water or the air-conditioning hot water, then enters the first throttling valve (10) through the first one-way valve (6) and the first electromagnetic valve (8), is throttled and decompressed into low-temperature low-pressure gas-liquid mixed refrigerant, then enters the finned heat exchanger (5), exchanges heat with relatively high-temperature outdoor air, is evaporated into low-pressure gas refrigerant after absorbing the outdoor air heat, and then sequentially passes through the interface e and the interface s of the four-way reversing valve (2), The gas-liquid separator (12) finally returns to the air suction port of the compressor (1) and is compressed into high-temperature and high-pressure gas refrigerant by the compressor (1), and the process is repeated; the air-conditioning hot water or the process/sanitary hot water with lower temperature enters the composite water-cooled condenser (3), the condensation heat discharged by the high-temperature and high-pressure gas refrigerant outside the heat exchange tube is absorbed, the temperature of the condensation heat is increased, the condensation heat leaves the composite water-cooled condenser (3), then the condensation heat is conveyed to the air-conditioning end or the heat-requiring end of a user, the heat is discharged to the air-conditioning end or the heat-requiring end, the temperature of the heat-requiring end is reduced, and then the heat is conveyed back to the composite water-cooled condenser (3), and the process/sanitary hot water is repeatedly circulated.

10. The double-cold-source air-source heat pump unit with total heat recovery of claim 1, characterized in that: the operation of the process/sanitary hot water waterway in the combined type water-cooled condenser (3) can be controlled by starting and stopping a hot water pump and also can be switched and controlled by an electric or pneumatic valve, and the electric and pneumatic valves can adopt two-way valves and three-way valves; the waterway one-way valve (15) connected with the outlet of the cooling water pump (14) can be replaced by a first two-way valve (22) and a first two-way valve (22), and the first two-way valve (22) can adopt electric or pneumatic or manual valves.

Technical Field

The invention belongs to the technical field of heat pump machinery, and particularly relates to a double-cold-source air source heat pump with total heat recovery.

Background

The conventional central air-conditioning host generally adopts the following two modes:

1 Water-cooled chiller Unit

During refrigeration, a water-cooled water chilling unit provides 7 ℃ chilled water for the tail end of an air conditioner such as a fan coil to cool air in a room, a water-cooled condenser transfers condensation heat of a high-temperature and high-pressure refrigerant to cooling water, and the cooling water is conveyed to a cooling tower by a cooling water pump to discharge the heat to outdoor atmosphere. Usually, a water-cooling water chilling unit is placed indoors, a cooling tower is placed outdoors, a longer cooling water circulation pipeline is arranged between the water-cooling water chilling unit and the cooling tower, and a high-power and large-lift cooling water pump is needed to drive cooling water to circulate; and the linkage performance of the main machine, the cooling tower and the cooling water pump is poor, so that the whole air conditioning system is high in power consumption and low in energy efficiency.

When heating is carried out in winter and transition seasons, additional heating equipment such as a boiler and the like is required to be arranged, so that the energy efficiency is low, the environmental pollution is large, and the operation and maintenance are complex.

The matched civil engineering and the occupation of indoor space cause higher construction cost.

2 air-cooled cold and hot water unit

When refrigerating in summer, the air-cooled cold and hot water unit discharges a large amount of heat released by high-temperature and high-pressure gas compressed by the compressor in the condensation process to outdoor air through the fin heat exchanger, the specific heat capacity and the density of the air are low, the temperature rise of the air is generally about 10 ℃, and the average temperature of inlet and outlet air is high; meanwhile, the heat transfer coefficient of the air side is low, and the required heat exchange temperature difference is large. Therefore, the condensing temperature of the air-cooled cold and hot water unit is very high, the refrigeration energy efficiency is usually only 2.6-3.0, the energy consumption of the system is overlarge, and the national energy-saving and emission-reducing policy is not met.

When a conventional air-cooled cold and hot water unit performs refrigeration operation in summer, low-pressure refrigerant gas coming out of a water side heat exchanger of an air conditioner generally needs to sequentially pass through a four-way valve and a gas-liquid separator and then enters a compressor, and the on-way resistance and the local resistance of a low-pressure suction pipeline are large, so that the suction pressure of the compressor and the refrigeration efficiency of the unit are reduced.

Whether the water cooling water chilling unit or the air cooling water chilling and heating unit is adopted, a large amount of condensation waste heat needs to be discharged to the outdoor atmosphere environment in summer, so that the outdoor temperature is obviously increased, and the urban heat island effect is caused.

Disclosure of Invention

In order to overcome the defects that a water-cooled water chiller cannot realize the heating function in winter and a boiler is required to be configured to solve the problem that the cooling energy efficiency of an air-cooled water chiller is too low in summer, the invention provides a double-cold-source air source heat pump with total heat recovery, water cooling is adopted in summer, and a cooling water system consisting of a cooling tower and a cooling water pump is integrated to greatly improve the refrigerating capacity and the cooling energy efficiency; in winter, an air source heat pump is adopted to provide an air conditioning and heating function. Meanwhile, during refrigeration in summer, the condensation waste heat can be used for producing free process/sanitary hot water, and in other seasons, the fin type heat exchanger can absorb the heat of outdoor air, and then refrigeration cycle and compressor do work to prepare process/sanitary hot water, so that the problems of annual air conditioning refrigeration, air conditioning heating and process/sanitary hot water are solved.

In a first aspect of the invention, the invention provides a double-cold-source air source heat pump unit with total heat recovery, which comprises a compressor 1 connected in a refrigeration circulation loop, the high-pressure outlet of the compressor 1 is connected with a connector d of a four-way reversing valve 2, a combined type water-cooled condenser 3 connected with a connector c of the four-way reversing valve 2, a finned heat exchanger 5 connected with a connector e of the four-way reversing valve 2, a gas-liquid separator 12 connected with a connector s of the four-way reversing valve 2, a first one-way valve 6 connected with an outlet of the combined type water-cooled condenser 3, a second one-way valve 7, a first electromagnetic valve 8 and a second electromagnetic valve 9 connected with an outlet of the first one-way valve 6, a first throttling valve 10 connected with an outlet of the first electromagnetic valve 8, a second throttling valve 11 connected with an outlet of the second electromagnetic valve 9 and a shell-and-tube heat exchanger 4 connected with an outlet of the second throttling valve 11; the outlet of the first throttle valve 10 is connected with the inlet of the second one-way valve 7 and the liquid side interface of the finned heat exchanger 5; the outlet of the gas-liquid separator 12 is connected with the outlet of the shell-and-tube heat exchanger 4 and the air suction port of the compressor 1; the unit has the functions of refrigerating in summer and heating in winter, and also has the function of total heat recovery, and can provide process or sanitary hot water all year round; and in addition, low-pressure gas coming out of the shell-and-tube heat exchanger 4 directly enters an air suction port of a compressor, so that the refrigerating capacity and the refrigerating efficiency of the unit are improved.

In addition, according to the above embodiment of the present invention, the following additional technical features may be provided:

specifically, the heat pump unit of the invention further comprises a first three-way valve 16 connected with a cooling water outlet of the combined type water-cooled condenser 3, a cooling tower 13 connected with a connector q of the first three-way valve 16, a cooling water pump 14 connected with a water outlet of the cooling tower 13, a waterway one-way valve 15 connected with an outlet of the cooling water pump 14, a hot water pump 20 connected with a process/sanitary hot water inlet of the combined type water-cooled condenser 3, and a second three-way valve 17 connected with a water inlet of the shell-and-tube heat exchanger 4; the port m of the first three-way valve 16 is connected with the water outlet of the shell-and-tube heat exchanger 4; and the interface i of the second three-way valve 17 is connected with a cooling water inlet of the connection composite water-cooled condenser 3 and a water outlet of the waterway one-way valve 15.

Specifically, the composite water-cooled condenser 3 is provided with a total heat recovery heat exchange tube bundle at the upper part, the process/sanitary hot water at the inner side of the heat exchange tube can absorb the heat discharged by the high-temperature and high-pressure gas refrigerant at the outer side of the heat exchange tube in the condensation process, and the process/sanitary hot water leaves the composite water-cooled condenser 3 after the temperature rises and leads to the heat-required end of a user; the lower part is provided with a cooling water heat exchange tube bundle, the cooling water at the inner side of the heat exchange tube can absorb the heat discharged by the high-temperature and high-pressure gas refrigerant at the outer side of the heat exchange tube in the condensation process, and the cooling water leaves the composite water-cooled condenser 3 after the temperature rises; the process/sanitary hot water loop at the inner side of the heat exchange tube of the total heat recovery heat exchange tube bundle and the cooling water loop at the inner side of the heat exchange tube of the cooling water heat exchange tube bundle are mutually independent, and the high-temperature high-pressure gas refrigerant entering the top of the composite water-cooled condenser 3 firstly flows through the total heat recovery heat exchange tube bundle and then flows through the cooling water heat exchange tube bundle, and is condensed into high-pressure liquid after the heat is discharged to the process/sanitary hot water or the cooling water.

Specifically, a first three-way valve 16 interface p is connected with a cooling water outlet of the composite water-cooled condenser 3, an interface q is connected with a cooling tower inlet, an interface m is connected with an air conditioner water outlet of the shell-and-tube heat exchanger 4, an interface j of a second three-way valve 17 is connected with air conditioner return water flowing from the tail end of an air conditioner, an interface h is connected with the air conditioner water inlet of the shell-and-tube heat exchanger 4, and an interface i is connected with the cooling water inlet of the composite water-cooled condenser 3, wherein a waterway valve group 18 formed by the first three-way valve 16, the second three-way valve 17, a pipe section connected with the cooling water and the air conditioner water can be replaced by a mode of combining a plurality of two-way valves and three-way valves; the three-way valve and the two-way valve can adopt electric or pneumatic or manual valves.

The refrigeration mode control method of the heat pump unit is used, the four-way reversing valve 2 and the first electromagnetic valve 8 are powered off, the second electromagnetic valve 9 is powered on, the interface p of the first three-way valve 16 is conducted with the interface q, the interface p and the interface q are not conducted with the interface m, the interface h of the second three-way valve 17 is conducted with the interface j, the interface h and the interface j are not conducted with the interface i, the cooling tower 13 and the cooling water pump 14 are in a running state, an air conditioning water path in the shell-and-tube heat exchanger 4 is in a running state, the fan of the fin type heat exchanger 5 stops running, and a process/sanitary hot water path on the inner side of a total heat recovery heat exchange tube bundle heat exchange tube on the upper portion of the combined type water-cooled condenser 3 does not run; high-temperature and high-pressure gas refrigerant discharged by the compressor 1 enters the composite water-cooled condenser 3 through the interface d and the interface c of the four-way reversing valve 2, flows through the outer side of the heat exchange tube of the total heat recovery heat exchange tube bundle, exchanges heat with cooling water on the inner side of the heat exchange tube with relatively low temperature on the outer side of the heat exchange tube of the cooling water heat exchange tube bundle, discharges condensation heat to the cooling water, and is condensed into high-pressure liquid; the high-pressure liquid sequentially passes through the first check valve 6 and the second electromagnetic valve 9 and then enters the second throttle valve 11, is throttled and depressurized into a low-temperature and low-pressure gas-liquid mixed refrigerant, enters the shell-and-tube heat exchanger 4, absorbs the heat of the air conditioner chilled water to cool the refrigerant, evaporates the refrigerant into low-pressure gas, finally returns to the air suction port of the compressor 1, is compressed into a high-temperature and high-pressure gas refrigerant by the compressor 1, and is repeatedly circulated in the way; cooling water absorbing condensation heat of the high-temperature and high-pressure gas refrigerant and having the increased temperature enters the cooling tower 13 through the interfaces p and q of the first three-way valve 16, the heat is discharged to outdoor air in the cooling tower 13, the temperature is decreased, then the cooling water is conveyed to the inner side of the heat exchange tube of the cooling water heat exchange tube bundle at the lower part of the combined water-cooled condenser 3 through the waterway one-way valve 15 by the cooling water pump 14, the condensation heat absorbing the condensation heat discharged by the high-temperature and high-pressure gas refrigerant at the outer side of the heat exchange tube is increased and leaves the combined water-cooled condenser 3, and the process is repeated; the air-conditioning chilled water with lower temperature from the shell-and-tube heat exchanger 4 flows to the tail end of the air conditioner of a user, cools the circulating air flowing through the tail end of the air conditioner to release cold energy, then the temperature is increased, the air-conditioning chilled water is conveyed back to the shell-and-tube heat exchanger 4 through a three-way valve connector j and a connector h by an air-conditioning water pump, exchanges heat with the low-temperature low-pressure gas-liquid mixed refrigerant throttled by the throttle valve 6, the air-conditioning chilled water leaves the shell-and-tube heat exchanger 4 after the temperature is reduced by the refrigerant, and the circulation is repeated.

The refrigeration and heating water mode control method using the heat pump unit comprises the steps that a four-way reversing valve 2 and a first electromagnetic valve 8 are powered off, a second electromagnetic valve 9 is powered on, a connector p of a first three-way valve 16 is conducted with a connector q, the connector p and the connector q are not conducted with a connector m, a connector h of a second three-way valve 17 is conducted with a connector j, the connector h and the connector j are not conducted with a connector i, a cooling tower 13 and a cooling water pump 14 stop running, a process/sanitary hot water waterway on the inner side of a total heat recovery heat exchange tube bundle heat exchange tube on the upper portion of a combined type water-cooled condenser 3 runs, an air conditioner waterway in a shell and tube heat exchanger 4 is in a running state, and a fan of a fin type heat exchanger 5 stops running; high-temperature and high-pressure gas refrigerant discharged by the compressor 1 enters the composite water-cooled condenser 3 through the interface d and the interface c of the four-way reversing valve 2, exchanges heat with process/sanitary hot water on the inner side of a heat exchange tube with relatively low temperature on the outer side of a heat exchange tube of the total heat recovery heat exchange tube bundle, and is condensed into high-pressure liquid after being discharged to the process/sanitary hot water; the high-pressure liquid flows through the outer side of the cooling water heat exchange tube bundle and then leaves the composite water-cooled condenser 3, then sequentially passes through the first check valve 6 and the second electromagnetic valve 9 and then enters the second throttling valve 11, is throttled and depressurized into low-temperature and low-pressure gas-liquid mixed refrigerant, then enters the shell-and-tube evaporator 4, absorbs the heat of the air conditioner chilled water, cools the air conditioner chilled water to be evaporated into low-pressure gas, finally returns to the air suction port of the compressor 1, is compressed into high-temperature and high-pressure gas refrigerant by the compressor 1, and is repeatedly circulated in the way; the process/sanitary hot water absorbing the condensation heat of the high-temperature and high-pressure gas refrigerant and having the temperature rising is conveyed to the end needing heat of a user, the temperature of the process/sanitary hot water is reduced after the heat is discharged to the end needing heat, then the process/sanitary hot water is conveyed to the inner side of the heat exchange tube of the total heat recovery heat exchange tube bundle at the upper part of the combined type water-cooled condenser 3, the condensation heat absorbing the high-temperature and high-pressure gas refrigerant outside the heat exchange tube has the temperature rising and leaves the combined type water-cooled condenser 3, and the process/sanitary hot water is circulated repeatedly in the way; the air-conditioning chilled water with lower temperature from the shell-and-tube heat exchanger 4 flows to the tail end of the air conditioner of a user, cools the circulating air flowing through the tail end of the air conditioner to release cold energy, then the temperature is increased, the air-conditioning chilled water is conveyed back to the shell-and-tube heat exchanger 4 through a three-way valve connector j and a connector h by an air-conditioning water pump, exchanges heat with the low-temperature low-pressure gas-liquid mixed refrigerant throttled by the throttle valve 6, the air-conditioning chilled water leaves the shell-and-tube heat exchanger 4 after the temperature is reduced by the refrigerant, and the circulation is repeated.

The heating mode control method of the heat pump unit is used, the four-way reversing valve 2 and the second electromagnetic valve 9 are powered off, the first electromagnetic valve 8 is powered on, the interface p of the first three-way valve 16 is conducted with the interface m, the interface p and the interface m are not conducted with the interface q, the interface j of the second three-way valve 17 is conducted with the interface i, the interface j and the interface i are not conducted with the interface h, the cooling tower 13 and the cooling water pump 14 stop running, the process/sanitary hot water waterway stops running, the fan of the finned heat exchanger 5 is in a running state, and air-conditioning hot water enters the inner side of the heat exchange tube of the cooling water heat exchange tube bundle at the lower part of the composite water-cooled condenser 3; the high-temperature high-pressure gas refrigerant discharged by the compressor 1 enters the composite water-cooled condenser 3 through the interface d and the interface c of the four-way reversing valve 2, flows through the outer side of the heat exchange tube of the total heat recovery heat exchange tube bundle, exchanges heat with air-conditioning hot water at the inner side of the heat exchange tube with relatively low temperature at the outer side of the heat exchange tube of the cooling water heat exchange tube bundle, is condensed into high-pressure liquid after being discharged to the air-conditioning hot water, then enters the first throttling valve 10 through the first one-way valve 6 and the first electromagnetic valve 8, enters the finned heat exchanger 5 after being throttled and depressurized into low-temperature low-pressure gas-liquid mixed refrigerant, exchanges heat with outdoor air with relatively high temperature, is evaporated into low-pressure gas refrigerant after absorbing the outdoor air heat, then sequentially passes through the interface e and the interface s of the four-way reversing valve 2 and the gas-liquid separator 12, finally returns to the air suction port of the compressor 1 to be compressed into high-temperature high-pressure gas refrigerant by the compressor 1, the above steps are repeated and circulated; the lower-temperature air-conditioning hot water enters the inner side of a heat exchange pipe of a cooling water heat exchange pipe bundle at the lower part of the composite water-cooled condenser 3, absorbs the condensation heat discharged by a high-temperature and high-pressure gas refrigerant outside the heat exchange pipe, the condensation heat is increased in temperature and then leaves the composite water-cooled condenser 3, and then is conveyed to the tail end of a user air conditioner, the heat is discharged to circulating air flowing through the tail end of the air conditioner, the temperature is reduced, and then the circulating air is conveyed back to the cooling water heat exchange pipe bundle by the air-conditioning water pump, so that the circulating is repeated; when the surface of the finned heat exchanger is frosted or frozen, the first electromagnetic valve 8 is powered off, the four-way reversing valve 2 and the second electromagnetic valve 9 are powered on, a connector p of a first three-way valve 16 is communicated with a connector m, the connector p and the connector m are not communicated with a connector q, a connector j of a second three-way valve 17 is completely communicated with a connector h or is mostly communicated, the cooling tower 13 and the cooling water pump 14 stop running, the fan of the finned heat exchanger 5 stops running, and the process/sanitary hot water waterway stops running; high-temperature high-pressure gas discharged by the compressor 1 enters the finned heat exchanger 5 through the interfaces d and e of the four-way reversing valve 2, a large amount of condensation heat is transferred to frost or ice on the surfaces of fins, so that the frost or ice absorbs heat and melts into water to be separated from the surfaces of the fins, thereby realizing the defrosting function, high-pressure gas refrigerant is condensed into high-pressure liquid, then enters the second throttling valve 11 through the second one-way valve 7 and the second electromagnetic valve 9, is throttled and depressurized into low-temperature low-pressure gas-liquid mixed refrigerant, then enters the shell-and-tube heat exchanger 4 to exchange heat with air-conditioner hot water with higher temperature, evaporates into low-pressure gas after absorbing the heat of the air-conditioner hot water, finally returns to an air suction port of the compressor 1, is compressed into the high-temperature high-pressure gas refrigerant by the compressor 1, and is repeatedly circulated until defrosting is finished.

The hot water mode control method of the heat pump unit is used, the four-way reversing valve 2 and the second electromagnetic valve 9 are powered off, the first electromagnetic valve 8 is powered on, the on-off of each interface of the first three-way valve 16 and the second three-way valve 17 keeps the state of the last refrigerating or heating operation, the cooling tower 13 and the cooling water pump 14 stop running, the air-conditioning water path in the shell-and-tube heat exchanger 4 stops running, the process/sanitary hot water path on the inner side of the total heat recovery heat exchange tube bundle at the upper part of the combined water-cooled condenser 3 runs, and the fan of the finned heat exchanger 5 is in the running state; the high-temperature high-pressure gas discharged by the compressor 1 enters the composite water-cooled condenser 3 through the interface d and the interface c of the four-way reversing valve 2, exchanges heat with relatively-low-temperature process/sanitary hot water on the outer side of a heat exchange pipe of the total heat recovery heat exchange pipe bundle, discharges a large amount of condensation heat to the process/sanitary hot water, is condensed into high-pressure liquid after being heated and heated, then leaves the composite water-cooled condenser 3 after flowing through a cooling water heat exchange pipe on the lower part of the composite water-cooled condenser 3, then enters the first throttle valve 10 through the first check valve 6 and the first electromagnetic valve 8 in sequence, enters the finned heat exchanger 5 after being throttled and decompressed into low-temperature low-pressure gas-liquid mixed refrigerant, exchanges heat with relatively-high-temperature outdoor air, evaporates into low-pressure gas after absorbing the outdoor air heat, and then sequentially passes through the interface e and the interface s of the four-way reversing valve 2, The gas-liquid separator 12 finally returns to the suction port of the compressor 1, and is compressed into high-temperature and high-pressure gas refrigerant by the compressor 1, and the cycle is repeated in this way; the process/sanitary hot water with lower temperature enters the inner side of the heat exchange tube of the total heat recovery heat exchange tube bundle at the upper part of the combined type water-cooled condenser 3, absorbs the condensation heat discharged by the high-temperature and high-pressure gas refrigerant at the outer side of the heat exchange tube, the temperature of the condensation heat rises, the condensation heat leaves the combined type water-cooled condenser 3, then the condensation heat is conveyed to the heat-requiring tail end of a user, the heat is discharged to the heat-requiring tail end, the temperature of the heat-requiring tail end is reduced, then the heat is conveyed to the inner side of the heat exchange tube of the total heat recovery heat exchange tube bundle at the upper part of the combined type water-cooled condenser 3, and the process/sanitary hot water is circulated repeatedly; when the surface of the finned heat exchanger is frosted or frozen, the first electromagnetic valve 8 is powered off, the four-way reversing valve 2 and the second electromagnetic valve 9 are powered on, a connector p of a first three-way valve 16 is communicated with a connector m, the connector p and the connector m are not communicated with a connector q, a connector j of a second three-way valve 17 is completely communicated or partially communicated with a connector h, the cooling tower 13 and the cooling water pump 14 stop running, a fan of the finned heat exchanger 5 stops running, and an air conditioning water path in the shell and tube heat exchanger 4 runs; the high-temperature high-pressure gas refrigerant discharged by the compressor 1 sequentially enters the finned heat exchanger 5 through the interface d and the interface e of the four-way reversing valve 2, a large amount of condensation heat is discharged to frost or ice on the surface of the fin, the frost or ice is melted into water to be separated from the surface of the fin so as to achieve a defrosting function, the high-pressure gas is condensed into high-pressure liquid, then enters the second throttling valve 11 through the second one-way valve 7 and the second electromagnetic valve 9, is throttled and depressurized into low-temperature low-pressure gas-liquid mixed refrigerant, then enters the shell-and-tube heat exchanger 4, is evaporated into low-pressure gas after absorbing the air-conditioning water heat, finally returns to the air suction port of the compressor 1, is compressed into the high-temperature high-pressure gas refrigerant by the compressor 1, and the cycle is repeated; the air-conditioning water entering the shell-and-tube heat exchanger 4 releases heat to the throttled low-temperature low-pressure gas-liquid mixed refrigerant, the temperature of the air-conditioning water is reduced, the air-conditioning water leaves the shell-and-tube heat exchanger 4, the air-conditioning water is driven by an air-conditioning water pump to pass through the air-conditioning tail end and an air-conditioning water loop and then returns to the shell-and-tube heat exchanger 4, and the repeated circulation is carried out until defrosting is finished.

The heating and water heating mode control method of the heat pump unit is used, the four-way reversing valve 2 and the second electromagnetic valve 9 are powered off, the first electromagnetic valve 8 is powered on, the interface p of the first three-way valve 16 is communicated with the interface m, the interface p and the interface m are not communicated with the interface q, the interface j of the second three-way valve 17 is communicated with the interface i, the interface j and the interface i are not communicated with the interface h, the cooling tower 13 and the cooling water pump 14 stop running, and the fan of the fin type heat exchanger 5 is in a running state; the process/sanitary hot water waterway and the air-conditioning hot water waterway can be operated simultaneously according to requirements, or only the process/sanitary hot water waterway is operated, or only the air-conditioning hot water waterway is operated. When the process/sanitary hot water is selected as an optimized heating object, the operation of the air-conditioning hot water waterway can be stopped firstly, the operation of the process/sanitary hot water waterway is stopped after the temperature of the process/sanitary hot water reaches a set value, and the air-conditioning hot water waterway is put into an operating state; when the air-conditioning hot water is selected as an optimized heating object, the process/sanitary hot water waterway can stop running firstly, the air-conditioning hot water waterway stops running after the water temperature of the air-conditioning hot water reaches a set value, and the process/sanitary hot water waterway is put into a running state; when the air-conditioning hot water waterway is put into operation, the air-conditioning hot water enters the inner sides of the heat exchange tubes of the cooling water heat exchange tube bundles at the lower part of the composite condenser 3; the high-temperature high-pressure gas refrigerant discharged by the compressor 1 enters the composite water-cooled condenser 3 through the interface d and the interface c of the four-way reversing valve 2, flows through the outer side of a total heat recovery heat exchange tube bundle heat exchange tube and the outer side of a cooling water heat exchange tube bundle heat exchange tube in sequence, exchanges heat with process/sanitary hot water or air conditioning hot water with relatively low temperature, is condensed into high-pressure liquid after being discharged to the process/sanitary hot water or the air conditioning hot water, then enters the first throttling valve 10 through the first one-way valve 6 and the first electromagnetic valve 8, enters the finned heat exchanger 5 after being throttled and depressurized into low-temperature low-pressure gas-liquid mixed refrigerant, exchanges heat with outdoor air with relatively high temperature, is evaporated into low-pressure gas refrigerant after absorbing the outdoor air heat, then sequentially passes through the interface e and the interface s of the four-way reversing valve 2 and the gas-liquid separator 12 and finally returns to the air suction port of the compressor 1, compressed into high-temperature and high-pressure gas refrigerant by the compressor 1, and repeatedly circulated in such a way; the air-conditioning hot water or the process/sanitary hot water with lower temperature enters the composite water-cooled condenser 3, the condensation heat discharged by the high-temperature and high-pressure gas refrigerant outside the heat exchange tube is absorbed, the temperature of the condensation heat is increased, the condensation heat leaves the composite water-cooled condenser 3 and is then conveyed to the end of the user air conditioner or the end needing heat, the heat is discharged to the end of the air conditioner or the end needing heat, the temperature of the end needing heat is reduced, and then the condensation heat is conveyed back to the composite water-cooled condenser 3, and the process/sanitary hot water is circulated repeatedly.

Specifically, the operation of the process/sanitary hot water waterway in the combined water-cooled condenser 3 can be controlled by starting and stopping the hot water pump or switching the hot water pump through an electric or pneumatic valve, and the electric or pneumatic valve can be a two-way valve or a three-way valve; the waterway check valve 15 connected to the outlet of the cooling water pump 14 may be replaced with a first two-way valve 22 and a first two-way valve 22, and the first two-way valve 22 may be electrically, pneumatically or manually operated valves.

The invention has five functions of refrigeration, heating, refrigeration plus total heat recovery, hot water and heating and water heating and operation modes, achieves the purposes of waste heat recovery, multiple purposes of one machine, environmental protection and energy saving, and undoubtedly and effectively improves the energy utilization efficiency.

Drawings

FIG. 1 is a schematic diagram of one embodiment of the present invention.

Fig. 2 is a schematic diagram of another embodiment of the present invention.

Fig. 3 is a schematic view of a first waterway valve set according to an embodiment of the present invention.

FIG. 4 is a schematic view of a second waterway valve assembly according to an embodiment of the present invention.

FIG. 5 is a schematic view of a third waterway valve assembly according to an embodiment of the present invention.

FIG. 6 is a schematic view of a fourth waterway valve assembly according to an embodiment of the present invention.

FIG. 7 is a schematic view of a fifth waterway valve assembly according to an embodiment of the present invention.

Wherein; 1-a compressor; a 2-four-way reversing valve; 3-a compound water-cooled condenser; 4-shell and tube heat exchanger; 5-a finned heat exchanger; 6-a first one-way valve; 7-a second one-way valve; 8-a first solenoid valve; 9-a second solenoid valve; 10-a first throttle valve; 11-a second throttle valve; 12-a gas-liquid separator; 13-a cooling tower; 14-a cooling water pump; 15-a waterway one-way valve; 16-a first three-way valve; 17-a second three-way valve and 18-a waterway valve group; 19-a third throttle valve; 20-a hot water pump; 21-hot water three-way valve; 22-a first two-way valve, 23-a second two-way valve, 24-a third two-way valve, 25-a fourth two-way valve, 26-a fifth two-way valve, 27-a sixth two-way valve, 28-a seventh two-way valve and 29-an eighth two-way valve; 30-a third three-way valve; 32-third one-way valve.

Detailed Description

Reference will now be made in detail to embodiments of the present invention, examples of which are illustrated in the accompanying drawings, wherein like or similar reference numerals refer to the same or similar elements or elements having the same or similar function throughout. The embodiments described below with reference to the drawings are illustrative and intended to be illustrative of the invention and are not to be construed as limiting the invention.

In the description of the present invention, it is to be understood that the terms "first", "second" and the like are used for descriptive purposes only and are not to be construed as indicating or implying relative importance or implying any number of technical features indicated. Thus, a feature defined as "first" or "second" may explicitly or implicitly include one or more of that feature. In the description of the present invention, "a plurality" means two or more, for example, two, three, etc., unless specifically defined otherwise.

In the present invention, unless otherwise expressly specified or limited, the terms "connected," "communicating," and the like are to be construed broadly, e.g., as meaning fixedly connected, detachably connected, or integrally formed; can be mechanical connection and electrical connection; may be directly connected, or indirectly connected through an intermediate; there may be communication within two elements or an interaction of two elements unless otherwise expressly limited. The specific meanings of the above terms in the present invention can be understood by those skilled in the art according to specific situations.

In the present invention, unless otherwise expressly stated or limited, a first feature "above", "below" or "on" a second feature may be directly contacting the first and second features or indirectly contacting the first and second features through intervening media. Also, a first feature "on," "over," or "above" a second feature may be directly on or obliquely above the second feature, or simply indicate that the first feature is at a higher level than the second feature. A first feature may be "under," "beneath," or "beneath" a second feature, and the first and second features may be in direct contact, or the first and second features may be in indirect contact via an intermediate. Also, a first feature "under," "beneath," or "beneath" a second feature may be directly under or obliquely below the second feature, or simply mean that the first feature is at a lesser level than the second feature.

In the description herein, it is understood that the description of the terms "one embodiment" or "a particular embodiment," etc., is intended to mean 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. In this specification, the schematic representations of the terms used above are not necessarily intended to refer to the same embodiment or example. Furthermore, the particular features, structures, materials, or characteristics described may be combined in any suitable manner in any one or more embodiments or examples. Furthermore, various embodiments or examples and features of different embodiments or examples described in this specification can be combined and combined by one skilled in the art without contradiction.

As shown in fig. 1, in one aspect of the present invention, there is provided a dual cold source air source heat pump with total heat recovery, comprising a compressor 1 connected in a refrigeration cycle, the high-pressure outlet of the compressor 1 is connected with a connector d of a four-way reversing valve 2, a combined type water-cooled condenser 3 connected with a connector c of the four-way reversing valve 2, a finned heat exchanger 5 connected with a connector e of the four-way reversing valve 2, a gas-liquid separator 12 connected with a connector s of the four-way reversing valve 2, a first one-way valve 6 connected with an outlet of the combined type water-cooled condenser 3, a second one-way valve 7, a first electromagnetic valve 8 and a second electromagnetic valve 9 connected with an outlet of the first one-way valve 6, a first throttling valve 10 connected with an outlet of the first electromagnetic valve 8, a second throttling valve 11 connected with an outlet of the second electromagnetic valve 9 and a shell-and-tube heat exchanger 4 connected with an outlet of the second throttling valve 11; the outlet of the first throttle valve 10 is connected with the inlet of the second one-way valve 7 and the liquid side interface of the finned heat exchanger 5; the outlet of the gas-liquid separator 12 and the outlet of the shell-and-tube heat exchanger 4 and the suction port of the compressor 1 are connected to each other. In summer, water cooling is adopted for refrigeration, the condensation temperature can be reduced by about 14 ℃ compared with that of an air-cooled heat pump, the refrigerating capacity and the refrigerating efficiency of the unit can be obviously improved, low-pressure gas coming out of the shell-and-tube heat exchanger 4 directly enters the air suction port of the compressor, and the defects that the conventional air-cooled heat pump unit needs to flow through the four-way valve and the gas-liquid separator in sequence and then enters the air suction port of the compressor, the pressure drop of a low-pressure air suction side component and a pipeline is too large, and the refrigerating capacity and the refrigerating efficiency of the unit are reduced can be effectively overcome.

The double-cold-source air source heat pump with the total heat recovery function further comprises a first three-way valve 16 connected with a cooling water outlet of the combined type water-cooled condenser 3, a cooling tower 13 connected with a connector q of the first three-way valve 16, a cooling water pump 14 connected with a water outlet of the cooling tower 13, a waterway one-way valve 15 connected with an outlet of the cooling water pump 14, a hot water pump 20 connected with a process/sanitary hot water inlet of the combined type water-cooled condenser 3, and a second three-way valve 17 connected with a water inlet of the shell-and-tube heat exchanger 4; the port m of the first three-way valve 16 is connected with the water outlet of the shell-and-tube heat exchanger 4; and the interface i of the second three-way valve 17 is connected with a cooling water inlet of the connection composite water-cooled condenser 3 and a water outlet of the waterway one-way valve 15.

The upper part of the combined type water-cooled condenser 3 is provided with a total heat recovery heat exchange tube bundle, when in a hot water mode, a refrigerating and heating water mode and a heating and heating water mode, process/sanitary hot water at the inner side of a heat exchange tube absorbs heat discharged by a high-temperature and high-pressure gas refrigerant at the outer side of the heat exchange tube in the condensation process, and leaves the combined type water-cooled condenser 3 after the temperature rises and leads to the heat-requiring tail end of a user; the lower part is provided with a cooling water heat exchange tube bundle, and after absorbing the heat discharged by a high-temperature and high-pressure gas refrigerant outside the heat exchange tube in the condensation process in the cooling water refrigeration mode or the air-conditioning hot water heating mode or the heating water heating mode, the temperature rises and leaves the combined water-cooled condenser 3 to lead to the cooling tower in the cooling mode or the air-conditioning tail end heating mode or the heating water heating mode. The process/sanitary hot water loop at the inner side of the heat exchange tube of the total heat recovery heat exchange tube bundle and the cooling water loop at the inner side of the heat exchange tube of the cooling water heat exchange tube bundle are mutually independent, and the high-temperature high-pressure gas refrigerant entering the top of the composite water-cooled condenser 3 firstly flows through the total heat recovery heat exchange tube bundle and then flows through the cooling water heat exchange tube bundle, and is condensed into high-pressure liquid after the heat is discharged to the process/sanitary hot water or the cooling water.

The first three-way valve 16 and the second three-way valve 17 may be electrically operated valves or pneumatic valves, and may also be manually operated valves or other types of valves.

The double-cold-source air source heat pump with total heat recovery of the embodiment specifically works as follows:

in the refrigeration mode, the working states of all parts are as follows: the four-way reversing valve 2 and the first electromagnetic valve 8 are powered off, the second electromagnetic valve 9 is powered on, the interface p of the first three-way valve 16 is conducted with the interface q and is not conducted with the interface m, the interface h of the second three-way valve 17 is conducted with the interface j and is not conducted with the interface i, the cooling tower 13 and the cooling water pump 14 are in an operating state, the air-conditioning waterway in the shell-and-tube heat exchanger 4 is in an operating state, the fan of the finned heat exchanger 5 stops operating, the process/sanitary hot water waterway on the inner side of the full heat recovery heat exchange tube bundle heat exchange tube on the upper portion of the combined water-cooled condenser 3 is not operated, and the air-conditioning waterway in the shell-and-tube heat exchanger 4 is operated.

A refrigerant flow path: the compressor 1- > a connector d- > of the four-way reversing valve 2- > a connector c- > a composite water-cooled condenser 3- > a first one-way valve 6- > a second electromagnetic valve 9- > a second throttling valve 11- > a shell-and-tube heat exchanger 4- > the compressor 1.

The opening degree of the second throttle valve 11 is controlled according to the superheat degree of the gas-side outlet of the shell-and-tube heat exchanger 4, the suction superheat degree of the low-pressure inlet of the compressor 1, or the exhaust superheat degree of the high-pressure outlet of the compressor 1.

(II) a refrigeration and water heating mode, wherein the working states of all parts are as follows: the four-way reversing valve 2 and the first electromagnetic valve 8 are powered off, the second electromagnetic valve 9 is powered on, a connector p of a first three-way valve 16 is communicated with a connector q and is not communicated with a connector m, a connector h of a second three-way valve 17 is communicated with a connector j and is not communicated with a connector i, the cooling tower 13 and the cooling water pump 14 stop running, the process/sanitary hot water waterway at the inner side of the heat exchange tube of the total heat recovery heat exchange tube bundle at the upper part of the combined type water-cooled condenser 3 runs, the air-conditioning waterway in the shell-and-tube heat exchanger 4 is in a running state, the fan of the finned heat exchanger 5 stops running, and the air-conditioning waterway in the shell-and-tube heat exchanger 4 runs;

a refrigerant flow path: the compressor 1- > a connector d- > of the four-way reversing valve 2- > a connector c- > a composite water-cooled condenser 3- > a first one-way valve 6- > a second electromagnetic valve 9- > a second throttling valve 11- > a shell-and-tube heat exchanger 4- > the compressor 1.

The opening degree of the second throttle valve 11 is controlled according to the superheat degree of the gas-side outlet of the shell-and-tube heat exchanger 4, the suction superheat degree of the low-pressure inlet of the compressor 1, or the exhaust superheat degree of the high-pressure outlet of the compressor 1.

(III) heating mode, and working states of all parts: the four-way reversing valve 2 and the second electromagnetic valve 9 are powered off, the first electromagnetic valve 8 is powered on, a connector p of a first three-way valve 16 is communicated with a connector m but not communicated with a connector q, a connector j of a second three-way valve 17 is communicated with a connector i but not communicated with a connector h, the cooling tower 13 and the cooling water pump 14 stop running, the process/sanitary hot water waterway stops running, the fan of the finned heat exchanger 5 is in a running state, the hot water pump 20 stops running, and air-conditioning hot water enters the inner side of the heat exchange tube of the cooling water heat exchange tube bundle in the lower part of the combined water-cooled condenser 3.

A refrigerant flow path: the compressor 1- > a connector d- > of the four-way reversing valve 2- > a connector c- > a composite water-cooled condenser 3- > a first one-way valve 6- > a first electromagnetic valve 8- > a first throttling valve 10- > a fin type heat exchanger 5- > a connector e- > of the four-way reversing valve 2- > a connector s- > a gas-liquid separator 12- > the compressor 1.

The opening degree of the first throttle valve 10 is controlled according to the superheat degree of the outlet at the gas side of the finned heat exchanger 5, the suction superheat degree of the low-pressure inlet of the compressor 1 or the exhaust superheat degree of the high-pressure outlet of the compressor 1.

(IV) a hot water mode, and the working states of all parts: the four-way reversing valve 2 and the second electromagnetic valve 9 are powered off, the first electromagnetic valve 8 is powered on, the first three-way valve 16 and the second three-way valve 17 are kept in the state of the last refrigerating or heating operation, the cooling tower 13 and the cooling water pump 14 stop operating, the air-conditioning water channel in the shell-and-tube heat exchanger 4 stops operating, the process/sanitary hot water channel on the inner side of the total heat recovery heat exchange tube bundle heat exchange tube on the upper portion of the combined type water-cooled condenser 3 operates, and the fan of the fin-type heat exchanger 5 is in the operating state.

A refrigerant flow path: the compressor 1- > a connector d- > of the four-way reversing valve 2- > a connector c- > a composite water-cooled condenser 3- > a first one-way valve 6- > a first electromagnetic valve 8- > a first throttling valve 10- > a fin type heat exchanger 5- > a connector e- > of the four-way reversing valve 2- > a connector s- > a gas-liquid separator 12- > the compressor 1.

The opening degree of the first throttle valve 10 is controlled according to the superheat degree of the outlet at the gas side of the finned heat exchanger 5, the suction superheat degree of the low-pressure inlet of the compressor 1 or the exhaust superheat degree of the high-pressure outlet of the compressor 1.

(V) heating and water heating mode, and the working states of all the components are as follows: the four-way reversing valve 2 and the second electromagnetic valve 9 are powered off, the first electromagnetic valve 8 is powered on, the interface p of the first three-way valve 16 is communicated with the interface m, the interface p and the interface m are not communicated with the interface q, the interface j of the second three-way valve 17 is communicated with the interface i, the interface j and the interface i are not communicated with the interface h, the cooling tower 13 and the cooling water pump 14 stop running, and the fan of the finned heat exchanger 5 is in a running state. The process/sanitary hot water waterway and the air-conditioning hot water waterway can be operated simultaneously according to requirements, or only the process/sanitary hot water waterway is operated, or only the air-conditioning hot water waterway is operated. When the process/sanitary hot water is selected as an optimized heating object, the operation of the air-conditioning hot water waterway can be stopped firstly, the operation of the process/sanitary hot water waterway is stopped after the temperature of the process/sanitary hot water reaches a set value, and meanwhile, the air-conditioning hot water waterway is put into operation; when the air-conditioning hot water is selected as an optimized heating object, the process/sanitary hot water waterway can be stopped firstly, the air-conditioning hot water waterway stops running after the water temperature of the air-conditioning hot water reaches a set value, and the process/sanitary hot water waterway is put into operation; when the air-conditioning hot water waterway is put into operation, the air-conditioning hot water can be fed into the inner side of heat exchange tube of cooling water heat exchange tube bundle of lower portion of composite condenser 3.

A refrigerant flow path: the compressor 1- > a connector d- > of the four-way reversing valve 2- > a connector c- > a composite water-cooled condenser 3- > a first one-way valve 6- > a first electromagnetic valve 8- > a first throttling valve 10- > a fin type heat exchanger 5- > a connector e- > of the four-way reversing valve 2- > a connector s- > a gas-liquid separator 12- > the compressor 1.

As shown in fig. 2, another double-cold-source air source heat pump with total heat recovery provided by the present invention includes a compressor 1 connected in a refrigeration cycle loop, a high-pressure outlet of the compressor 1 is connected to a port d of a four-way reversing valve 2, a combined water-cooled condenser 3 connected to a port c of the four-way reversing valve 2, a finned heat exchanger 5 connected to a port e of the four-way reversing valve 2, a gas-liquid separator 12 connected to a port s of the four-way reversing valve 2, a first check valve 6 connected to an outlet of the combined water-cooled condenser 3, a second check valve 7 and a third throttle valve 19 connected to an outlet of the first check valve 6, a first electromagnetic valve 8 and a second electromagnetic valve 9 connected to an outlet of the third throttle valve 19, a third check valve 32 connected to an outlet of the first electromagnetic valve 8, and a shell-tube heat exchanger 4 connected to an outlet of the second electromagnetic valve 9; the outlet of the third one-way valve 32 is connected with the inlet of the second one-way valve 7 and the liquid side interface of the finned heat exchanger 5; the outlet of the gas-liquid separator 12 and the outlet of the shell-and-tube heat exchanger 4 and the suction port of the compressor 1 are connected to each other. In summer, water cooling is adopted for refrigeration, the condensation temperature can be reduced by about 14 ℃ compared with that of an air-cooled heat pump, the refrigerating capacity and the refrigerating efficiency of the unit can be obviously improved, low-pressure gas coming out of the shell-and-tube heat exchanger 4 directly enters the air suction port of the compressor, and the defects that the conventional air-cooled heat pump unit needs to flow through the four-way valve and the gas-liquid separator in sequence and then enters the air suction port of the compressor, the pressure drop of a low-pressure air suction side component and a pipeline is too large, and the refrigerating capacity and the refrigerating efficiency of the unit are reduced can be effectively overcome.

The double-cold-source air source heat pump with total heat recovery further comprises a first three-way valve 16 connected with a cooling water outlet of the combined type water-cooled condenser 3, a cooling tower 13 connected with a connector q of the first three-way valve 16, a cooling water pump 14 connected with a water outlet of the cooling tower 13, a first two-way valve 22 connected with an outlet of the cooling water pump 14, a hot water three-way valve 21 connected with a process/sanitary hot water inlet of the combined type water-cooled condenser 3, and a second three-way valve 17 connected with a water inlet of the shell-and-tube heat exchanger 4; the port m of the first three-way valve 16 is connected with the water outlet of the shell-and-tube heat exchanger 4; the interface i of the second three-way valve 17 is connected with a cooling water inlet of the composite water-cooled condenser 3 and a water outlet of the first two-way valve 22, and the interface o of the hot water three-way valve 21 is connected with a water outlet of the composite water-cooled condenser 3 for process/sanitary hot water.

The composite water-cooled condenser 3 is provided with a total heat recovery heat exchange tube bundle at the upper part, and when in a hot water mode, a refrigerating and heating water mode and a heating and heating water mode, process/sanitary hot water at the inner side of a heat exchange tube absorbs heat discharged by a high-temperature and high-pressure gas refrigerant at the outer side of the heat exchange tube in the condensation process, leaves the composite water-cooled condenser 3 after the temperature rises, and leads to the heat-required tail end of a user; the lower part is provided with a cooling water heat exchange tube bundle, the cooling water refrigeration mode, the air conditioning hot water heating mode or the heating water heating mode at the inner side of the heat exchange tube absorbs the heat discharged by the high-temperature high-pressure gas refrigerant at the outer side of the heat exchange tube in the condensation process, and the high-temperature high-pressure gas refrigerant leaves the composite water-cooled condenser 3 after the temperature rises and is led to the cooling tower refrigeration mode, the air conditioning tail end heating mode or the heating water heating mode. The process/sanitary hot water loop at the inner side of the heat exchange tube of the total heat recovery heat exchange tube bundle and the cooling water loop at the inner side of the heat exchange tube of the cooling water heat exchange tube bundle are mutually independent, and the high-temperature high-pressure gas refrigerant entering the top of the composite water-cooled condenser 3 firstly flows through the total heat recovery heat exchange tube bundle and then flows through the cooling water heat exchange tube bundle, and is condensed into high-pressure liquid after the heat is discharged to the process/sanitary hot water or the cooling water.

The double-cold-source air source heat pump with total heat recovery of the embodiment specifically works as follows:

in the refrigeration mode, the working states of all parts are as follows: the four-way reversing valve 2 and the first electromagnetic valve 8 are powered off, the second electromagnetic valve 9 is powered on, the interface p of the first three-way valve 16 is communicated with the interface q, the interface p and the interface q are not communicated with the interface m, the interface h of the second three-way valve 17 is communicated with the interface j, the interface h and the interface j are not communicated with the interface i, the cooling tower 13 and the cooling water pump 14 are in a running state, an air conditioner waterway in the shell and tube heat exchanger 4 runs, the fan of the fin type heat exchanger 5 stops running, and the interface n of the hot water three-way valve 21 is communicated with the interface o and is not communicated with the interface r.

A refrigerant flow path: the compressor 1- > an interface d- > of the four-way reversing valve 2- > an interface c- > of the four-way reversing valve 2- > the composite water-cooled condenser 3- > the first one-way valve 6- > the third throttle valve 19- > the second electromagnetic valve 9- > the shell-and-tube heat exchanger 4- > the compressor 1.

The opening degree of the third throttle valve 19 is controlled according to the superheat degree of the gas side outlet of the shell-and-tube heat exchanger 4, the suction superheat degree of the low-pressure inlet of the compressor 1, or the exhaust superheat degree of the high-pressure outlet of the compressor 1.

(II) a refrigeration and water heating mode, wherein the working states of all parts are as follows: the four-way reversing valve 2 and the first electromagnetic valve 8 are powered off, the second electromagnetic valve 9 is powered on, the interface p of the first three-way valve 16 is communicated with the interface q, the interface p and the interface q are not communicated with the interface m, the interface h of the second three-way valve 17 is communicated with the interface j, the interface h and the interface j are not communicated with the interface i, the cooling tower 13 and the cooling water pump 14 stop running, the interface n of the hot water three-way valve 21 is fully or partially communicated with the interface r, the fan of the fin type heat exchanger 5 stops running, and the air conditioner water path in the shell and tube type heat exchanger 4 runs.

A refrigerant flow path: the compressor 1- > an interface d- > of the four-way reversing valve 2- > an interface c- > of the four-way reversing valve 2- > the composite water-cooled condenser 3- > the first one-way valve 6- > the third throttle valve 19- > the second electromagnetic valve 9- > the shell-and-tube heat exchanger 4- > the compressor 1.

The opening degree of the third throttle valve 19 is controlled according to the superheat degree of the gas side outlet of the shell-and-tube heat exchanger 4, the suction superheat degree of the low-pressure inlet of the compressor 1, or the exhaust superheat degree of the high-pressure outlet of the compressor 1.

(III) heating mode, and working states of all parts: the four-way reversing valve 2 and the second electromagnetic valve 9 are powered off, the first electromagnetic valve 8 is powered on, a connector p of the first three-way valve 16 is conducted with a connector m and is not conducted with q, a connector j of the second three-way valve 17 is conducted with a connector i and is not conducted with h, the cooling tower 13 and the cooling water pump 14 stop running, a connector n of the hot water three-way valve 21 is conducted with a connector o and is not conducted with a connector r, the fan of the fin type heat exchanger 5 is in a running state, and air-conditioning hot water enters the inner side of a heat exchange tube of a cooling water heat exchange tube bundle in the lower portion of the combined type water-cooled condenser 3.

A refrigerant flow path: the compressor 1- > an interface d-of the four-way reversing valve 2- > an interface c-of the four-way reversing valve 2- > a shell-and-tube heat exchanger 4- > a first one-way valve 6- > a third throttle valve 19- > a first electromagnetic valve 8- > a third one-way valve 32- > a fin-type heat exchanger 5- > an interface e-of the four-way reversing valve 2- > an interface s-of the four-way reversing valve 2- > a gas-liquid separator 12- > the compressor 1.

And the opening degree of the third throttle valve 19 is controlled according to the superheat degree of the gas side outlet of the finned heat exchanger 5 or the suction superheat degree of the low-pressure inlet of the compressor 1 or the exhaust superheat degree of the high-pressure outlet of the compressor 1.

(IV) a hot water mode, and the working states of all parts: the four-way reversing valve 2 and the second electromagnetic valve 9 are powered off, the first electromagnetic valve 8 is powered on, the first three-way valve 16 and the second three-way valve 17 are kept in the state of the last refrigerating or heating operation, the cooling tower 13 and the cooling water pump 14 stop operating, the air-conditioning water channel in the shell-and-tube heat exchanger 4 stops operating, the interface n of the hot water three-way valve 21 is completely or mostly communicated with the interface r, and the fan of the finned heat exchanger 5 is in the operating state.

A refrigerant flow path: the compressor 1- > an interface d-of the four-way reversing valve 2- > an interface c-of the four-way reversing valve 2- > a shell-and-tube heat exchanger 4- > a first one-way valve 6- > a third throttle valve 19- > a first electromagnetic valve 8- > a third one-way valve 32- > a fin-type heat exchanger 5- > an interface e-of the four-way reversing valve 2- > an interface s-of the four-way reversing valve 2- > a gas-liquid separator 12- > the compressor 1.

(V) heating and water heating mode, and the working states of all the components are as follows: the four-way reversing valve 2 and the second electromagnetic valve 9 are powered off, the first electromagnetic valve 8 is powered on, the interface p of the first three-way valve 16 is communicated with the interface m, the interface p and the interface m are not communicated with the interface q, the interface j of the second three-way valve 17 is communicated with the interface i, the interface j and the interface i are not communicated with the interface h, the cooling tower 13 and the cooling water pump 14 stop running, and the fan of the finned heat exchanger 5 is in a running state. The process/sanitary hot water waterway and the air-conditioning hot water waterway can be operated simultaneously according to requirements, or only the process/sanitary hot water waterway is operated, or only the air-conditioning hot water waterway is operated. When the process/sanitary hot water is selected as an optimized heating object, the operation of the air-conditioning hot water waterway can be stopped firstly, the operation of the process/sanitary hot water waterway is stopped after the temperature of the process/sanitary hot water reaches a set value, and meanwhile, the air-conditioning hot water waterway is put into operation; when the air-conditioning hot water is selected as an optimized heating object, the process/sanitary hot water waterway can be stopped firstly, the air-conditioning hot water waterway stops running after the water temperature of the air-conditioning hot water reaches a set value, and the process/sanitary hot water waterway is put into operation; when the air-conditioning hot water waterway is put into operation, the air-conditioning hot water can be fed into the inner side of heat exchange tube of cooling water heat exchange tube bundle of lower portion of composite condenser 3.

A refrigerant flow path: the compressor 1- > an interface d of the four-way reversing valve 2- > an interface c of the four-way reversing valve 2- > the composite water-cooled condenser 3- > the first one-way valve 6- > the third throttle valve 19- > the first electromagnetic valve 8- > the third one-way valve 32- > the fin-type heat exchanger 5- > an interface e of the four-way reversing valve 2- > an interface s of the four-way reversing valve 2- > the gas-liquid separator 12- > the compressor 1.

And the opening degree of the third throttle valve 19 is controlled according to the superheat degree of the gas side outlet of the finned heat exchanger 5 or the suction superheat degree of the low-pressure inlet of the compressor 1 or the exhaust superheat degree of the high-pressure outlet of the compressor 1.

As shown in fig. 3-7, in another aspect of the present invention, five changes of the waterway valve set are proposed.

Firstly, a second two-way valve 23 and a third two-way valve 24 are used in the waterway valve group 18 to replace the first three-way valve 16, when water is heated for refrigeration or refrigeration, a port j of the second three-way valve 17 is communicated with a port h but not communicated with a port i, the second two-way valve 23 is opened, and the third two-way valve 24 is closed; when heating or heating and heating water, the interface j of the second three-way valve 17 is communicated with the interface i but not communicated with the interface h, the third two-way valve 24 is opened, and the second two-way valve 23 is closed.

Secondly, the fourth two-way valve 25 and the fifth two-way valve 26 are used in the water path valve group 18 to replace the second three-way valve 17, when water is heated for refrigeration or refrigeration, the interface p of the first three-way valve 16 is communicated with the interface q but not communicated with the interface m, the fifth two-way valve 26 is opened, and the fourth two-way valve 25 is closed; when heating or heating and heating water, the port p of the first three-way valve 16 is communicated with the port m but not communicated with the port q, the fourth two-way valve 25 is opened, and the fifth two-way valve 26 is closed.

Thirdly, the second two-way valve 23 and the third two-way valve 24 are used for replacing the first three-way valve 16, the fourth two-way valve 25 and the fifth two-way valve 26 are used for replacing the second three-way valve 17, when the water is heated for cooling or cooling, the second two-way valve 23 and the fifth two-way valve 26 are opened, and the third two-way valve 24 and the fourth two-way valve 25 are closed; when water is heated, the second two-way valve 23 and the fifth two-way valve 26 are closed, and the third two-way valve 24 and the fourth two-way valve 25 are opened.

Fourthly, the second two-way valve 23 and the third two-way valve 24 are used in the water channel valve group 18 to replace the first three-way valve 16, the sixth two-way valve 27, the seventh two-way valve 28 and the eighth two-way valve 29 are used to replace the second three-way valve 17, when the water is heated for cooling or cooling, the second two-way valve 23 and the seventh two-way valve 28 are opened, and the third two-way valve 24, the sixth two-way valve 27 and the eighth two-way valve 29 are closed; when water is heated, the second two-way valve 23 and the seventh two-way valve 28 are closed, the third two-way valve 24 and the sixth two-way valve 27 are opened, and the eighth two-way valve 29 is opened or closed as needed.

Fifthly, in the water path valve group 18, the first three-way valve 16 is replaced by the second two-way valve 23 and the third two-way valve 24, the second three-way valve 17 is replaced by the eighth two-way valve 29 and the third three-way valve 30, when the water is heated for refrigeration or refrigeration, the second two-way valve 23 is opened, the third two-way valve 24 and the eighth two-way valve 29 are closed, and the interface x of the third three-way valve 30 is communicated with the interface y but not communicated with the interface z; when heating or heating water, the second two-way valve 23 is closed, the third two-way valve 24 is opened, the interface x of the third three-way valve 30 is communicated with the interface z but not communicated with the interface y, and the eighth two-way valve 29 can be opened or closed as required.

While embodiments of the present invention have been shown and described above, it should be understood that the above embodiments are exemplary and should not be taken as limiting the invention. Various changes and modifications may be made to the invention without departing from the spirit and scope of the invention, and such changes and modifications are intended to be within the scope of the invention as claimed.