CN1865812A - Heat pump system and method for heating a fluid - Google Patents
Heat pump system and method for heating a fluid Download PDFInfo
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- CN1865812A CN1865812A CNA200510125308XA CN200510125308A CN1865812A CN 1865812 A CN1865812 A CN 1865812A CN A200510125308X A CNA200510125308X A CN A200510125308XA CN 200510125308 A CN200510125308 A CN 200510125308A CN 1865812 A CN1865812 A CN 1865812A
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- refrigerant
- fluid
- pipeline
- temperature
- condenser
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Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24H—FLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
- F24H4/00—Fluid heaters characterised by the use of heat pumps
- F24H4/02—Water heaters
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24D—DOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
- F24D15/00—Other domestic- or space-heating systems
- F24D15/04—Other domestic- or space-heating systems using heat pumps
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24D—DOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
- F24D17/00—Domestic hot-water supply systems
- F24D17/02—Domestic hot-water supply systems using heat pumps
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24H—FLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
- F24H9/00—Details
- F24H9/20—Arrangement or mounting of control or safety devices
- F24H9/2007—Arrangement or mounting of control or safety devices for water heaters
- F24H9/2014—Arrangement or mounting of control or safety devices for water heaters using electrical energy supply
- F24H9/2028—Continuous-flow heaters
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B1/00—Compression machines, plants or systems with non-reversible cycle
- F25B1/10—Compression machines, plants or systems with non-reversible cycle with multi-stage compression
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B30/00—Heat pumps
- F25B30/02—Heat pumps of the compression type
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2339/00—Details of evaporators; Details of condensers
- F25B2339/04—Details of condensers
- F25B2339/047—Water-cooled condensers
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2400/00—General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
- F25B2400/04—Refrigeration circuit bypassing means
- F25B2400/0403—Refrigeration circuit bypassing means for the condenser
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2400/00—General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
- F25B2400/05—Compression system with heat exchange between particular parts of the system
- F25B2400/052—Compression system with heat exchange between particular parts of the system between the capillary tube and another part of the refrigeration cycle
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2400/00—General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
- F25B2400/13—Economisers
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2600/00—Control issues
- F25B2600/25—Control of valves
- F25B2600/2509—Economiser valves
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
- Y02B30/12—Hot water central heating systems using heat pumps
Abstract
This invention relates to a heat pump system and in particular to a heat pump system and method for heating a fluid. According to one aspect of the invention, there is provided a heat pump system for heating a fluid, said system including: an evaporator for extracting heat from a heat source to vaporise a refrigerant; a compressor fluidly connected to said evaporator for compressing said refrigerant vapour; a condenser fluidly connected to said compressor for transferring heat from said compressed refrigerant to said fluid; a main expansion device fluidly connecting said condenser to said evaporator for reducing the temperature of the refrigerant; means for diverting and reducing the temperature of a portion of said refrigerant from said condenser, and means for fluidly injecting said temperature reduced refrigerant portion into said compressor such that said temperature reduced refrigerant portion mixes with said refrigerant vapour at an intermediate pressure and induces at least quasi-two- stage compression of said refrigerant vapour and said refrigerant portion for discharge into said condenser. According to another aspect of the invention, there is provided a method for heating a fluid.
Description
Technical field
The present invention relates to heat pump and relate in particular to heat pump and the method that adds hot fluid.
It mainly is to be used as a heat pump and a kind of method that the present invention develops, and this method is used under the big environment of cold environment or environment temperature change water being heated, and is hereinafter all illustrated with reference to this kind purposes.Yet, recognize that the present invention is not limited to this special application field.
Background technology
Should never be considered to admit that to any discussion of prior art this kind prior art is well-known or forms the general knowledge in this field by specification.
The cleaning water need be heated to about 60 ℃ or more than.For water is heated, need be heated to this temperature toward contact.The someone uses air supply heat pump system (air sourced heatpump system) to carry out this type water is heated, and uses compressor of air conditioner usually.Yet, because the compressor of air conditioner operating temperature range is narrow, conventional heat pump just can not be under ambient temperature range widely for example summer awfully hot but work under the situation that winter is terribly cold.Similarly, this conventional system can not be worked under the situation that the temperature difference is bigger between water and the thermal source.For example, environment temperature continues lowly such as in the cold environment being exactly this kind situation.
The mode that overcomes this kind difficulty just is to use two-stage compression system, multi-stage compression system or cascade system (cascade system).Yet these system requirements have two or more compressors, so just make heat pump become complicated, expensive, and are difficult to adapt to the big environment temperature of change.And when environment temperature was warm, this compressibility was also just unnecessary.
Under cold environment, typically use fossil-fuel-fired boiler water is heated, this usage operating cost height, and environment had ill-effect.
Summary of the invention
The objective of the invention is to overcome or improve at least one shortcoming in the prior art, perhaps provide the replacement scheme of usefulness.
The objective of the invention is provides a kind of heat pump with its way of recommendation, and this system has the compressor that can become accurate two stages of compression and carry out, its can be under cold environment or the big environment of environment temperature change under operate, and not only simply but also not expensive.
According to an aspect of the present invention, provide a kind of heat pump that is used to add hot fluid, this system comprises:
Be used for extracting hot and evaporimeter that refrigerant is evaporated from thermal source;
With the compressor that described evaporimeter fluid links to each other, it is used to compress the steam of above-mentioned refrigerant;
With the condenser that described compressor fluid links to each other, it is used for the heat from described compression refrigerant is sent to described fluid;
The flexible adjuster (expansiondevice) of the master that described condenser is linked to each other with described evaporimeter fluid, it is used to reduce the temperature of refrigerant;
Be used to make the device that shifts and reduce temperature from the described refrigerant of the part of described condenser; And
Be used for described temperature having been reduced the device that refrigerant partly is ejected into described compressor through fluid, under intermediate pressure, mix with described refrigerant vapor thereby make described temperature reduce refrigerant part, and cause described refrigerant vapor and be discharged into described refrigerant part in the described condenser by accurate at least two stages of compression.
According to another aspect of the present invention, provide a kind of method that is used to add hot fluid, this method comprises the following steps:
Extract heat and the cooling by evaporation agent from thermal source;
Compress described refrigerant vapor so that improve its temperature;
Sending described fluid to from the described heat that is compressed refrigerant vapor;
After above-mentioned transfer step, a part of described refrigerant is shifted and the reduction temperature;
Reduce the temperature of described refrigerant;
During described compression step, introduce described temperature and reduced the refrigerant part, under intermediate pressure, mix with described refrigerant vapor thereby make described temperature reduce the refrigerant part, and cause described refrigerant vapor and described refrigerant part by accurate at least two stages of compression; And
Discharge and describedly be compressed refrigerant so that in described transfer step, heat is sent to described fluid.
Transfer and temperature reduce device and preferably include the flexible adjuster that links to each other with condenser and compressor fluid.Should preferably include capillary or expansion valve (expansion valve) by flexible adjuster.Flexible adjuster can also comprise for example intercooler of heat exchanger.
Transfer and temperature reduce device and preferably include the bypass channel that links to each other with condenser and flexible adjuster fluid.
Fluid ejection apparatus preferably includes fluid injection valve, and this valve is used to control refrigerant and partly flows into flexible adjuster.Compressor preferably includes a fluid jet that is connected in fluid ejection apparatus.Fluid ejection apparatus preferably includes the check-valves that is connected with fluid jet fluid.
Described method preferably includes and makes described refrigerant reduce the return step of step to described evaporation step from described temperature.
Main flexible adjuster preferably links to each other with the condenser fluid via first pipeline.This first pipeline preferably links to each other with the bypass channel fluid.Main flexible adjuster can be an expansion valve.
Capillary is preferably near first pipeline, so that make first pipeline of flowing through go to the refrigerant cooling of main flexible adjuster.In a kind of recommendation form, capillary is spirally coiled in around first pipeline.Downstream end capillaceous can connect a segment pipe.This duct section (pipe section) preferably contacts with first pipeline, so that conduct heat between first pipeline and duct section.Duct section can be arranged essentially parallel to first pipeline, and can be fixed on first pipeline by metal holder or other suitable fasteners.Between the duct section and first pipeline, preferably there is heat transfer cream (heattransfer paste) to get involved, so that carry out heat transmission.Duct section preferably also is deformed into consistent with first pipeline.
Comprise under the situation of flexible adjuster and intercooler at temperature reduction device, preferably intercooler links to each other with condenser and main flexible adjuster fluid, thereby make refrigerant go to main flexible adjuster by intercooler, and with the refrigerant part heat-shift that passes intercooler.
Heated fluid is water preferably.Thermal source can be a surrounding air.
Description of drawings
Below, only with way of example with reference to description of drawings preferred embodiment of the present invention, in the accompanying drawings:
Fig. 1 is used for heat pump schematic overview to water heating according to the present invention; And
Fig. 2 is the schematic overview of another embodiment of the present invention.
The specific embodiment
Referring to Fig. 1, be used for the heat pump of water heating is comprised evaporimeter 1 and condenser 5, this evaporimeter is by making the refrigerant evaporation send compressor 4 to from the heat of thermal source 3 on every side, this compressor links to each other with evaporimeter 1 fluid and is used for the compression refrigerant steam, and this condenser links to each other with compressor 4 fluids and is used for the heat of the compression refrigerant of controlling oneself is transmitted feedwater 6.Thermal source 3 is the surrounding air under the cold environment, and compressor 4 is to have liquid ejection outlet 7 and the conventional compressor that is used for cryogenic refrigeration.
Its form is that flexible adjuster 8 capillaceous links to each other with condenser 5 and compressor 4 fluids, so that sub-fraction condensing refrigerant shifted and reduce its temperature.Fluid ejection apparatus 9 has fluidly reduced the refrigerant part to temperature and has been ejected into the compressor 4 from capillary 8.Temperature has reduced the refrigerant part mixes with the refrigerant vapor that is compressed to intermediate pressure in compressor 4, and causes accurate at least two stages of compression.The refrigerant that combines (refrigerant vapor and refrigerant part) is compressed again subsequently, and is discharged in the condenser 5.
Capillary 8 is spirally coiled in around the pipeline 11, when passing pipeline 11 with convenient cryogen flow to main expansion valve 10 it is cooled off.Duct section 15 also is fixed on the part 21 of pipeline 11 via metal holder, and is arranged essentially parallel to pipe section 21 and contacts with it, so that promote the heat transmission between duct section 15 and the pipe section 21.Between duct section 15 and pipe section 21, also applied heat transfer cream.Duct section 15 can be deformed, so that consistent with pipe section 21 and improve and conduct heat.
Other parts of heat pump comprise liquid electromagnetic valve 23 and the filter/dryer 25 between condenser 5 and capillary 8, and this valve is used to make condensing refrigerant is mobilely carried out and disconnect.Be provided with peephole (sight glass) 27 on pipeline 11, it is used to observe the refrigerant that enters before the main expansion valve 10.On auxiliary piping 31, also be provided with deicing magnetic valve 29.
The following describes the operational circumstances of heat pump.The heat that refrigerant in the evaporimeter 1 is taken from surrounding air 3 is evaporated.Compressor 4 extracts the refrigerant vapor of flash-pot 1, and with it from low pressure, low-temperature steam state boil down to high pressure, high-temperature vapour state.Then, high pressure, hyperthermia induced refrigerant vapor are discharged to condenser 5, and this condenser plays the work of heat exchanger in order to heat is become water 6 from refrigerant vapor.The result of this process is that refrigerant is condensed into liquid and cold excessively.
Then, liquid cryogen passes liquid electromagnetic valve 23 and filter/dryer 25, so that remove moisture and dirt in the refrigerant.After most of liquid cryogen passes filter/dryer 25, go to main expansion valve 10 with regard to flowing through pipeline 11.Liquid cryogen expands and passes main expansion valve 10, causes its pressure and temperature to descend.The temperature of refrigerant just is lower than the temperature of surrounding air 3 this moment.Then, refrigerant enters evaporimeter 1, there, is transmitted to refrigerant once again from the heat of surrounding air 3.The refrigerant that has evaporated finally is discharged in the compressor 4, and this kind circulation is carried out repeatedly.
When most of liquid cryogens enter main expansion valve 10, there is sub-fraction liquid cryogen (its can account for whole refrigerant about 10%) to enter the bypass channel 12, and passes liquid injection magnetic valve 13 and go to capillary 8 from pipeline 11.Capillary 8 makes the refrigerant demi-inflation, causes its pressure and temperature to descend.Partly pass duct section 15 and check-valves 17 and go to jet 7 so temperature has reduced refrigerant.So injected compressor 4 of giving of the refrigerant of liquid state/steam form part, so that mix and its cooling (be that is to say with the superheated refrigerant vapor after handling through pseudo-first-order compression in the compressor 4, after refrigerant vapor had been compressed into intermediate pressure, the refrigerant part is injected to be advanced in the compressor).Consequently, accurate two stages of compression has taken place, and combined refrigerant vapor and refrigerant partly are compressed to final pressure.The refrigerant that has compressed is discharged in the condenser 5 with that.
Because the refrigerant in the compressor 4 has passed through pseudo-first-order compression at least, temperature has been reduced refrigerant partly to be introduced in the compressor 4 and mixes with superheated refrigerant, will reduce the temperature of next rank compression refrigerant before, and therefore reduce the temperature in the compressor so that carry out subsequent compression.Be lowered to regard to the pressure ratio that causes the compression of each rank like this and conform with the desired degree of accurate two stages of compression, and therefore improve the efficient of each compression.The cause of spraying owing to the refrigerant segment fluid flow makes accurate two stages of compression combine in compressor with middle the cooling, also can reduce the power (power) that from heat pump, extracts (with single stage compress comparatively speaking).Fluid injection valve 13 and check-valves 17 are being controlled injected timing and the direction that temperature in the compressor 4 has reduced the refrigerant part of advancing.Therefore, just can controllably reach accurate at least two stages of compression with single-stage compressor.The result is that the temperature difference between condensation temperature and the evaporating temperature has obviously increased, so just increased the environment temperature opereating specification of heat pump.
The recommendation form of flexible adjuster 8 is a capillary, so that heat pump is simplified.The temperature that also can allow capillary 8 has reduced the refrigerant part and has only absorbed in its expansion from being used after the heat in the pipeline 11 and before entering main expansion valve 10.As mentioned above, capillary 8 is spirally coiled in around pipeline 11 and the duct section 15, and this duct section is arranged essentially parallel to pipeline 11 and contact with it.In this way, the refrigerant in the pipeline 11 will additionally be cooled off, and has so just reduced the risk that splash (flashing) took place before entering main expansion valve 10 liquid cryogen.
In the present embodiment, although there is the whole refrigerant of about 10% quantity to be transferred to capillary 8, the quantity of this transfer according to around the temperature of thermal source and desired water temperature and decide.
Although preferred embodiment of the present invention above has been described, understand that each building block of this system can change in other embodiments.
Fig. 2 has shown second embodiment, and wherein, corresponding component is all represented with same Reference numeral.In a second embodiment, flexible adjuster 8 is for having the expansion valve 33 of intercooler 35.Intercooler 35 links to each other with condenser 5 and expansion valve 10 fluids.Bypass channel 12 is positioned at intercooler 35 downstreams.Liquid cryogen from condenser 5 enters intercooler 35.Via bypass channel 12 before being extracted liquid injection valve 13, intercooler 35 makes the liquid cryogen cooling earlier in refrigerant part.Refrigerant partly passes expansion valve 33 so that further reduce its temperature and pressure.Temperature has reduced refrigerant and has partly then turned back to cooler 35, so as be delivered to the liquid cryogen exchanged heat of passing intercooler 35 before the compressor 4 from condenser 5.As in first embodiment, refrigerant part is mixed with refrigerant vapor in compressor and is caused accurate at least two stages of compression.Liquid cryogen part is extraction from middle cooler 35 after, thereby will reduce the possibility of refrigerant in expansion valve 33 and main expansion valve 9 splash in the two.
In some other embodiment,, just can cause multi-stage compression if requirement has reduced the refrigerant part by other those temperature after spraying the compression processing of the accurate second level.
Compressor can be the refrigeration compressor that wherein has one or more liquid ejection outlet, or is modified as any compressor that is equipped with liquid ejection outlet.
Heat pump has been described simplifiedly, so that help to understand the present invention.Recognize in this heat pump, to also have other parts and control and the used mechanical device of safety not to give explanation, but do not influence the basic operation of this system recommendation form like this.
Recommendation form of the present invention discussed above provides water has been heated used energy efficient and practical system, especially sends hot air supply heat pump system under the chilling temperatures environment.Recommendation form of the present invention substitutes current fossil-fuel-fired boiler, thereby reduces any adverse effect to environment.
Although with reference to special example the present invention has been described, the professional can understand, can implement the present invention with many other forms.
Claims (26)
1. heat pump that is used to add hot fluid, described system comprises:
Be used for extracting hot and evaporimeter that refrigerant is evaporated from thermal source;
With the compressor that described evaporimeter fluid links to each other, it is used to compress the steam of above-mentioned refrigerant;
With the condenser that described compressor fluid links to each other, it is used for the heat from described compression refrigerant is sent to described fluid;
The flexible adjuster of the master that described condenser is linked to each other with described evaporimeter fluid, it is used to reduce the temperature of refrigerant;
Be used to make the device that shifts and reduce temperature from the described refrigerant of the part of described condenser; And
Be used for described temperature has been reduced the device that the refrigerant segment fluid flow is ejected into described compressor, make described temperature reduce refrigerant part and under intermediate pressure, mix, and cause described refrigerant vapor and be discharged into described refrigerant part in the described condenser by accurate at least two stages of compression with described refrigerant vapor.
2. the system as claimed in claim 1 is characterized in that: described transfer and the device that reduces temperature comprise the flexible adjuster that links to each other with condenser and compressor fluid.
3. system as claimed in claim 2 is characterized in that: described flexible adjuster comprises capillary.
4. system as claimed in claim 2 is characterized in that: described flexible adjuster comprises expansion valve.
5. system as claimed in claim 4 is characterized in that: described expansion valve comprises a heat exchanger.
6. system as claimed in claim 5 is characterized in that: described heat exchanger is an intercooler.
7. system as claimed in claim 6, it is characterized in that: described intercooler links to each other with described condenser and the flexible adjuster fluid of described master, go to the flexible adjuster of described master thereby refrigerant passes described intercooler, and with the described refrigerant part heat-shift that passes described intercooler.
8. the system as claimed in claim 1, it is characterized in that: described fluid ejection apparatus comprises fluid injection valve, it is used to control described refrigerant and partly enters flowing of described flexible adjuster.
9. system as claimed in claim 8 is characterized in that: described compressor comprises the fluid jet that is connected with fluid ejection apparatus.
10. system as claimed in claim 9 is characterized in that: described fluid ejection apparatus comprises the check-valves that is connected with described fluid jet.
11. the system as claimed in claim 1 is characterized in that: the device of described transfer and reduction temperature comprises the bypass channel that links to each other with described condenser and described flexible adjuster fluid.
12. system as claimed in claim 3 is characterized in that: the flexible adjuster of described master links to each other with described condenser fluid by first pipeline.
13. system as claimed in claim 12 is characterized in that: described first pipeline with make described condenser be connected with the bypass channel that described capillary fluid links to each other.
14. system as claimed in claim 13 is characterized in that: described capillary is near described first pipeline, so that make the refrigerant cooling of passing described first pipeline and going to the flexible adjuster of described master.
15. system as claimed in claim 14 is characterized in that: described first pipeline of described capillary coiled coil.
16. system as claimed in claim 13 is characterized in that: described downstream end capillaceous is connecting second pipeline, and described second pipeline contacts with described first pipeline, so that conduct heat between described first pipeline and described second pipeline.
17. system as claimed in claim 16 is characterized in that: described second pipeline is arranged essentially parallel to described first pipeline.
18. system as claimed in claim 16 is characterized in that: between described first pipeline and described second pipeline, have heat transfer cream to put into, conduct heat so that promote.
19. system as claimed in claim 16 is characterized in that: described second pipeline is deformed so that consistent with described first pipeline.
20. the system as claimed in claim 1 is characterized in that: the flexible adjuster of described master is an expansion valve.
21. the system as claimed in claim 1 is characterized in that: described fluid is a water.
22. the system as claimed in claim 1 is characterized in that: described thermal source is a surrounding air.
23. a method that adds hot fluid, this method comprises the following steps:
Extract heat and the cooling by evaporation agent from thermal source;
Compress described refrigerant vapor so that improve its temperature;
Sending described fluid to from the described heat that is compressed refrigerant vapor;
After above-mentioned transfer step, a part of described refrigerant is shifted and the reduction temperature;
Reduce the temperature of described refrigerant;
During described compression step, introduce described temperature and reduced the refrigerant part, under intermediate pressure, mix with described refrigerant vapor thereby make described temperature reduce the refrigerant part, and cause described refrigerant vapor and described refrigerant part by accurate at least two stages of compression; And
Discharge and describedly be compressed refrigerant so that in described transfer step, heat is sent to described fluid.
24. method as claimed in claim 23 is characterized in that: also comprise making described refrigerant reduce the return step of step to described evaporation step from described temperature.
25. method as claimed in claim 23 is characterized in that: described fluid is a water.
26. method as claimed in claim 23 is characterized in that: described thermal source is a surrounding air.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| AU2005902571A AU2005902571A0 (en) | 2005-05-19 | Heat pump system and method for heating a fluid | |
| AU2005902571 | 2005-05-19 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN1865812A true CN1865812A (en) | 2006-11-22 |
Family
ID=37424908
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNA200510125308XA Pending CN1865812A (en) | 2005-05-19 | 2005-11-15 | Heat pump system and method for heating a fluid |
Country Status (8)
| Country | Link |
|---|---|
| US (1) | US20080210768A1 (en) |
| EP (1) | EP1888976A4 (en) |
| JP (1) | JP2008541000A (en) |
| KR (1) | KR20080028371A (en) |
| CN (1) | CN1865812A (en) |
| CA (1) | CA2608688A1 (en) |
| NZ (1) | NZ563726A (en) |
| WO (1) | WO2006122367A1 (en) |
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| CN102016449B (en) * | 2008-05-02 | 2013-12-25 | 大金工业株式会社 | Refrigeration unit |
| CN106091455B (en) * | 2016-08-04 | 2018-07-10 | 青岛大学 | A kind of quasi- two stage compression refrigeration system of piston compressor intermediate injection |
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| JP2011094810A (en) * | 2009-09-30 | 2011-05-12 | Fujitsu General Ltd | Heat pump cycle apparatus |
| US8157892B2 (en) | 2010-05-17 | 2012-04-17 | Enverid Systems, Inc. | Method and system for improved-efficiency air-conditioning |
| EP2613098B1 (en) * | 2010-12-08 | 2018-03-28 | Daikin Europe N.V. | Heating |
| US8690999B2 (en) | 2011-02-09 | 2014-04-08 | Enverid Systems, Inc. | Modular, high-throughput air treatment system |
| BR112013029302A2 (en) | 2011-05-17 | 2017-03-01 | Enverid Systems Inc | carbon dioxide reduction sorbents from indoor air |
| US9328936B2 (en) | 2012-01-10 | 2016-05-03 | Enverid Systems, Inc. | Methods and systems for managing air quality and energy use in air-conditioning systems |
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-
2006
- 2006-05-18 CA CA002608688A patent/CA2608688A1/en not_active Abandoned
- 2006-05-18 NZ NZ563726A patent/NZ563726A/en not_active IP Right Cessation
- 2006-05-18 US US11/914,695 patent/US20080210768A1/en not_active Abandoned
- 2006-05-18 WO PCT/AU2006/000663 patent/WO2006122367A1/en not_active Application Discontinuation
- 2006-05-18 KR KR1020077029326A patent/KR20080028371A/en not_active Application Discontinuation
- 2006-05-18 JP JP2008511505A patent/JP2008541000A/en active Pending
- 2006-05-18 EP EP06741091A patent/EP1888976A4/en not_active Withdrawn
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102016449B (en) * | 2008-05-02 | 2013-12-25 | 大金工业株式会社 | Refrigeration unit |
| CN106091455B (en) * | 2016-08-04 | 2018-07-10 | 青岛大学 | A kind of quasi- two stage compression refrigeration system of piston compressor intermediate injection |
Also Published As
| Publication number | Publication date |
|---|---|
| JP2008541000A (en) | 2008-11-20 |
| KR20080028371A (en) | 2008-03-31 |
| US20080210768A1 (en) | 2008-09-04 |
| NZ563726A (en) | 2009-09-25 |
| EP1888976A4 (en) | 2011-02-23 |
| WO2006122367A1 (en) | 2006-11-23 |
| EP1888976A1 (en) | 2008-02-20 |
| CA2608688A1 (en) | 2006-11-23 |
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