PL389256A1 - Compressor heat pump with thermal accelerator - Google Patents
Compressor heat pump with thermal acceleratorInfo
- Publication number
- PL389256A1 PL389256A1 PL389256A PL38925609A PL389256A1 PL 389256 A1 PL389256 A1 PL 389256A1 PL 389256 A PL389256 A PL 389256A PL 38925609 A PL38925609 A PL 38925609A PL 389256 A1 PL389256 A1 PL 389256A1
- Authority
- PL
- Poland
- Prior art keywords
- working medium
- temperature
- evaporator
- compressor
- stream
- Prior art date
Links
Classifications
-
- 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
- F25B9/00—Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point
- F25B9/02—Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point using Joule-Thompson effect; using vortex effect
- F25B9/04—Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point using Joule-Thompson effect; using vortex effect using vortex effect
-
- 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
- F25B41/00—Fluid-circulation arrangements
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
- Compression-Type Refrigeration Machines With Reversible Cycles (AREA)
Abstract
Przedmiotem wynalazku jest sprężarkowa pompa ciepła z akceleratorem termicznym, gdzie czynnikiem roboczym jest gaz propan- butan, który w temperaturze dolnego źródła, wynoszącej 5°C, ma prężność par na poziomie 4 barów. W obiegu czynnika roboczego, pomiędzy parownikiem (1), a sprężarką (10), umiejscowione jest urządzenie Vortex Tube (4). Czynnik roboczy w fazie ciekłej w parowniku (1) pobiera ciepło z dolnego źródła, paruje, co powoduje podniesienie ciśnienia w parowniku (1) do poziomu 4 barów. Czynnik roboczy w fazie gazowej o temperaturze 5°C i ciśnieniu 4 barów trafia za pośrednictwem zaworu regulacyjnego (2) do wejścia (3) urządzenia Vortex Tube (4), gdzie jest rozdzielany na dwa strumienie o niskim ciśnieniu, ciepły (5) o temperaturze 62°C i zimny (6) o temperaturze -35°C (stosunek objętości strumienia ciepłego do zimnego wynosi 4/6). Strumień zimny (6), poprzez zawór regulacyjny (7) i za pośrednictwem wymiennika ciepła (8) jest ocieplany do temperatury 5°C (korzystając z energii dolnego źródła), a następnie mieszany (9) ze strumieniem ciepłym (5), co w konsekwencji daje strumień czynnika roboczego trafiającego do sprężarki (10) o temperaturze 22°C. W kolejnym etapie czynnik roboczy trafia do skraplacza (11), gdzie jest skraplany i oddaje ciepło, a następnie, już w fazie ciekłej, poprzez zawór ekspansywny (12) trafia do parownika (1).The subject of the invention is a compressor heat pump with a thermal accelerator, where the working medium is propane-butane gas, which at the lower source temperature of 5°C has a vapor pressure of 4 bars. In the working medium circuit, between the evaporator (1) and the compressor (10), there is a Vortex Tube device (4). The working medium in the liquid phase in the evaporator (1) absorbs heat from the lower source, evaporates, which increases the pressure in the evaporator (1) to 4 bar. The working medium in the gaseous phase with a temperature of 5 ° C and a pressure of 4 bars goes through the control valve (2) to the inlet (3) of the Vortex Tube device (4), where it is divided into two streams of low pressure, warm (5) with a temperature 62°C and cold (6) at -35°C (the ratio of the volume of the hot to cold stream is 4/6). The cold stream (6), through the control valve (7) and through the heat exchanger (8), is warmed up to the temperature of 5°C (using the energy of the lower source), and then mixed (9) with the hot stream (5), which in consequently, it gives a stream of working medium going to the compressor (10) at a temperature of 22°C. In the next stage, the working medium goes to the condenser (11), where it is condensed and gives off heat, and then, already in the liquid phase, through the expansion valve (12) it goes to the evaporator (1).
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PL389256A PL224444B1 (en) | 2009-10-12 | 2009-10-12 | Compressor heat pump with thermal accelerator |
PCT/PL2010/000102 WO2011046458A1 (en) | 2009-10-12 | 2010-10-11 | The compression heat pump with thermal accelerator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PL389256A PL224444B1 (en) | 2009-10-12 | 2009-10-12 | Compressor heat pump with thermal accelerator |
Publications (2)
Publication Number | Publication Date |
---|---|
PL389256A1 true PL389256A1 (en) | 2011-04-26 |
PL224444B1 PL224444B1 (en) | 2016-12-30 |
Family
ID=43385623
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PL389256A PL224444B1 (en) | 2009-10-12 | 2009-10-12 | Compressor heat pump with thermal accelerator |
Country Status (2)
Country | Link |
---|---|
PL (1) | PL224444B1 (en) |
WO (1) | WO2011046458A1 (en) |
Families Citing this family (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104792055A (en) * | 2014-01-21 | 2015-07-22 | 广州九恒新能源有限公司 | Air energy carbon dioxide heat pump type drying machine |
CN104457027A (en) * | 2014-12-02 | 2015-03-25 | 苟仲武 | Improved compression heat pump working method and device |
RU2717483C2 (en) * | 2015-02-26 | 2020-03-23 | Юрий Михайлович Примазон | Vortex heat pump |
CN105783320A (en) * | 2016-05-09 | 2016-07-20 | 珠海格力节能环保制冷技术研究中心有限公司 | Air conditioner system |
CN105923674B (en) * | 2016-06-07 | 2018-12-11 | 重庆大学 | Supercritical CO2Heat pump driven double heat source seawater desalination systems |
CN108773258A (en) * | 2018-08-10 | 2018-11-09 | 大连民族大学 | Electric vehicle heating system based on vortex tube |
CN109916102A (en) * | 2019-01-21 | 2019-06-21 | 江苏白雪电器股份有限公司 | Auto-cascade cycle dual temperature system with vortex tube |
CN110530045B (en) * | 2019-07-09 | 2020-07-28 | 西安交通大学 | Transcritical CO2System multifunctional defogging and dehumidifying system and control method |
CN110530047B (en) * | 2019-07-17 | 2020-10-27 | 西安交通大学 | Double-vortex-tube-assisted transcritical CO2System and control method thereof |
CN117387239B (en) * | 2023-12-12 | 2024-05-03 | 珠海格力电器股份有限公司 | Air conditioning system and related control method |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
SU1002754A1 (en) * | 1981-06-08 | 1983-03-07 | Московское Ордена Ленина, Ордена Октябрьской Революции И Ордена Трудового Красного Знамени Высшее Техническое Училище Им. Н.Э.Баумана | Vortex-type refrigerator |
US6250086B1 (en) * | 2000-03-03 | 2001-06-26 | Vortex Aircon, Inc. | High efficiency refrigeration system |
AU2001239966A1 (en) * | 2000-03-03 | 2001-09-17 | Vai Holdings, Llc. | High efficiency refrigeration system |
JP4665856B2 (en) * | 2006-07-13 | 2011-04-06 | 株式会社富士通ゼネラル | Vortex tube and refrigerant circuit using the same |
-
2009
- 2009-10-12 PL PL389256A patent/PL224444B1/en unknown
-
2010
- 2010-10-11 WO PCT/PL2010/000102 patent/WO2011046458A1/en active Application Filing
Also Published As
Publication number | Publication date |
---|---|
PL224444B1 (en) | 2016-12-30 |
WO2011046458A1 (en) | 2011-04-21 |
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