CN207702733U - CO2Hot application apparatus - Google Patents

CO2Hot application apparatus Download PDF

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Publication number
CN207702733U
CN207702733U CN201721507979.7U CN201721507979U CN207702733U CN 207702733 U CN207702733 U CN 207702733U CN 201721507979 U CN201721507979 U CN 201721507979U CN 207702733 U CN207702733 U CN 207702733U
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CN
China
Prior art keywords
heat
water
heat exchanger
pump
application apparatus
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Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN201721507979.7U
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Chinese (zh)
Inventor
游素月
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Individual
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Individual
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Publication date
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Priority to CN201721507979.7U priority Critical patent/CN207702733U/en
Application granted granted Critical
Publication of CN207702733U publication Critical patent/CN207702733U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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Abstract

The utility model provides a CO2Hot application apparatus, including:One CO2Heat application system and a heat reservoir.The CO2Heat application system has a CO2Refrigerant cycles, the cycle are made of a first heat exchanger, a compressor, a second heat exchanger and an expansion valve, are configured in a CO together with a thermal cycle2In heat-pump apparatus.Wherein, the CO2Refrigerant cycles, by carbon dioxide condensing to postcritical gas, reduce CO in air relatively using vapor-compression mode2Content neither influences ball ecological environment, and can reduce the average temperature of the earth, slows down the threat of greenhouse effects.The heat reservoir has a pipeline by second heat exchanger, guides normal-temperature water and CO2Refrigerant cycles heat exchange is high-temperature water, reaches heating effect, and electricity consumption is few.The thermal cycle is by CO2Hot gas output outside refrigerant cycles, dries food waste the like waste, has both the efficiency of recycling.

Description

CO2Hot application apparatus
Technical field
The utility model is related to the hot application field of heating, particularly relate to it is a kind of using vapor-compression mode by CO2Condensation To the device of supercritical gas.
Background technology
In hot application field, the heating means of early stage are burnings.Burning charcoal causes raw black smoke, or generates an oxidation The pernicious gases such as carbon, carbon dioxide.Burning natural gas directly heats water temperature, and the service efficiency of consuming energy is about 80%.
Recent heating means use electric heater, and normal-temperature water is directly heated to high-temperature water.The Normal practice of electric heater, The heat of 860 kilocalories is generated with kilowatt-hour, the service efficiency of consuming energy is about 95%.
Therefore, it takes new technology to replace existing hot application mode, just becomes the utility model project urgently to be resolved hurrily.
New content
The utility model provides a kind of CO2Hot application apparatus, main purpose are:Using vapor-compression mode, by CO2It is cold It coagulates to postcritical gas, while heat exchange is carried out with normal-temperature water, neither influence ball ecological environment, and heating effect can be reached Fruit has both the efficiency of recycling.
In order to achieve the above object, the CO of the utility model2Hot application apparatus includes:
One CO2Heat application system, including:One CO2Refrigerant cycles, by a first heat exchanger, a compressor, one second heat Exchanger and an expansion valve form, the CO2Refrigerant cycles use vapor-compression mode by carbon dioxide condensing to postcritical gas Body;One thermal cycle, by CO2Hot gas output outside refrigerant cycles;And
One heat reservoir has a pipeline by second heat exchanger, which is the water inlet end of room temperature, another end It is the water outlet of high temperature.
Wherein, the first heat exchanger, compressor, expansion valve and second heat exchanger configuration are in a CO2In heat-pump apparatus. The thermal cycle is configured in CO2In heat-pump apparatus, guiding hot gas exports CO2Outside heat-pump apparatus.
In addition, the heat reservoir also has a water tank group, the water tank group to have an at least water tank, the water tank to be connected to pipeline Between both ends.Secondly, the pipeline can connect third heat exchanger, pressure reducing valve, circulating pump, with water end (W.E.), boiler, connector, check valve, One of ball valve, back water pump and stand-by pump.
The CO2It is present in earth atmosphere, visible light is allowed to pass through, absorb infrared ray and ultraviolet light, keeps the sun Thermal energy be not lost in, greenhouse effects can be caused.The CO of the utility model2Hot application apparatus, using vapor-compression mode by CO2It is cold It coagulates to postcritical gas, it is opposite to reduce CO in air2Content neither influences ball ecological environment, and it is average to reduce the earth Temperature, slow down the threat of greenhouse effects.
Meanwhile normal-temperature water flows into heat reservoir, with CO2Refrigerant cycles heat exchange is high-temperature water, reaches heating effect.Especially It is the CO of the utility model2Hot application apparatus kilowatt-hour can generate the heat for being three times in 860 kilocalories.In other words, equally Heat, the electricity consumption of the utility model, only the 1/3 of electric heater.
Furthermore the CO2Hot gas caused by refrigerant cycles operating is collected and is exported the external world by thermal cycle, can dry food waste The like waste has both the efficiency of recycling.
Description of the drawings
Fig. 1 is the utility model CO2The schematic diagram of hot application apparatus.
Fig. 2 is the utility model CO2The configuration diagram of hot application apparatus.
In figure:
CO210 suction device 11 of heat application system
12 compressor 13 of heat exchanger
14 expansion valve 15 of second heat exchanger
CO216 thermal cycle 17 of refrigerant cycles
Hot gas output 18
20 pipeline 21 of heat reservoir
22 water outlet 23 of water inlet end
24 water tank 241,242,243 of water tank group
25 circulating pump 26 of pressure reducing valve
With 27 boiler 28 of water end (W.E.)
CO2The draining of heat-pump apparatus 30 31
32 check valve 33 of connector
34 back water pump 35 of ball valve
Stand-by pump 36
40 normal-temperature water 41 of water tank of voltage regulation
42 waste water of middle warm water flows into 43
44 filter 45 of discharge of wastewater
46 third heat exchanger 47 of water meter
Specific implementation mode
In fig. 1 it is illustrated that CO2The principle of hot application apparatus, specifically by a CO2One heat accumulation system of the collocation of heat application system 10 20 composition of system.
Wherein, the CO2Heat application system 10 includes two parts:One is CO2Refrigerant cycles 16, one is thermal cycle 17.The CO2 Refrigerant cycles 16 are made of a first heat exchanger 12, a compressor 13, a second heat exchanger 14 and an expansion valve 15.It should CO2Refrigerant cycles 16 are interior cycles, using vapor-compression mode, by carbon dioxide (CO2) condense to postcritical gas.The heat Cycle 20 is outer circulation, collects CO2Hot gas outside refrigerant cycles 16, and kitchen is dried to the external world by 18 output of hot gas output Remaining the like waste has both the efficiency of recycling.
The heat reservoir 20 has a pipeline 21 by second heat exchanger 14.21 one end of pipeline is the water inlet end of room temperature 22, normal-temperature water carries out heat exchange with second heat exchanger 14, therefore 21 other end of pipeline is the water outlet 23 of high temperature.
After energization, the CO2Heat application system 10 supplies electrical power to a suction device 11 and extracts outside air.First heat is handed over Parallel operation 12 executes heat exchange operation, and the thermal energy of air is transmitted to refrigerant.The refrigerant is carbon dioxide (CO2), it is compressed Machine 13 is pressed into postcritical gas, generates the cholesteric-nematic transition of condensation, while discharging high temperature.The second heat exchanger 14 is by phase transformation High temperature and room temperature 21 heat exchange of pipeline, form up to about 80 °~90 ° of water temperature and flow to water outlet 23 or with water end (W.E.), such as Spa pool, bathroom or washroom etc..Under the flow-rate adjustment of expansion valve 15, the carbon dioxide (CO of loss of heat2) flow to the first heat Exchanger 12 carries out heat exchange with outside air once again.
In addition, the heat reservoir 20 also has a water tank group 24, the water tank group 24 there are three water tank 241,242,243, These water tanks 241,242,243 are chained together, between being connected to 21 both ends of pipeline (i.e. water inlet end 22 and water outlet 23), Be conducive to the convection current of normal-temperature water and high-temperature water.
Certainly, which is also connected a pressure reducing valve 25 and a circulating pump 26, contributes to control or the water of water (flow) direction The adjusting of pressure.
As shown in Fig. 2, the CO2The configuration diagram of hot application apparatus.Wherein, the first heat exchanger, compressor, expansion valve, Second heat exchanger and thermal cycle configuration are in a CO2In heat-pump apparatus 30.The thermal cycle guides hot gas output 18 to CO2Heat pump is set Outside standby 30.Certainly, heat exchange can inevitably generate some water, therefore CO2Heat-pump apparatus 30 needs 31 or relevant draining of a draining to set It applies, avoids seeping phenomenon.
In addition to this, which also has multiple water end (W.E.) 27, a boiler 28, multiple two-ways or the connectors of threeway 32, multiple check valves 33, multiple ball valves 34, a back water pump 35, a stand-by pump 36, a water tank of voltage regulation 40, a filter 45, a water Table 46 and a third heat exchanger 47, are connected to pipeline 21 in CO2The part of 30 outside of heat-pump apparatus.
Under the guiding of pipeline 21, normal-temperature water 41 flows into third heat exchanger 47 via water tank of voltage regulation 40.In third heat exchange In device 47, the waste heat that normal-temperature water 41 flows into 43 with waste water carries out heat exchange, becomes middle warm water 42 and flows out third heat exchanger 47.Institute The waste water stated typically refers to the flowing water after bathing or shower, and after loss of heat, discharge of wastewater 44 is discharged outside third heat exchanger 19.
Warm water 42 filters out impurity in filter 45 in this, and flow is shown by water meter 46, begins to enter CO230 heat of heat-pump apparatus Be exchanged for high-temperature water, operated by the flow of connector 32, check valve 33 and ball valve 34, into three water tanks 241,242,243 it One, it turns to multiple flow to bathroom, washroom, swimming pool or spa pool with one of water end (W.E.) 27 respectively.
If the water temperature of any water tank 241,242,243 is less than default value, moreover it is possible to reheat via boiler 28, then return Flowing water case 241,242,243.As for the back water pump 35 or stand-by pump 36 then determine water pipeline 21 flow direction.

Claims (5)

1. a kind of CO2Hot application apparatus, including:
One CO2Heat application system has:One uses vapor-compression mode by carbon dioxide condensing to the CO of postcritical gas2It causes SAPMAC method is made of a first heat exchanger, a compressor, a second heat exchanger and an expansion valve;One by CO2Refrigerant cycles The thermal cycle of external hot gas output;And
One heat reservoir has a pipeline by second heat exchanger, which is the water inlet end of room temperature, and another end is high The water outlet of temperature.
2. CO as described in claim 12Hot application apparatus, wherein the first heat exchanger, compressor, expansion valve and the second heat Exchanger is configured in a CO2In heat-pump apparatus.
3. CO as claimed in claim 22Hot application apparatus, wherein the thermal cycle is configured in CO2Heat is guided in heat-pump apparatus Gas exports CO2Outside heat-pump apparatus.
4. CO as claimed in claim 1,2 or 32Hot application apparatus, wherein the heat reservoir also has a water tank group, the water Case group has an at least water tank, the water tank to be connected between the pipeline both ends.
5. CO as claimed in claim 42Hot application apparatus, wherein piping connection third heat exchanger, pressure reducing valve, the cycle Pump, with one of water end (W.E.), boiler, connector, check valve, ball valve, back water pump and stand-by pump.
CN201721507979.7U 2017-11-13 2017-11-13 CO2Hot application apparatus Expired - Fee Related CN207702733U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201721507979.7U CN207702733U (en) 2017-11-13 2017-11-13 CO2Hot application apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201721507979.7U CN207702733U (en) 2017-11-13 2017-11-13 CO2Hot application apparatus

Publications (1)

Publication Number Publication Date
CN207702733U true CN207702733U (en) 2018-08-07

Family

ID=63022480

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201721507979.7U Expired - Fee Related CN207702733U (en) 2017-11-13 2017-11-13 CO2Hot application apparatus

Country Status (1)

Country Link
CN (1) CN207702733U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109780723A (en) * 2017-11-13 2019-05-21 游素月 CO2Hot application apparatus

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109780723A (en) * 2017-11-13 2019-05-21 游素月 CO2Hot application apparatus

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GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20180807

Termination date: 20201113