WO1981001607A1 - Procede d'obtention de chaleur pour le chauffage et dispositif de mise en oeuvre de ce procede - Google Patents

Procede d'obtention de chaleur pour le chauffage et dispositif de mise en oeuvre de ce procede Download PDF

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Publication number
WO1981001607A1
WO1981001607A1 PCT/CH1980/000145 CH8000145W WO8101607A1 WO 1981001607 A1 WO1981001607 A1 WO 1981001607A1 CH 8000145 W CH8000145 W CH 8000145W WO 8101607 A1 WO8101607 A1 WO 8101607A1
Authority
WO
WIPO (PCT)
Prior art keywords
heat
heating
evaporator
medium
working medium
Prior art date
Application number
PCT/CH1980/000145
Other languages
German (de)
English (en)
Inventor
H Koppitz
H Spath
Original Assignee
Wemac Finanz & Handelsanstalt
H Koppitz
H Spath
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Wemac Finanz & Handelsanstalt, H Koppitz, H Spath filed Critical Wemac Finanz & Handelsanstalt
Priority to AU64876/80A priority Critical patent/AU6487680A/en
Publication of WO1981001607A1 publication Critical patent/WO1981001607A1/fr

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B30/00Heat pumps
    • F25B30/02Heat pumps of the compression type

Definitions

  • the invention relates to a method for obtaining heating heat, in which heat is extracted from a vaporous working medium brought to a higher temperature by compression for heating purposes, the medium being condensed, expanded, evaporated and compressed again.
  • the evaporation of the working medium is accomplished by supplying heat from the environment. The heat is taken from the ambient air, the ground or water.
  • the known methods cannot be used where heat cannot be removed from the surroundings to an adequate extent, such as, for example, B. in cities.
  • the invention aims to provide a method in which the supply of external heat to evaporate the working medium can be dispensed with in whole or in part. According to the invention, this is achieved in such a way that all or part of the heat required to evaporate the relaxed medium is removed from the compressed medium. At least part of the heat given off during its condensation is expediently used for the evaporation of the working medium.
  • the invention also relates to a device for carrying out the method, in which the working medium is recirculated from an evaporator via a compressor, heat exchanger and a throttle to the evaporator.
  • a condenser is arranged between the heat exchanger that absorbs the heat and the throttle, which is connected to the evaporator via the additional circuit of an auxiliary medium.
  • Fig. 1 is a schematic diagram of a first embodiment of the invention.
  • Fig. 2 is a schematic diagram of another embodiment of the invention.
  • Part of the basic scheme according to FIG. 1 corresponds to that of a conventional heat pump.
  • a compressor 1 draws in vaporous working medium of the usual type coming from the evaporator 2 and compresses this steam, as a result of which it is overheated. When working medium, it can be.
  • heat is extracted from the working medium and, after its condensation, it is fed to a storage container 4. From there it returns to the evaporator 2 via a throttle 5.
  • This known circuit is partly drawn in dashed lines in the basic scheme according to FIG. 1 and corresponds to an operating state in which the valves 6 and 8 are open and the valves 7 and 9 are closed.
  • the evaporator 2 would have to be supplied with heat from the outside to evaporate the medium.
  • the heat exchanger 3 would then Overheating and condensation heat of the medium is dissipated by the heating circuit 10 in which the circulation pump 11 is arranged.
  • a separate condenser 12 is now connected between the heat exchanger 3 and the throttle 5, it being possible for the direct, dashed line connection between the heat exchanger 3 on the one hand and the throttle 5 and the reservoir 4 on the other hand to be omitted.
  • a partial condensation of the working medium takes place in the heat exchanger 3. Essentially, however, the condensation in the. Capacitor 12 made.
  • the heat exchanger 3 When the system starts up at low temperatures (first start-up), the heat exchanger 3 is switched off by opening the valve 7 and closing the valve 6, and the superheated medium is fed directly to the condenser 12 in order to provide sufficient heat for the provide vaporization of the working medium. As soon as the intended operating temperatures have been reached, the heat exchanger 3 is switched on and the system now works in a stationary state. The superheat of the working medium coming from the evaporator and part of its heat of condensation can now be taken as useful heat from the heat exchanger 3 and supplied to a consumer by the heating circuit 12.
  • the additional capacitor 12 makes it possible to create ideal working conditions for carrying out the method.
  • the working medium is optimally cooled in front of the throttle 5, and the heat of condensation obtained in the condenser 12 is fed to the evaporator 2 via the auxiliary circuit 13. Since no or only partial external heat is required for evaporation, the method according to the invention can be used universally.
  • the device can be regulated in accordance with the output.
  • the mixing valve 15 the auxiliary Circuit 13 optimally regulated depending on the compressor output and the amount of heat carried away in the heating circuit 10, so that both the evaporator 2 and the condenser 12 operate in the intended temperature ranges.
  • the method is also suitable for using heat loss from other systems, especially cooling systems or cooling devices, to evaporate the working medium.
  • a basic diagram of a device which accomplishes this is shown in FIG. 2.
  • a branch line 16 is provided after the condenser 12, upstream of the valve 9, which leads via a valve 17 to a second throttle 18 and to the evaporator of the cooling device 19 and finally to the suction line 20 of the compressor 1.
  • the valve 17 is also opened, the working medium is evaporated both in the evaporator 2 and in the evaporator of the cooling device as long as the required evaporation temperature of the cooling device is not exceeded.
  • the evaporation rate in the evaporator 2 and thus the condensation of the working medium in the condenser 12 can therefore be reduced.
  • the proportion of condensation in the heat exchanger 3 is thus greater, so that an increased heat output can be taken from it. If the performance of the cooling device 19 is sufficiently high, the valve 9 can optionally be completely closed and the condensation can be carried out entirely in the heat exchanger 3. For example, B. by the inventive method, the heat of condensation of cooling devices and cooling systems in the household can be used for the treatment of hot service water.
  • an injector 23 is arranged in the heating circuit 10. This has a similar regulating function to the mixing valve 15.
  • the injector 23 ensures that, depending on the temperature of the medium circuit, part of the heating circuit passes directly from the flow 21 into the return 22. This prevents excessive cooling of the medium circuit at low temperatures. The injector becomes ineffective at higher temperatures. The injector works automatically depending on the heating circuit temperature and does not require any external force to operate it.

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Central Heating Systems (AREA)

Abstract

Par ce procede, on obtient de la chaleur pour le chauffage, au moyen de la compression, a haute temperature, d'un fluide de travail sous forme de vapeur. Le fluide est ainsi condense, detendu, vaporise et a nouveau comprime. La chaleur necessaire a la vaporisation du fluide detendu est prelevee totalement ou en partie du fluide comprime. Conformement au but, au moins une partie de la chaleur cedee lors de la condensation est utilisee pour la vaporisation du fluide de travail. On peut renoncer entierement ou en partie a l'utilisation de chaleur exterieure pour la vaporisation du fluide de travail.
PCT/CH1980/000145 1979-12-03 1980-12-01 Procede d'obtention de chaleur pour le chauffage et dispositif de mise en oeuvre de ce procede WO1981001607A1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AU64876/80A AU6487680A (en) 1979-12-03 1980-12-01 Process for obtaining heat for heating and device for implementing such process

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
AT764479 1979-12-03
AT7644/79 1979-12-03

Publications (1)

Publication Number Publication Date
WO1981001607A1 true WO1981001607A1 (fr) 1981-06-11

Family

ID=3598135

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/CH1980/000145 WO1981001607A1 (fr) 1979-12-03 1980-12-01 Procede d'obtention de chaleur pour le chauffage et dispositif de mise en oeuvre de ce procede

Country Status (2)

Country Link
EP (1) EP0041957A1 (fr)
WO (1) WO1981001607A1 (fr)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0061349A2 (fr) * 1981-03-25 1982-09-29 Thomas H. Hebert Dispositif et méthode de transfert thermique pour pré- et sous-refroidir et condensateur à cet effet

Citations (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR792390A (fr) * 1935-07-12 1935-12-30 Delas Mode de chauffage et de réfrigération des locaux au moyen de pompes de chaleur
US2462557A (en) * 1947-10-08 1949-02-22 Carl M Santee Heat pump means for controlling the temperature of the walls of a room
DE1102187B (de) * 1957-03-05 1961-03-16 Heat Pump & Refrigeration Ltd Waermepumpenanlage
CH560360A5 (fr) * 1973-10-16 1975-03-27 Ledermann Hugo
FR2280039A1 (fr) * 1974-07-24 1976-02-20 Alsthom Cgee Machine thermodynamique fonctionnant en pompe de chaleur
DE2540813A1 (de) * 1974-09-13 1976-04-01 Amour Floride Nieto Waermepumpe
DE2509065A1 (de) * 1975-03-01 1976-09-09 Volkswagenwerk Ag Gehaeuseartige anordnung zur schalldaempfung
DE2525643A1 (de) * 1975-06-09 1976-12-16 Baelz Gmbh Helmut Warmwasserheizungs- oder -bereitungsanlage
FR2338465A1 (fr) * 1976-01-15 1977-08-12 Multifluid En Procede et dispositif de chauffage et de refrigeration
DE2620133A1 (de) * 1976-05-07 1977-11-24 Bosch Gmbh Robert Einrichtung zum beheizen oder kuehlen von raeumen
DE2655513A1 (de) * 1976-12-08 1978-06-15 Vaillant Joh Kg Regeleinrichtung
DE2758737A1 (de) * 1977-12-29 1979-07-05 Siemens Ag Verfahren zum betreiben einer waermepumpe
EP0003723A2 (fr) * 1978-01-31 1979-08-22 Sintab Swedinventor Ab Procédé et dispositif de chauffage par pompe à chaleur
EP0006612A2 (fr) * 1978-06-28 1980-01-09 McCord, James W. Appareil générateur et récupérateur de vapeur

Patent Citations (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR792390A (fr) * 1935-07-12 1935-12-30 Delas Mode de chauffage et de réfrigération des locaux au moyen de pompes de chaleur
US2462557A (en) * 1947-10-08 1949-02-22 Carl M Santee Heat pump means for controlling the temperature of the walls of a room
DE1102187B (de) * 1957-03-05 1961-03-16 Heat Pump & Refrigeration Ltd Waermepumpenanlage
CH560360A5 (fr) * 1973-10-16 1975-03-27 Ledermann Hugo
FR2280039A1 (fr) * 1974-07-24 1976-02-20 Alsthom Cgee Machine thermodynamique fonctionnant en pompe de chaleur
DE2540813A1 (de) * 1974-09-13 1976-04-01 Amour Floride Nieto Waermepumpe
DE2509065A1 (de) * 1975-03-01 1976-09-09 Volkswagenwerk Ag Gehaeuseartige anordnung zur schalldaempfung
DE2525643A1 (de) * 1975-06-09 1976-12-16 Baelz Gmbh Helmut Warmwasserheizungs- oder -bereitungsanlage
FR2338465A1 (fr) * 1976-01-15 1977-08-12 Multifluid En Procede et dispositif de chauffage et de refrigeration
DE2620133A1 (de) * 1976-05-07 1977-11-24 Bosch Gmbh Robert Einrichtung zum beheizen oder kuehlen von raeumen
DE2655513A1 (de) * 1976-12-08 1978-06-15 Vaillant Joh Kg Regeleinrichtung
DE2758737A1 (de) * 1977-12-29 1979-07-05 Siemens Ag Verfahren zum betreiben einer waermepumpe
EP0003723A2 (fr) * 1978-01-31 1979-08-22 Sintab Swedinventor Ab Procédé et dispositif de chauffage par pompe à chaleur
EP0006612A2 (fr) * 1978-06-28 1980-01-09 McCord, James W. Appareil générateur et récupérateur de vapeur

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0061349A2 (fr) * 1981-03-25 1982-09-29 Thomas H. Hebert Dispositif et méthode de transfert thermique pour pré- et sous-refroidir et condensateur à cet effet
EP0061349A3 (fr) * 1981-03-25 1983-08-03 Thomas H. Hebert Dispositif et méthode de transfert thermique pour pré- et sous-refroidir et condensateur à cet effet

Also Published As

Publication number Publication date
EP0041957A1 (fr) 1981-12-23

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