CN207702733U - CO2Hot application apparatus - Google Patents
CO2Hot application apparatus Download PDFInfo
- 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
- Authority
- CN
- China
- Prior art keywords
- heat
- water
- heat exchanger
- pump
- application apparatus
- Prior art date
- 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
Links
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
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.
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)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109780723A (en) * | 2017-11-13 | 2019-05-21 | 游素月 | CO2Hot application apparatus |
-
2017
- 2017-11-13 CN CN201721507979.7U patent/CN207702733U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109780723A (en) * | 2017-11-13 | 2019-05-21 | 游素月 | CO2Hot application apparatus |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN201244179Y (en) | High-efficient energy-saving heat pump sauna system | |
CN109099501A (en) | The novel heating device that air source heat pump and vapour-water heat-exchange unit cooperate | |
CN205782788U (en) | Air energy steam all-in-one | |
CN207702733U (en) | CO2Hot application apparatus | |
CN202008184U (en) | Instant electric heating type solar heat supply system | |
CN205744026U (en) | Exhaust steam of electric power plant heating Living Water and softening water heat supply water charging system | |
CN201514041U (en) | Air source heating machine for steam room | |
CN101313879B (en) | CO2 high-temperature heat pump saunas system | |
CN203310084U (en) | High-temperature air source heat pump water heater | |
CN102168869A (en) | Electric instant heating type solar heat supply heating system | |
CN109780723A (en) | CO2Hot application apparatus | |
CN202008190U (en) | Heating system complementarily using solar energy, air source and electric energy | |
CN202126010U (en) | Air source heat pump and fuel gas series type water heater | |
CN109140772A (en) | Water heater and floor heating based on a kind of heat pump and fast electric heating block combiner | |
CN204683337U (en) | Heat pump water dispenser | |
CN207945848U (en) | A kind of recombination energy heat utilization device | |
CN208846403U (en) | Adjacent machine auxiliary steam based on furnace water circulation starts heating system | |
CN208566195U (en) | Open type heat pump hot water apparatus based on air circulation | |
CN107166480A (en) | Nuclear power plant's heating plant heat-exchange system | |
CN208871902U (en) | A kind of green energy conservation moving energy station provided multiple forms of energy to complement each other | |
CN207936490U (en) | A kind of heat pump-electromagnetic induction composite crude oil heating device | |
CN105758060B (en) | A kind of solar heat pump and water heating, cold air, heating all-in-one | |
CN205783237U (en) | A kind of air source heat pump floor heating circulation system | |
CN205402885U (en) | Energy -efficient electric hanging stove of 5KW | |
CN205783800U (en) | A kind of heat pump air-source water heater |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
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 |