GB2077407A - Heat pump - Google Patents

Heat pump Download PDF

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Publication number
GB2077407A
GB2077407A GB8114872A GB8114872A GB2077407A GB 2077407 A GB2077407 A GB 2077407A GB 8114872 A GB8114872 A GB 8114872A GB 8114872 A GB8114872 A GB 8114872A GB 2077407 A GB2077407 A GB 2077407A
Authority
GB
United Kingdom
Prior art keywords
evaporator
conduit
heat pump
icing
air
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.)
Withdrawn
Application number
GB8114872A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Volkswagen AG
Original Assignee
Volkswagen AG
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 Volkswagen AG filed Critical Volkswagen AG
Publication of GB2077407A publication Critical patent/GB2077407A/en
Withdrawn legal-status Critical Current

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
    • F25B30/04Heat pumps of the sorption type
    • 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
    • F25B47/00Arrangements for preventing or removing deposits or corrosion, not provided for in another subclass
    • F25B47/02Defrosting cycles
    • F25B47/027Defrosting cycles for defrosting sorption type systems
    • 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
    • F25DREFRIGERATORS; COLD ROOMS; ICE-BOXES; COOLING OR FREEZING APPARATUS NOT OTHERWISE PROVIDED FOR
    • F25D21/00Defrosting; Preventing frosting; Removing condensed or defrost water
    • F25D21/02Detecting the presence of frost or condensate
    • F25D21/025Detecting the presence of frost or condensate using air pressure differential detectors

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Sorption Type Refrigeration Machines (AREA)
  • Air Conditioning Control Device (AREA)

Abstract

The heat pump provides a connection (11) for ducting hot refrigerant gas from an expeller (1) directly to an evaporator (4) of the pump under the control of a solenoid valve (12) and a throttle (13). The evaporator is equipped with an icing sensor (16) which on sensing a, predetermined degree of icing of the evaporator opens the solenoid valve to permit gas to enter the evaporator through the throttle to effect de-icing. The consequent rise in pressure in the evaporator shuts off an expansion valve (5) through which condensate from a condenser (2) of the pump is normally fed to the evaporator. <IMAGE>

Description

SPECIFICATION Heat pump The invention relates to a heat pump.
A heat pump is known comprising a device for producing a hot refrigerant vapour, a condenser connected downstream of the device, and an evaporator for the refrigerant which is provided with an air inlet conduit and an air exhaust conduit and an expansion valve.
At inlet air temperatures below approximately 80C and at a high relative air humidity, icing of the evaporator can occur which at least considerably impairs the mode of operation of the heat pump.
Consequently, the object of the invention is to construct such a heat pump in which the evaporator can be defrosted in a short time at only a low additional expense.
There is provided by the present invention a heat pump having a device for producing a hot refrigerant vapour, a condenser connected downstream of the device, and an evaporator for the refrigerant which is provided with an air inlet conduit and an air exhaust conduit and an expansion valve, wherein a conduit for hot refrigerant vapour leads from the device directly to the inlet of the evaporator and incorporates a throttle for reducing the pressure in the conduit in operation to a value, in excess of the evaporator pressure, leading to condensation, and a solenoid valve which is arranged to be operated by an icing sensor, to open the conduit only when a predetermined degree of icing of the evaporator occurs.
An advantage of the present invention resides in the low energy expenditure for de-icing which essentially involves only a direct connection conduit between the expeller or the compressor on the one hand and the evaporator on the other hand, together with two valves which, if required, can also be combined.
At this juncture, it may be mentioned that a return conduit leading from the output of a compressor and by-passing the condensor, is known from German Offenlegungsshrift 25 19 409, F24J 3/00. However, in the latter instance, this conduit serves to supply superheated steam to the evaporator downstream of the heat exchanger, and to the compressor upstream of the heat exhanger, the steam being condensed at this location and then being fed to a flow medium reservoir, connected upstream of the evaporator, for the refrigerant. Thus, this known heat pump neither seeks to solve the problem on which the invention is based, nor is this problem automatically solved.
Also, German Offenlegungsschrift 27 36 434, F24J, 3/04 may be mentioned which describes an arrangement in which, in contrast to the present invention, the hot gas is carried in processing conduits and in a by-pass around a throttle.
Defrosting is effected by cooling the hot gas, and not by condensation, the defrosting performance being low with the acceptance of losses in the cold exchanger.
An embodiment of the invention will be further described hereinafter with reference to the accompanying drawing, in which the sole Figure is a schematic diagram of an embodiment of the invention.
Referring to the Figure, the conduits for gaseous or vaporized refrigerant, NH3 in the present instance, are indicated by two parallel solid lines, the conduits for liquid refrigerant are indicated by one solid line. Conduits for weak solution are shown by a solid line having dots, and conduits for rich solution are shown by dash-dot lines. Heating water conduits are indicated by lines which are broken at large distances apart, and air conduits are indicated by lines which are broken at short distances apart.
The absorption heat pump illustrated in the Figure is constructed in accordance with known principles. The not NH3 gas obtained by heat input in the expeller 1 first flows into the condenser 2 in which heat is transferred to the heating water.
Refrigerant now in a liquid form flows from the condenser 2 by way of the cold exchanger 3 to the evaporator 4 whose chief components are the expansion valve 5 and the refrigerant/intake air heat exchanger 6. Thus, after it has expanded, the refrigerant absorbs its energy from the ambient air and consequently leaves the evaporator in the form of gas which passes through the cold exchanger 3 and flows to the absorber 7 in which the spiral 8, having the heating water flowing therethrough, effects the heat exchange with the heating water which is then fed to loads. Weak solution is also fed to the absorber 7 in addition to the gaseous refrigerant, and rich solution flows back into the expeller 1 from the absorber by way of the heat exhanger 9.
The direct conduit 11 leads to the inlet of the evaporator heat exchanger 6 from the connection conduit 10 between the expeller 1 and the condenser 2. The conduit 11, which consequently by-passes the condenser 2, incorporates two valves, that is to say, the solenoid valve 12 and the throttle 1 3. The differential pressure gauge 1 6 connected between the inlet air line 14 and the exhaust air line 1 5 opens the solenoid valve 12 only when a specific limiting value of the differential pressure between the conduits 1 4 and 1 5 signals the existence of troublesome icing in the evaporator 4.
The throttle 1 3 ensures that, when the solenoid valve 2 is open, the hot refrigerant vapour or gas then carried in the conduit 11 is only expanded up to a pressure value which lies above the previous evaporator pressure and which enables condensation above the icing temperature.
The thermal expansion valve 5 closes upon a pressure rise by the hot refrigerant gas which has flowed into the evaporator, so that the injection of condensate is stopped. When using diaphragm throttling instead of the injection valve 5, the conduit 11 has to be ciosed by, for example an additional solenoid valve.
The inlet air conduit 14 incorporates the blower 1 7 which is directly or indirectly triggered by the differential pressure gauge 1 6 and which is designed such that it assists the defrosting operation only at inlet air temperatures in excess of OOC.
A high defrosting performance and short defrosting times result from the condensation of the hot refrigerant vapour, fed through the conduit 11, in the evaporator 4. The defrosting cycle is terminated by closing of the solenoid valve 12 by, for example, a time delay. When the evaporator pressure then drops, the condensate produced in the evaporator is then completely evaporated again. The expansion valve 5 opens automatically towards the end of this evaporation process, and the heat pumping process is resumed.
Condensate produced during defrosting can thus remain in the evaporator, since it evaporates again later when the heat pumping operation is resumed. However, it is also possible to feed condensate directly to the absorber by a separate conduit, particularly when large quantities of condensate are produced.
Instead of the differential pressure at the evaporator, a different quantity, such as the difference between the intake air temperature and the vaporization temperature or the vaporization pressure can be detected as the characteristic quantity of the degree of icing.

Claims (5)

1. A heat pump having a device for producing a hot refrigerant vapour, a condenser connected downstream of the device, and an evaporated for the refrigerant which is provided with an air inlet conduit and an air exhaust conduit and an expansion valve, wherein a conduit for hot refrigerant vapour leads from the device directly to the inlet of the evaporator and incorporates a throttle for reducing the pressure in the conduit in operation to a value, in excess of the evaporator pressure, leading to condensation, and a solenoid valve which is arranged to be operated by an icing sensor, to open the conduit only when a predetermined degree of icing of the evaporator occurs.
2. A heat pump as claimed in claim 1, wherein the expansion valve of the evaporator shuts off when a predetermined pressure rise occurs in the evaporator as a result of the refrigerant vapour which has flowed in.
3. A heat pump as claimed in claim 1 or 2, wherein a blower is located in the inlet air conduit or exhaust air conduit and is switched off when the conduit is open and at inlet air temperatures below OOC.
4. A heat pump as claimed in any of claims 1 to 3, wherein the icing sensor is a differential pressure gauge connected between the inlet air conduit and the exhaust air conduit of the evaporator, and the solenoid valve opens the conduit only when a predetermined differential pressure occurs.
5. A heat pump substantially as hereinbefore described with reference to the accompanying drawing.
GB8114872A 1980-05-16 1981-05-15 Heat pump Withdrawn GB2077407A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE19803018706 DE3018706A1 (en) 1980-05-16 1980-05-16 HEAT PUMP

Publications (1)

Publication Number Publication Date
GB2077407A true GB2077407A (en) 1981-12-16

Family

ID=6102544

Family Applications (1)

Application Number Title Priority Date Filing Date
GB8114872A Withdrawn GB2077407A (en) 1980-05-16 1981-05-15 Heat pump

Country Status (3)

Country Link
DE (1) DE3018706A1 (en)
FR (1) FR2482711A1 (en)
GB (1) GB2077407A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0354749A2 (en) * 1988-08-09 1990-02-14 Yazaki Corporation Air-cooled absorption Air-conditioner
FR2705622A1 (en) * 1993-05-27 1994-12-02 Valeo Thermique Habitacle Method and device for heating the passenger compartment of a motor vehicle
EP3285025A1 (en) * 2016-08-18 2018-02-21 Andreas Bangheri Absorption heat pump and method for operating an absorption pump
CN108120190A (en) * 2017-11-10 2018-06-05 山东奇威特太阳能科技有限公司 A kind of method that absorption installation heat exchanger surface delays frosting

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3629440A1 (en) * 1986-08-29 1988-03-03 Absorptions Und Waermetechnik Absorption system, in particular absorption heat pump
CN108507267A (en) * 2017-09-15 2018-09-07 樊永信 A kind of solar energy defrosting system for refrigeration house suitable for indirect refrigeration system
DE102017219228A1 (en) * 2017-10-26 2019-05-02 Robert Bosch Gmbh Combined boiler operating and defrosting device

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2637983A (en) * 1950-08-22 1953-05-12 Kramer Trenton Co Refrigerating apparatus with hot gas defrosting means
US2762206A (en) * 1952-09-30 1956-09-11 Carrier Corp Defrosting arrangements for refrigeration systems
US2770104A (en) * 1953-06-15 1956-11-13 Stanley J Sweynor Defrosting evaporators in refrigeration systems
DE958845C (en) * 1953-09-05 1957-02-28 Sulzer Ag Compression refrigeration system
US3163998A (en) * 1962-09-06 1965-01-05 Recold Corp Refrigerant flow control apparatus
DE2736434A1 (en) * 1977-08-10 1979-02-22 Vaillant Joh Gmbh & Co Heat pump for heating circuit - has condenser-type heat exchanger with transducer actuated and by=pass valves
DE2854055A1 (en) * 1978-12-14 1980-07-03 Linde Ag Heat transfer medium in absorption heating system - stops supply of refrigerating medium to absorber below set temp.
DE3016532C2 (en) * 1980-04-29 1986-09-25 Buderus Ag, 6330 Wetzlar Absorption heat pump

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0354749A2 (en) * 1988-08-09 1990-02-14 Yazaki Corporation Air-cooled absorption Air-conditioner
EP0354749A3 (en) * 1988-08-09 1991-12-18 Yazaki Corporation Air-cooled absorption air-conditioner
FR2705622A1 (en) * 1993-05-27 1994-12-02 Valeo Thermique Habitacle Method and device for heating the passenger compartment of a motor vehicle
EP3285025A1 (en) * 2016-08-18 2018-02-21 Andreas Bangheri Absorption heat pump and method for operating an absorption pump
US20180051919A1 (en) * 2016-08-18 2018-02-22 Andreas Bangheri Absorption heat pump and method for operating an absorption heat pump
US10605501B2 (en) * 2016-08-18 2020-03-31 Andreas Bangheri Absorption heat pump and method for operating an absorption heat pump
CN108120190A (en) * 2017-11-10 2018-06-05 山东奇威特太阳能科技有限公司 A kind of method that absorption installation heat exchanger surface delays frosting

Also Published As

Publication number Publication date
DE3018706A1 (en) 1981-11-26
FR2482711A1 (en) 1981-11-20

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Legal Events

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WAP Application withdrawn, taken to be withdrawn or refused ** after publication under section 16(1)