CN102393054B - Air-conditioning water heating system - Google Patents
Air-conditioning water heating system Download PDFInfo
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- CN102393054B CN102393054B CN 201110382258 CN201110382258A CN102393054B CN 102393054 B CN102393054 B CN 102393054B CN 201110382258 CN201110382258 CN 201110382258 CN 201110382258 A CN201110382258 A CN 201110382258A CN 102393054 B CN102393054 B CN 102393054B
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 174
- 238000010438 heat treatment Methods 0.000 title claims abstract description 47
- 238000004378 air conditioning Methods 0.000 title claims abstract description 41
- 238000011084 recovery Methods 0.000 claims abstract description 58
- 239000002918 waste heat Substances 0.000 claims abstract description 50
- 238000004146 energy storage Methods 0.000 claims abstract description 48
- 235000020679 tap water Nutrition 0.000 claims abstract description 6
- -1 Alpaka Chemical compound 0.000 claims description 9
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 9
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims description 9
- 239000004411 aluminium Substances 0.000 claims description 9
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 9
- 229910052782 aluminium Inorganic materials 0.000 claims description 9
- 238000002485 combustion reaction Methods 0.000 claims description 9
- 239000010949 copper Substances 0.000 claims description 9
- 229910052802 copper Inorganic materials 0.000 claims description 9
- 239000007789 gas Substances 0.000 claims description 9
- 229910001220 stainless steel Inorganic materials 0.000 claims description 9
- 239000010935 stainless steel Substances 0.000 claims description 9
- 239000010936 titanium Substances 0.000 claims description 9
- 229910052719 titanium Inorganic materials 0.000 claims description 9
- 239000002351 wastewater Substances 0.000 abstract description 22
- 239000008399 tap water Substances 0.000 abstract description 4
- 238000001816 cooling Methods 0.000 abstract 1
- 238000007599 discharging Methods 0.000 abstract 1
- 238000005265 energy consumption Methods 0.000 abstract 1
- 239000003570 air Substances 0.000 description 31
- 238000009833 condensation Methods 0.000 description 24
- 230000005494 condensation Effects 0.000 description 24
- 238000005057 refrigeration Methods 0.000 description 12
- 238000000034 method Methods 0.000 description 8
- 238000003303 reheating Methods 0.000 description 7
- 230000015572 biosynthetic process Effects 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 238000001704 evaporation Methods 0.000 description 4
- 230000008020 evaporation Effects 0.000 description 4
- 239000012080 ambient air Substances 0.000 description 2
- 238000000605 extraction Methods 0.000 description 2
- 230000008676 import Effects 0.000 description 2
- 238000007872 degassing Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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Abstract
The invention relates to an air-conditioning water heating system, which is characterized by comprising a compressor (1), a water-storage condenser (2), a first change-over valve (3), a first throttling valve (4), an energy-storage type waste heat recovery exchanger (5), an evaporator (7), an air-cooled condenser (8), a second throttling valve (9), a second change-over valve (10), a water heat exchanger (6) and a shower device. The air-conditioning water heating system adopts a multi-function design, and can provide air cooling and discharging functions while producing hot water; and the air-conditioning water heating system carries out first heat recovery by using the temperature difference between waste water and tap water, and then heats a heat-pump water heater for heating hot water by taking the waste water as a heat source, therefore, both the advantages such as high efficiency and stability of the heat-pump water heater are achieved, and the energy consumption for heating hot water can be reduced as far as possible by using the temperature difference between the waste water and tap water.
Description
Affiliated technical field
The present invention relates to a kind of air conditioning and water heating system, specifically be a kind of used heat that takes full advantage of waste water after the shower, the energy that absorbs can be stored to Teat pump boiler start next time provides heat, the air conditioning and water heating system of cold air function can be provided again.
Background technology
Teat pump boiler is the device that comes heat hot water from water or air the inside draw heat, and its advantage is: system is simple, stable, the thermal efficiency is high.At present the air conditioning and water heating system of the employing Teat pump boiler commonly used heat energy that relies on consumed power to produce fully provide life with hot water or the related cold air function that provides, energy resource consumption is big, use cost is higher; And most shower rooms, the waste water after the shower all is directly to emit, and contained heat also together slatterns in these waste water, is not fully used, and causes the waste of the energy.
Summary of the invention
The technical problem to be solved in the present invention provides a kind of used heat that takes full advantage of waste water after the shower, the energy that absorbs can be stored to Teat pump boiler start next time provides heat, and the air conditioning and water heating system of cold air function can be provided again.
The technical problem to be solved in the present invention, can realize by following technical scheme: a kind of air conditioning and water heating system is characterized in that: comprise compressor 1, storage-type condenser 2, energy storage type Waste Heat Recovery interchanger 5, evaporimeter 7, air cooled condenser 8, water heat exchanger 6 and shower bath; The outlet of wherein said compressor 1 is communicated with the air inlet of storage-type condenser 2; The gas outlet of described storage-type condenser 2 is communicated with the entrance of first switching valve 3, one of them outlet of this first switching valve 3 is communicated with the entrance of energy storage type Waste Heat Recovery interchanger 5, another outlet of this first switching valve 3 is communicated with the entrance of first throttle valve 4, and the outlet of described first throttle valve 4 is communicated with the entrance of energy storage type Waste Heat Recovery interchanger 5; The outlet of described energy storage type Waste Heat Recovery interchanger 5 is communicated with the entrance of second switching valve 10, one of them outlet of this second switching valve 10 is communicated with the entrance of compressor 1, another outlet of this second switching valve 10 is communicated with the entrance of air cooled condenser 8, the outlet of described air cooled condenser 8 is communicated with the entrance of second choke valve 9, the outlet of described second choke valve 9 is communicated with the entrance of evaporimeter 7, and the outlet of described evaporimeter 7 is communicated with the entrance of compressor 1; The entrance of described shower bath is communicated with the delivery port of described storage-type condenser 2, described water heat exchanger 6 is arranged on the top of described energy storage type Waste Heat Recovery interchanger 5, and the outlet of described water heat exchanger 6 is communicated with the water inlet of storage-type condenser 2 or the outlet of described water heat exchanger 6 is communicated with the water inlet of storage-type condenser 2 and the entrance of shower bath simultaneously.
Compressor 1 among the present invention, storage-type condenser 2, choke valve 4 and energy storage type Waste Heat Recovery interchanger 5 are communicated with the formation first cover refrigeration system; Compressor 1, storage-type condenser 2, energy storage type Waste Heat Recovery interchanger 5, air cooled condenser 8, expansion valve 9, evaporimeter 7 are communicated with the formation second cover refrigeration system simultaneously.When using air conditioning and water heating system provided by the invention, at first running water pipe 13 is communicated with the import of water heat exchangers 6.The shower heat recovery function of this air conditioning and water heating system at first running water pipe through the water inlet of the storage-type condenser 2 that is communicated with this water heater behind the water heat exchanger 6 respectively or be communicated with the water inlet of storage-type condenser 2 simultaneously and the entrance of shower bath.The water heat exchanger 6 of the baffle plate that catchments is arranged, in order to the Waste Water Centralized after the shower is discharged in can selecting behind a place.
When selecting this air conditioning and water heating system in shower, to be with the function of cold air, at first adjust first switching valve 3, second switching valve 10, make the gas outlet of storage-type condenser 2 directly be communicated with the entrance of energy storage type Waste Heat Recovery interchanger 5, the outlet of energy storage type Waste Heat Recovery interchanger is communicated with air cooled condenser 8, and this moment, second refrigeration system of this air conditioning and water heating system was communicated with.During this second refrigeration system operation, at first compressor operating is carried out first order condensation by storage-type condenser 2, in condensation the water in the storage tank of storage-type condenser 2 is heated to suitable temperature hot water for shower bath is provided, and is generally 55 ℃; When first order condensation can't be satisfied condensation effect when the hot water temperature is higher, carry out second level condensation by energy storage type Waste Heat Recovery interchanger 5, the energy storage type Waste Heat Recovery interchanger 5 of this moment is condenser functions, when the water of energy storage type Waste Heat Recovery interchanger inside also is heated can't satisfy condensation and require the time, carry out third level condensations by air cooled condenser 8 again, guarantee the condensation effect of whole process of refrigerastion by the condensation that divides three grades.Working medium is evaporated in evaporimeter by 10 throttlings of second choke valve after the condensation, and cold air is provided in evaporation process.
When selecting the pure shower function of this air conditioning and water heating system, at first adjust first switching valve 3, second switching valve 10, make the gas outlet of storage-type condenser 2 through the entrance of choke valve 4 connection energy storage type Waste Heat Recovery interchangers 5, the outlet of energy storage type Waste Heat Recovery interchanger 5 directly is communicated with the entrance of compressor 1, and this moment, first refrigeration system of this air conditioning and water heating system was communicated with.During this first refrigeration system operation, at first compressor operating by the storage-type condenser condenses, is heated to suitable temperature with the water in the storage tank in condensation, is generally 55 ℃ hot water for shower bath is provided; In the inner evaporation of energy storage type Waste Heat Recovery interchanger, the energy storage type Waste Heat Recovery exchange of this moment is evaporator function to working medium by the expansion valve throttling after the condensation.
In above-mentioned two kinds of operating positions, energy storage type Waste Heat Recovery interchanger 5 and the water heat exchanger 6 of this air conditioning and water heating system all carry out the shower heat recovery function.After opening shower bath, compressor operating, originally 55 ℃ hot water becomes and is about 40 ℃ waste water after shower, these waste water through shower bath at first be sprayed onto on the water heat exchanger 6 with water heat exchanger in 10-15 ℃ of running water carry out heat exchange, first amount of reheating that at this moment realizes reclaims.Running water is promoted to 20-25 ℃ or higher temperature by 10-15 ℃ after water heat exchanger reclaims heat, waste water drops to 25-30 ℃ or lower by 40 ℃.When the outlet of water heat exchanger 6 only was communicated with the water inlet of storage-type condenser 2, the running water after first amount of reheating reclaims all entered and carries out further heat exchange in the storage-type condenser 2; When the outlet of water heat exchanger 6 is communicated with the entrance of the water inlet of storage-type condenser 2 and shower bath simultaneously, in the running water after first amount of reheating reclaims, a part enters condenser and carries out further heat exchange, another part then directly enters shower bath, and two parts running water mixes the temperature that reaches suitable in shower bath.
The second heavy Waste Heat Recovery is finished by evaporimeter, evaporimeter and waste water carry out heat exchange, make waste water by 25-30 ℃ of cold water that freezes to about 5-10 ℃, in this process, cold-producing medium in the evaporimeter has absorbed more than 20 heats of spending, and absorbed heat is promoted to condenser by compressor, and the running water and the condenser that wherein promote after the temperature carry out heat exchange, reach the purpose that running water is heated into hot water, and then gush out from shower bath.Add in the whole process of hot tap-water the first heavy heat recovery and be to be finished by heat transfer naturally and do not need to consume any energy, second amount of reheating reclaims by compressor the heat that absorbs is promoted to the running water heating, and the electric energy that consumes when compressor promotes is second to return and receive about 1/3 of energy.And after shower finished, about 5-10 ℃ cold water in the evaporimeter can be by absorbing the heat of ambient air around the interchanger, and heat stored to task down heat is provided.
On the basis of the above, air cooled condenser 8 of the present invention and/or evaporimeter 7 are respectively equipped with and are communicated with extraneous blower fan; When using band cold air function of the present invention, the blower fan on air cooled condenser 8 and/or the evaporimeter 7 is connected to indoor gas extraction system and finishes the indoor exhaust function, to accelerate the circulation of room air.
On the basis of the above, shower bath of the present invention comprises switch 12 and shower gondola water faucet 11, and the entrance of described switch 12 is connected with the outlet of water heat exchanger 6 and the delivery port of storage-type condenser 2; The outlet of switch 12 is connected with shower gondola water faucet 11; Described shower gondola water faucet 11 is positioned at the top of water heat exchanger 6 and energy storage type Waste Heat Recovery interchanger 5.The switch 12 of described shower bath is hot and cold combustion taps or hot water tap; The water inlet of hot water of described hot and cold combustion taps, cold water inlet are communicated with the outlet of delivery port and the water interchanger 6 of storage-type condenser 2 respectively, and the delivery port of described hot and cold combustion taps is communicated with shower gondola water faucet 11; Described hot water tap's water inlet is communicated with the outlet of delivery port and the water interchanger 6 of storage-type condenser 2 respectively, and described hot water tap's delivery port is communicated with shower gondola water faucet 11.
Described compressor 1 is scroll compressor, rotor-type compressor or reciprocating compressor.
Described storage-type condenser 2 is heat-exchangers of the plate type, tube-in-tube heat exchanger or tube coil type heat exchanger; Described storage-type condenser 2 is made by stainless steel, red copper, Alpaka, aluminium or titanium, and it can also adopt other heat-transfer matcrial to make.
Described energy storage type Waste Heat Recovery interchanger 5 is tube coil type heat exchanger, tubular heat exchanger, honeycomb fashion heat exchanger or tube-in-tube heat exchanger; Described energy storage type Waste Heat Recovery interchanger is made by stainless steel, red copper, Alpaka, aluminium or titanium, and it can also adopt other heat-transfer matcrial to make.
Described water heat exchanger 6 is tubing heat exchanger or heat-exchangers of the plate type; Described hydro-thermal heat exchanger 6 is made by stainless steel, red copper, Alpaka, aluminium or titanium, and it can also adopt other heat-transfer matcrial to make.
Described first switching valve 3 and/or second switching valve 10 are triple valve, magnetic valve or the commutation function valve are arranged.
Described first throttle valve 4 and/or second choke valve 9 are expansion valve or capillary; Described expansion valve 3 is heating power expansion valve or electric expansion valve; Because the expansion valve adjustable extent is bigger, and capillary can not be regulated because its internal diameter is constant, so the preferred expansion valve of choke valve of the present invention, to regulate according to actual conditions neatly.
Described air cooled condenser 8 is finned type heat exchanger, heat-exchangers of the plate type, shell-and-tube exchanger, honeycomb fashion heat exchanger, tube-in-tube heat exchanger or tube coil type heat exchanger.
Described evaporimeter 7 is finned type heat exchanger, heat-exchangers of the plate type, shell-and-tube exchanger, tube-in-tube heat exchanger or tube coil type heat exchanger.
Compared with prior art, the present invention at first is multi-functional design, in the time of its heat production water, can provide cold air and degassing function; And the temperature difference of utilizing waste water and running water is carried out the recovery of first amount of reheating, recycling waste water comes the Teat pump boiler of heat hot water as thermal source, efficient, the stable advantage of Teat pump boiler can be brought into play, but also the energy resource consumption of the temperature difference minimizing heat hot water between waste water and running water can be utilized as far as possible.
Description of drawings
Fig. 1 is structural representation of the present invention.
The specific embodiment
Air conditioning and water heating system as shown in Figure 1 is embodiments of the invention, and it has comprised compressor 1, storage-type condenser 2, energy storage type Waste Heat Recovery interchanger 5, evaporimeter 7, air cooled condenser 8, water heat exchanger 6 and shower bath.Wherein, air cooled condenser 8 and evaporimeter 7 are respectively equipped with and are communicated with extraneous blower fan.
The outlet of compressor 1 is communicated with the air inlet of storage-type condenser 2; The gas outlet of storage-type condenser 2 is communicated with the entrance of first switching valve 3, one of them outlet of this first switching valve 3 is communicated with the entrance of energy storage type Waste Heat Recovery interchanger 5, another outlet of this first switching valve 3 is communicated with the entrance of first throttle valve 4, and the outlet of first throttle valve 4 is communicated with the entrance of energy storage type Waste Heat Recovery interchanger 5; The outlet outlet of energy storage type Waste Heat Recovery interchanger 5 is communicated with the entrance of second switching valve 10, one of them outlet of this second switching valve 10 is communicated with the entrance of compressor 1, another outlet of this second switching valve 10 is communicated with the entrance of air cooled condenser 8, the outlet of air cooled condenser 8 is communicated with the entrance of second choke valve 9, the outlet of second choke valve 9 is communicated with the entrance of evaporimeter 7, and the outlet of evaporimeter 7 is communicated with the entrance of compressor 1.Wherein compressor 1, storage-type condenser 2, choke valve 4 and energy storage type Waste Heat Recovery interchanger 5 are communicated with the formation first cover refrigeration system; Compressor 1, storage-type condenser 2, energy storage type Waste Heat Recovery interchanger 5, air cooled condenser 8, expansion valve 9, evaporimeter 7 are communicated with the formation second cover refrigeration system simultaneously.
Shower bath comprises hot and cold combustion taps 12 and the shower gondola water faucet 11 as switch, the water inlet of hot water of hot and cold combustion taps 12, cold water inlet are communicated with the outlet of delivery port and the water interchanger 6 of storage-type condenser 2 respectively, the outlet of water heat exchanger 6 also is communicated with the water inlet of storage-type condenser 2, and the delivery port of hot and cold combustion taps is communicated with shower gondola water faucet 11; Water heat exchanger 6 be arranged on energy storage type Waste Heat Recovery interchanger 5 directly over, and shower gondola water faucet 11 be positioned at water heat exchanger 6 directly over.
Compressor 1 wherein is scroll compressor, rotor-type compressor or reciprocating compressor; Storage-type condenser 2 is heat-exchangers of the plate type, tube-in-tube heat exchanger or tube coil type heat exchanger; Storage-type condenser 2 is made by stainless steel, red copper, Alpaka, aluminium or titanium; Energy storage type Waste Heat Recovery interchanger 5 is tube coil type heat exchanger, tubular heat exchanger, honeycomb fashion heat exchanger or tube-in-tube heat exchanger; Energy storage type Waste Heat Recovery interchanger is made by stainless steel, red copper, Alpaka, aluminium or titanium, and it can also adopt other heat-transfer matcrial to make water heat exchanger 6 is tubing heat exchanger or heat-exchangers of the plate type; Hydro-thermal heat exchanger 6 is by stainless steel, red copper, Alpaka, aluminium or titanium make first switching valve 3 and second switching valve 10 is triple valves, magnetic valve or commutation function valve first throttle valve 4 is arranged and second choke valve 9 is finned type heat exchangers for expansion valve or capillary air cooled condenser 8, heat-exchangers of the plate type, shell-and-tube exchanger, the honeycomb fashion heat exchanger, tube-in-tube heat exchanger or tube coil type heat exchanger evaporimeter 7 are finned type heat exchangers, heat-exchangers of the plate type, shell-and-tube exchanger, tube-in-tube heat exchanger or tube coil type heat exchanger.
When using air conditioning and water heating system provided by the invention, at first running water pipe 13 is communicated with the import of water heat exchangers 6.The shower heat recovery function of this air conditioning and water heating system at first running water pipe through the water inlet of the storage-type condenser 2 that is communicated with this water heater behind the water heat exchanger 6 respectively or be communicated with the water inlet of storage-type condenser 2 simultaneously and the entrance of shower bath.The water heat exchanger 6 of the baffle plate that catchments is arranged, in order to the Waste Water Centralized after the shower is discharged in can selecting behind a place.
When selecting this air conditioning and water heating system in shower, to be with the function of cold air, at first adjust first switching valve 3, second switching valve 10, make the gas outlet of storage-type condenser 2 directly be communicated with the entrance of energy storage type Waste Heat Recovery interchanger 5, the outlet of energy storage type Waste Heat Recovery interchanger is communicated with air cooled condenser 8, and this moment, second refrigeration system of this air conditioning and water heating system was communicated with.During this second refrigeration system operation, at first compressor operating is carried out first order condensation by storage-type condenser 2, in condensation the water in the storage tank of storage-type condenser 2 is heated to suitable temperature hot water for shower bath is provided, and is generally 55 ℃; When first order condensation can't be satisfied condensation effect when the hot water temperature is higher, carry out second level condensation by energy storage type Waste Heat Recovery interchanger 5, the energy storage type Waste Heat Recovery interchanger 5 of this moment is condenser functions, when the water of energy storage type Waste Heat Recovery interchanger inside also is heated can't satisfy condensation and require the time, carry out third level condensations by air cooled condenser 8 again, guarantee the condensation effect of whole process of refrigerastion by the condensation that divides three grades.Working medium is evaporated in evaporimeter by 10 throttlings of second choke valve after the condensation, and cold air is provided in evaporation process; And being connected to indoor gas extraction system, the blower fan on air cooled condenser 8 and the evaporimeter 7 finishes the indoor exhaust function.
When selecting the pure shower function of this air conditioning and water heating system, at first adjust first switching valve 3, second switching valve 10, make the gas outlet of storage-type condenser 2 through the entrance of choke valve 4 connection energy storage type Waste Heat Recovery interchangers 5, the outlet of energy storage type Waste Heat Recovery interchanger 5 directly is communicated with the entrance of compressor 1, and this moment, first refrigeration system of this air conditioning and water heating system was communicated with.During this first refrigeration system operation, at first compressor operating by the storage-type condenser condenses, is heated to suitable temperature with the water in the storage tank in condensation, is generally 55 ℃ hot water for shower bath is provided; In the inner evaporation of energy storage type Waste Heat Recovery interchanger, the energy storage type Waste Heat Recovery exchange of this moment is evaporator function to working medium by the expansion valve throttling after the condensation.
In above-mentioned two kinds of operating positions, energy storage type Waste Heat Recovery interchanger 5 and the water heat exchanger 6 of this air conditioning and water heating system all carry out the shower heat recovery function.After opening shower bath, compressor operating, originally 55 ℃ hot water becomes and is about 40 ℃ waste water after shower, these waste water through shower bath at first be sprayed onto on the water heat exchanger 6 with water heat exchanger in 10-15 ℃ of running water carry out heat exchange, first amount of reheating that at this moment realizes reclaims.Running water is promoted to 20-25 ℃ or higher temperature by 10-15 ℃ after water heat exchanger reclaims heat, waste water drops to 25-30 ℃ or lower by 40 ℃.The second heavy Waste Heat Recovery is finished by evaporimeter, evaporimeter and waste water carry out heat exchange, make waste water by 25-30 ℃ of cold water that freezes to about 5-10 ℃, in this process, cold-producing medium in the evaporimeter has absorbed more than 20 heats of spending, and absorbed heat is promoted to condenser by compressor, and the running water and the condenser that wherein promote after the temperature carry out heat exchange, reach the purpose that running water is heated into hot water, and then gush out from shower bath.Add in the whole process of hot tap-water the first heavy heat recovery and be to be finished by heat transfer naturally and do not need to consume any energy, second amount of reheating reclaims by compressor the heat that absorbs is promoted to the running water heating, and the electric energy that consumes when compressor promotes is second to return and receive about 1/3 of energy.And after shower finished, about 5-10 ℃ cold water in the evaporimeter can be by absorbing the heat of ambient air around the interchanger, and heat stored to task down heat is provided.
Claims (16)
1. an air conditioning and water heating system is characterized in that: comprise compressor (1), storage-type condenser (2), energy storage type Waste Heat Recovery interchanger (5), evaporimeter (7), air cooled condenser (8), water heat exchanger (6) and shower bath; The outlet of wherein said compressor (1) is communicated with the air inlet of storage-type condenser (2); The gas outlet of described storage-type condenser (2) is communicated with the entrance of first switching valve (3), one of them outlet of this first switching valve (3) is communicated with the entrance of energy storage type Waste Heat Recovery interchanger (5), another outlet of this first switching valve (3) is communicated with the entrance of first throttle valve (4), and the outlet of described first throttle valve (4) is communicated with the entrance of energy storage type Waste Heat Recovery interchanger (5); The outlet of described energy storage type Waste Heat Recovery interchanger (5) is communicated with the entrance of second switching valve (10), one of them outlet of this second switching valve (10) is communicated with the entrance of compressor (1), another outlet of this second switching valve (10) is communicated with the entrance of air cooled condenser (8), the outlet of described air cooled condenser (8) is communicated with the entrance of second choke valve (9), the outlet of described second choke valve (9) is communicated with the entrance of evaporimeter (7), and the outlet of described evaporimeter (7) is communicated with the entrance of compressor (1); The entrance of described shower bath is communicated with the delivery port of described storage-type condenser (2), described water heat exchanger (6) is arranged on the top of described energy storage type Waste Heat Recovery interchanger (5), and the outlet of described water heat exchanger (6) is communicated with the water inlet of storage-type condenser (2) or the outlet of described water heat exchanger (6) is communicated with the water inlet of storage-type condenser (2) and the entrance of shower bath simultaneously.
2. air conditioning and water heating system according to claim 1 is characterized in that: described air cooled condenser (8) and/or evaporimeter (7) are respectively equipped with and are communicated with extraneous blower fan.
3. air conditioning and water heating system according to claim 2, it is characterized in that: described shower bath comprises switch (12) and shower gondola water faucet (11), and the entrance of described switch (12) is connected with the outlet of water heat exchanger (6) and the delivery port of storage-type condenser (2); The outlet of switch (12) is connected with shower gondola water faucet (11); Described shower gondola water faucet (11) is positioned at the top of water heat exchanger (6) and energy storage type Waste Heat Recovery interchanger (5).
4. air conditioning and water heating system according to claim 3 is characterized in that: the switch of described shower bath (12) is hot and cold combustion taps or hot water tap; The water inlet of hot water of described hot and cold combustion taps, cold water inlet are communicated with the outlet of delivery port and the water heat exchanger (6) of storage-type condenser (2) respectively, and the delivery port of described hot and cold combustion taps is communicated with shower gondola water faucet (11); Described hot water tap's water inlet is communicated with the outlet of delivery port and the water heat exchanger (6) of storage-type condenser (2) respectively, and described hot water tap's delivery port is communicated with shower gondola water faucet (11).
5. air conditioning and water heating system according to claim 4, it is characterized in that: described compressor (1) is scroll compressor, rotor-type compressor or reciprocating compressor.
6. air conditioning and water heating system according to claim 5, it is characterized in that: described storage-type condenser (2) is heat-exchangers of the plate type, tube-in-tube heat exchanger or tube coil type heat exchanger.
7. air conditioning and water heating system according to claim 6, it is characterized in that: described storage-type condenser (2) is made by stainless steel, red copper, Alpaka, aluminium or titanium.
8. air conditioning and water heating system according to claim 7 is characterized in that: described energy storage type Waste Heat Recovery interchanger (5) is tube coil type heat exchanger, tubular heat exchanger, honeycomb fashion heat exchanger or tube-in-tube heat exchanger.
9. air conditioning and water heating system according to claim 8, it is characterized in that: described energy storage type Waste Heat Recovery interchanger is made by stainless steel, red copper, Alpaka, aluminium or titanium.
10. air conditioning and water heating system according to claim 9, it is characterized in that: described water heat exchanger (6) is tubing heat exchanger or heat-exchangers of the plate type.
11. air conditioning and water heating system according to claim 10 is characterized in that: described water heat exchanger (6) is made by stainless steel, red copper, Alpaka, aluminium or titanium.
12. air conditioning and water heating system according to claim 11 is characterized in that: described first switching valve (3) and/or second switching valve (10) are triple valve or magnetic valve.
13. air conditioning and water heating system according to claim 12 is characterized in that: described first throttle valve (4) and/or second choke valve (9) are expansion valve or capillary.
14. air conditioning and water heating system according to claim 13 is characterized in that: described expansion valve (3) is heating power expansion valve or electric expansion valve.
15. air conditioning and water heating system according to claim 14 is characterized in that: described air cooled condenser (8) is finned type heat exchanger, heat-exchangers of the plate type, shell-and-tube exchanger, honeycomb fashion heat exchanger, tube-in-tube heat exchanger or tube coil type heat exchanger.
16. air conditioning and water heating system according to claim 15 is characterized in that: described evaporimeter (7) is finned type heat exchanger, heat-exchangers of the plate type, shell-and-tube exchanger, tube-in-tube heat exchanger or tube coil type heat exchanger.
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CN 201110382258 CN102393054B (en) | 2011-11-25 | 2011-11-25 | Air-conditioning water heating system |
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CN103344042B (en) * | 2013-07-08 | 2016-02-17 | 武宣宇特能源开发有限公司 | Shower room |
CN104374115A (en) | 2013-08-14 | 2015-02-25 | 开利公司 | Heat pump system, heat pump unit and a multifunctional mode control method for heat pump system |
CN103743099B (en) * | 2014-01-28 | 2016-03-02 | 山东创尔沃热泵技术股份有限公司 | Shower heat cycle system with little energy consumption |
CN104224004B (en) * | 2014-09-12 | 2016-08-24 | 王盛洪 | A kind of recovery type heat bath devices |
CN105222342A (en) * | 2015-10-30 | 2016-01-06 | 江门市达能环保节能科技有限公司 | Enhanced heat exchange formula heat pump |
CN109883056B (en) * | 2019-01-09 | 2021-06-25 | 青岛海尔空调器有限总公司 | Control method of energy system |
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CN109764511B (en) * | 2019-01-09 | 2021-08-24 | 重庆海尔空调器有限公司 | Control method of energy system |
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CN114263994B (en) * | 2021-11-16 | 2023-07-11 | 中山大学 | Bathroom heat recovery water heater |
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JPS57129335A (en) * | 1981-02-04 | 1982-08-11 | Koji Mitsuo | Method for room cooling or space heating |
CN201662218U (en) * | 2009-11-23 | 2010-12-01 | 郭文康 | Multi-temperature-section heat pump type water heater unit |
CN201652663U (en) * | 2010-04-29 | 2010-11-24 | 四川长虹空调有限公司 | Heat recovery heat pump air conditioning system |
CN102168898A (en) * | 2011-04-15 | 2011-08-31 | 上海理工大学 | Multifunctional heat pump air-condition water heater and heat recovery method |
CN202328590U (en) * | 2011-11-25 | 2012-07-11 | 佛山市确正冷热设备有限公司 | Air conditioner hot water system |
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