CN102393054A - Air-conditioning water heating system - Google Patents
Air-conditioning water heating system Download PDFInfo
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- CN102393054A CN102393054A CN2011103822589A CN201110382258A CN102393054A CN 102393054 A CN102393054 A CN 102393054A CN 2011103822589 A CN2011103822589 A CN 2011103822589A CN 201110382258 A CN201110382258 A CN 201110382258A CN 102393054 A CN102393054 A CN 102393054A
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 167
- 238000010438 heat treatment Methods 0.000 title claims abstract description 41
- 238000004378 air conditioning Methods 0.000 title claims abstract description 35
- 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
- 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
- -1 Alpaka Chemical compound 0.000 claims description 8
- 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 9
- 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
- 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 makes full use of waste water after the shower, can the energy that absorb 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 to come the device of 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 that the present invention will solve provides a kind of used heat that makes full use of waste water after the shower, can the energy that absorb 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 that the present invention will solve; Can realize through 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 said storage-type condenser 2 is communicated with the inlet of first switching valve 3; One of them outlet of this first switching valve 3 is communicated with the inlet of energy storage type Waste Heat Recovery interchanger 5; Another outlet of this first switching valve 3 is communicated with the inlet of first throttle valve 4, and the outlet of said first throttle valve 4 is communicated with the inlet of energy storage type Waste Heat Recovery interchanger 5; The outlet of said energy storage type Waste Heat Recovery interchanger 5 is communicated with the inlet of second switching valve 10; One of them outlet of this second switching valve 10 is communicated with the inlet of compressor 1; Another outlet of this second switching valve 10 is communicated with the inlet of air cooled condenser 8; The outlet of said air cooled condenser 8 is communicated with the inlet of second choke valve 9, and the outlet of said second choke valve 9 is communicated with the inlet of evaporimeter 7, and the outlet of said evaporimeter 7 is communicated with the inlet of compressor 1; The inlet of said shower bath is communicated with the delivery port of said storage-type condenser 2; Said water heat exchanger 6 is arranged on the top of said energy storage type Waste Heat Recovery interchanger 5, and the outlet of said water heat exchanger 6 is communicated with the water inlet of storage-type condenser 2 or the outlet of said water heat exchanger 6 is communicated with the water inlet of storage-type condenser 2 and the inlet 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 and the inlet of shower bath simultaneously.The water heat exchanger 6 of the baffle plate that catchments is arranged, so that 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 inlet 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 through 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; Through the 5 implementation second level condensations of energy storage type Waste Heat Recovery interchanger; The energy storage type Waste Heat Recovery interchanger 5 of this moment is condenser functions; When the inner water of energy storage type Waste Heat Recovery interchanger also is heated can't satisfy condensation and require the time, carry out third level condensations through air cooled condenser 8 again, guarantee the condensation effect of whole process of refrigerastion through the condensation that divides three grades.Working medium is evaporated in evaporimeter through 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 inlet of the gas outlet of storage-type condenser 2 through 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 inlet 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 through 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 an evaporator function to working medium through the expansion valve throttling after the condensation.
In above-mentioned two kinds of operating positions, the 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 got into and carries out further heat exchange in the storage-type condenser 2; When the outlet of water heat exchanger 6 is communicated with the inlet of water inlet and shower bath of storage-type condenser 2 simultaneously; In the running water after first amount of reheating reclaims; A part gets into condenser and carries out further heat exchange; Another part then directly gets into shower bath, and two parts running water mixes the temperature that reaches suitable in shower bath.
The second heavy Waste Heat Recovery is accomplished by evaporimeter, and evaporimeter and waste water carry out heat exchange, and waste water is freezed to about 5-10 ℃ cold water by 25-30 ℃; In this process; Cold-producing medium in the evaporimeter has absorbed more than 20 heats of spending, and absorbed heat is promoted to condenser through compressor, and the running water and the condenser that wherein promote after the temperature carry out heat exchange; Reach the purpose that is heated into running water hot water, and then gush out from shower bath.Add that the first heavy heat recovery is need not consume any energy by the completion of conducting heat naturally in the whole process of hot tap-water; Second amount of reheating reclaims through 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 through 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 according to the 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 accomplishes the indoor exhaust function, to accelerate the circulation of room air.
On the basis of the above, shower bath according to the invention comprises switch 12 and shower gondola water faucet 11, and the inlet of said switch 12 is connected the delivery port with storage-type condenser 2 with the outlet of water heat exchanger 6; The outlet of switch 12 is connected with shower gondola water faucet 11; Said 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 said shower bath is hot and cold combustion taps or hot water tap; The water inlet of hot water of said hot and cold combustion taps, cold water inlet are communicated with the outlet of the delivery port and the water interchanger 6 of storage-type condenser 2 respectively, and the delivery port of said hot and cold combustion taps is communicated with shower gondola water faucet 11; Said hot water tap's water inlet is communicated with the outlet of the delivery port and the water interchanger 6 of storage-type condenser 2 respectively, and said hot water tap's delivery port is communicated with shower gondola water faucet 11.
Said compressor 1 is scroll compressor, rotor-type compressor or reciprocating compressor.
Said storage-type condenser 2 is heat-exchangers of the plate type, tube-in-tube heat exchanger or tube coil type heat exchanger; Said storage-type condenser 2 is processed by stainless steel, red copper, Alpaka, aluminium or titanium, and it can also adopt other heat-transfer matcrial to make.
Said 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; Said energy storage type Waste Heat Recovery interchanger is processed by stainless steel, red copper, Alpaka, aluminium or titanium, and it can also adopt other heat-transfer matcrial to make.
Said water heat exchanger 6 is tubing heat exchanger or heat-exchangers of the plate type; Said hydro-thermal heat exchanger 6 is processed by stainless steel, red copper, Alpaka, aluminium or titanium, and it can also adopt other heat-transfer matcrial to make.
Said first switching valve 3 and/or second switching valve 10 are triple valve, magnetic valve or the commutation function valve are arranged.
The said first throttle valve 4 and/or second choke valve 9 are expansion valve or capillary; Said 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.
Said 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.
Said 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, cold air and degassing function can be provided; And the temperature difference of utilizing waste water and running water is carried out the recovery of first amount of reheating; Utilize waste water to come the Teat pump boiler of heat hot water as thermal source again; 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 a 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 is respectively equipped with evaporimeter 7 and is 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 inlet of first switching valve 3; One of them outlet of this first switching valve 3 is communicated with the inlet of energy storage type Waste Heat Recovery interchanger 5; Another outlet of this first switching valve 3 is communicated with the inlet of first throttle valve 4, and the outlet of first throttle valve 4 is communicated with the inlet 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 inlet of second switching valve 10; One of them outlet of this second switching valve 10 is communicated with the inlet of compressor 1; Another outlet of this second switching valve 10 is communicated with the inlet of air cooled condenser 8; The outlet of air cooled condenser 8 is communicated with the inlet of second choke valve 9, and the outlet of second choke valve 9 is communicated with the inlet of evaporimeter 7, and the outlet of evaporimeter 7 is communicated with the inlet 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 the hot and cold combustion taps 12 and 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 the 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 processed 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 processed 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 process 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 and the inlet of shower bath simultaneously.The water heat exchanger 6 of the baffle plate that catchments is arranged, so that 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 inlet 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 through 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; Through the 5 implementation second level condensations of energy storage type Waste Heat Recovery interchanger; The energy storage type Waste Heat Recovery interchanger 5 of this moment is condenser functions; When the inner water of energy storage type Waste Heat Recovery interchanger also is heated can't satisfy condensation and require the time, carry out third level condensations through air cooled condenser 8 again, guarantee the condensation effect of whole process of refrigerastion through the condensation that divides three grades.Working medium is evaporated in evaporimeter through 10 throttlings of second choke valve after the condensation, and cold air is provided in evaporation process; And the blower fan on air cooled condenser 8 and the evaporimeter 7 is connected to indoor gas extraction system completion 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 inlet of the gas outlet of storage-type condenser 2 through 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 inlet 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 through 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 an evaporator function to working medium through the expansion valve throttling after the condensation.
In above-mentioned two kinds of operating positions, the 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 accomplished by evaporimeter, and evaporimeter and waste water carry out heat exchange, and waste water is freezed to about 5-10 ℃ cold water by 25-30 ℃; In this process; Cold-producing medium in the evaporimeter has absorbed more than 20 heats of spending, and absorbed heat is promoted to condenser through compressor, and the running water and the condenser that wherein promote after the temperature carry out heat exchange; Reach the purpose that is heated into running water hot water, and then gush out from shower bath.Add that the first heavy heat recovery is need not consume any energy by the completion of conducting heat naturally in the whole process of hot tap-water; Second amount of reheating reclaims through 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 through absorbing the heat of ambient air around the interchanger, and heat stored to task down heat is provided.
Claims (10)
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 said storage-type condenser (2) is communicated with the inlet of first switching valve (3); One of them outlet of this first switching valve (3) is communicated with the inlet of energy storage type Waste Heat Recovery interchanger (5); Another outlet of this first switching valve (3) is communicated with the inlet of first throttle valve (4), and the outlet of said first throttle valve (4) is communicated with the inlet of energy storage type Waste Heat Recovery interchanger (5); The outlet of said energy storage type Waste Heat Recovery interchanger (5) is communicated with the inlet of second switching valve (10); One of them outlet of this second switching valve (10) is communicated with the inlet of compressor (1); Another outlet of this second switching valve (10) is communicated with the inlet of air cooled condenser (8); The outlet of said air cooled condenser (8) is communicated with the inlet of second choke valve (9), and the outlet of said second choke valve (9) is communicated with the inlet of evaporimeter (7), and the outlet of said evaporimeter (7) is communicated with the inlet of compressor (1); The inlet of said shower bath is communicated with the delivery port of said storage-type condenser (2); Said water heat exchanger (6) is arranged on the top of said energy storage type Waste Heat Recovery interchanger (5), and the outlet of said water heat exchanger (6) is communicated with the water inlet of storage-type condenser (2) or the outlet of said water heat exchanger 6 is communicated with the water inlet of storage-type condenser (2) and the inlet 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 is characterized in that: said shower bath comprises switch (12) and shower gondola water faucet (11), and the inlet of said switch (12) is connected the delivery port with storage-type condenser (2) with the outlet of water heat exchanger (6); The outlet of switch (12) is connected with shower gondola water faucet (11); Said 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 said shower bath (12) is hot and cold combustion taps or hot water tap; The water inlet of hot water of said hot and cold combustion taps, cold water inlet are communicated with the outlet of the delivery port and the water interchanger (6) of storage-type condenser (2) respectively, and the delivery port of said hot and cold combustion taps is communicated with shower gondola water faucet (11); Said hot water tap's water inlet is communicated with the outlet of the delivery port and the water interchanger (6) of storage-type condenser (2) respectively, and said 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 is characterized in that: said compressor (1) is scroll compressor, rotor-type compressor or reciprocating compressor;
Said storage-type condenser (2) is heat-exchangers of the plate type, tube-in-tube heat exchanger or tube coil type heat exchanger;
Said storage-type condenser (2) is processed by stainless steel, red copper, Alpaka, aluminium or titanium.
6. air conditioning and water heating system according to claim 5 is characterized in that: said 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;
Said energy storage type Waste Heat Recovery interchanger is processed by stainless steel, red copper, Alpaka, aluminium or titanium.
7. air conditioning and water heating system according to claim 6 is characterized in that: said water heat exchanger (6) is tubing heat exchanger or heat-exchangers of the plate type;
Said hydro-thermal heat exchanger (6) is processed by stainless steel, red copper, Alpaka, aluminium or titanium.
8. air conditioning and water heating system according to claim 7 is characterized in that: said first switching valve (3) and/or second switching valve (10) are triple valve, magnetic valve or the commutation function valve are arranged.
9. air conditioning and water heating system according to claim 8 is characterized in that: said first throttle valve (4) and/or second choke valve (9) are expansion valve or capillary;
Said expansion valve 3 is heating power expansion valve or electric expansion valve.
10. air conditioning and water heating system according to claim 9 is characterized in that: said 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;
Said 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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| Application Number | Priority Date | Filing Date | Title |
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| CN 201110382258 CN102393054B (en) | 2011-11-25 | 2011-11-25 | Air-conditioning water heating system |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201110382258 CN102393054B (en) | 2011-11-25 | 2011-11-25 | Air-conditioning water heating system |
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| CN102393054B CN102393054B (en) | 2013-10-02 |
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| CN 201110382258 Expired - Fee Related CN102393054B (en) | 2011-11-25 | 2011-11-25 | Air-conditioning water heating system |
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| CN103054306A (en) * | 2013-02-07 | 2013-04-24 | 柳州宇特能源科技有限公司 | High-efficiency hairdressing bed |
| CN103344042A (en) * | 2013-07-08 | 2013-10-09 | 武宣宇特能源科技有限公司 | Shower room |
| CN103743099A (en) * | 2014-01-28 | 2014-04-23 | 山东创尔沃热泵技术股份有限公司 | Shower heat cycle system with little energy consumption |
| CN104224004A (en) * | 2014-09-12 | 2014-12-24 | 王盛洪 | Heat recovery type bathing machine |
| 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 |
| 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 |
| CN109737611A (en) * | 2019-01-09 | 2019-05-10 | 青岛海尔空调器有限总公司 | A kind of control method of energy resource system |
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| CN110513876A (en) * | 2019-09-16 | 2019-11-29 | 杜嵘 | A kind of wind water cooling integral type refrigeration system |
| CN114263994A (en) * | 2021-11-16 | 2022-04-01 | 中山大学 | Bathroom heat recovery system hot water system device |
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| CN103054306A (en) * | 2013-02-07 | 2013-04-24 | 柳州宇特能源科技有限公司 | High-efficiency hairdressing bed |
| CN103054306B (en) * | 2013-02-07 | 2015-12-30 | 柳州宇特能源科技有限公司 | efficient hairdressing bed |
| CN103344042B (en) * | 2013-07-08 | 2016-02-17 | 武宣宇特能源开发有限公司 | Shower room |
| CN103344042A (en) * | 2013-07-08 | 2013-10-09 | 武宣宇特能源科技有限公司 | Shower room |
| US10197306B2 (en) | 2013-08-14 | 2019-02-05 | Carrier Corporation | Heat pump system, heat pump unit using the same, and method for controlling multiple functional modes thereof |
| 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 |
| CN103743099A (en) * | 2014-01-28 | 2014-04-23 | 山东创尔沃热泵技术股份有限公司 | Shower heat cycle system with little energy consumption |
| CN104224004A (en) * | 2014-09-12 | 2014-12-24 | 王盛洪 | Heat recovery type bathing machine |
| 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 |
| CN109737611A (en) * | 2019-01-09 | 2019-05-10 | 青岛海尔空调器有限总公司 | A kind of control method of energy resource system |
| CN109764511A (en) * | 2019-01-09 | 2019-05-17 | 青岛海尔空调器有限总公司 | A kind of control method of energy resource system |
| CN109883056A (en) * | 2019-01-09 | 2019-06-14 | 青岛海尔空调器有限总公司 | A kind of control method of energy resource system |
| 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 |
| CN109764511B (en) * | 2019-01-09 | 2021-08-24 | 重庆海尔空调器有限公司 | Control method of energy system |
| CN110513876A (en) * | 2019-09-16 | 2019-11-29 | 杜嵘 | A kind of wind water cooling integral type refrigeration system |
| CN114263994A (en) * | 2021-11-16 | 2022-04-01 | 中山大学 | Bathroom heat recovery system hot water system device |
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