EP1921401A2 - Procédé de récuperation de chaleur - Google Patents

Procédé de récuperation de chaleur Download PDF

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Publication number
EP1921401A2
EP1921401A2 EP07021952A EP07021952A EP1921401A2 EP 1921401 A2 EP1921401 A2 EP 1921401A2 EP 07021952 A EP07021952 A EP 07021952A EP 07021952 A EP07021952 A EP 07021952A EP 1921401 A2 EP1921401 A2 EP 1921401A2
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EP
European Patent Office
Prior art keywords
refrigerant
heat exchanger
interior
temperature
line
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.)
Granted
Application number
EP07021952A
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German (de)
English (en)
Other versions
EP1921401A3 (fr
EP1921401B1 (fr
Inventor
Alfred Lotter
Günter Haunschmidt
Berthold Stiftinger
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.)
"arneg" Kuehlmobel und Ladeneinrichtungen Produktions- U Handelsgesellschaft Mbh
Original Assignee
"arneg" Kuehlmobel und Ladeneinrichtungen Produktions- U Handelsgesellschaft Mbh
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.)
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Publication date
Application filed by "arneg" Kuehlmobel und Ladeneinrichtungen Produktions- U Handelsgesellschaft Mbh filed Critical "arneg" Kuehlmobel und Ladeneinrichtungen Produktions- U Handelsgesellschaft Mbh
Publication of EP1921401A2 publication Critical patent/EP1921401A2/fr
Publication of EP1921401A3 publication Critical patent/EP1921401A3/fr
Application granted granted Critical
Publication of EP1921401B1 publication Critical patent/EP1921401B1/fr
Not-in-force legal-status Critical Current
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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
    • F25B29/00—Combined heating and refrigeration systems, e.g. operating alternately or simultaneously
    • F25B29/003—Combined heating and refrigeration systems, e.g. operating alternately or simultaneously of the compression type system
    • 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
    • F25B2400/07—Details of compressors or related parts
    • F25B2400/075—Details of compressors or related parts with parallel compressors
    • 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
    • F25B2400/22—Refrigeration systems for supermarkets
    • 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
    • F25B2700/00—Sensing or detecting of parameters; Sensors therefor
    • F25B2700/21—Temperatures
    • F25B2700/2106—Temperatures of fresh outdoor air
    • 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
    • F25B40/00—Subcoolers, desuperheaters or superheaters
    • F25B40/04—Desuperheaters
    • 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
    • F25B49/00—Arrangement or mounting of control or safety devices
    • F25B49/02—Arrangement or mounting of control or safety devices for compression type machines, plants or systems
    • F25B49/027—Condenser control arrangements

Definitions

  • the invention relates to a method for heat recovery in a refrigeration system and a refrigeration system with heat recovery.
  • refrigerated cabinets which can be subdivided into refrigeration units for normal refrigeration for a temperature range of +2 to + 6 ° C and refrigerated cabinets for freezing for temperatures around -18 ° C.
  • the refrigerated cabinets are often part of a refrigeration system.
  • the individual refrigeration units or cooling points are supplied via a pipe network with refrigerant.
  • the systems are designed as composite systems in which a pressure line and a condenser for the cooling points of both the normal cooling and the deep-freezing are provided.
  • a corresponding refrigeration system to be created.
  • the object is achieved by a method having the features of claim 1 or a refrigeration system having the features of claim 11.
  • the inventive method for heat recovery in a refrigeration system uses a portion of the heat of the guided in a pressure line coolant for heating the interior of a building.
  • the refrigeration system comprises a compressor device, a condenser connected thereto via the refrigerant pressure line and equipped with a ventilation device, at least one evaporator arranged in the interior of the building and serving as a cooling point, and an outside heat exchanger arranged outside the building.
  • the provision of the heat takes place by means of an interior heat exchanger, which is connected to the pressure line and arranged with respect to the flow direction of the refrigerant in front of the condenser.
  • the inventive method is characterized in that depending on at least the outside temperature, a part of the guided in the pressure line refrigerant is passed through the outdoor heat exchanger to the compressor device and thereby absorbs heat from the ambient air of the outer space.
  • the ambient air of the outer space is extracted by a heat exchanger arranged outside the building heat and fed to the refrigerant.
  • the ambient air is thus withdrawn under energy expense heat that is used to heat the building interior.
  • the outdoor heat exchanger is connected in parallel to the cooling points of the refrigeration system and ultimately acts as another cooling point or heat pump, which introduces additional heat output into the refrigerant circuit.
  • this heat is not taken from the building interior, as is the case with an indoor cooling point.
  • the commissioning of the outdoor heat exchanger as a heat pump takes place at least as a function of the outside temperature, for example, when a predetermined outdoor temperature is reached.
  • the ventilation device of the capacitor is at least partially deactivated as a function of at least the interior temperature of the building.
  • the ventilation device is completely or partially switched off or down depending on the heat request, thereby ultimately reducing the effective capacitor area and slightly increasing the temperature and pressure levels inside the condenser.
  • the refrigerant condenses in the indoor heat exchanger at least partially, whereby an adjustable additional heat output can be dissipated in the building interior and therefore is no longer discharged on the capacitor as pure heat loss.
  • the effective opening cross-section of a pressure regulating throttle arranged in the pressure line is changed as a function of at least the interior temperature in order to allow additional heat dissipation into the building interior.
  • the pressure regulating throttle is arranged behind the interior heat exchanger with respect to the flow direction of the refrigerant, wherein it may be located in front of or behind the condenser.
  • a back pressure is generated, whereby the condensation of the refrigerant in the indoor heat exchanger is assisted. Controlled throttling makes it possible to provide additional heat output for heating the building interior.
  • the part of the refrigerant that is guided as a function of at least the outside temperature by the outside heat exchanger can be supplied to at least one of a plurality of compressors of the compressor device.
  • This compressor can be decoupled from the suction side of the other compressor of the compressor device. This compressor is then available for heat pump operation of the outdoor heat exchanger.
  • the use of a compressor of the compressor device to provide additional heat output allows efficient utilization of the installed compressor capacity.
  • the compressor capacity is necessarily designed for high summer outdoor temperatures where high cooling capacities have to be provided. In winter, on the other hand, only part of the capacity is used. This power reserve is utilized by the method according to the invention for the building heating required in winter.
  • control and regulation method according to the invention preferably takes place in several stages:
  • the ventilation device of the condenser can be partially deactivated when the outside temperature falls below a first outside temperature threshold. As a result, it is achieved that the refrigerant in the interior heat exchanger at least partially condenses. The resulting heat is dissipated to the interior of the building.
  • an indoor temperature set point or a set flow temperature setpoint of a building heater is not reached and the outdoor temperature falls below a second outdoor temperature threshold that is lower than the first outdoor temperature threshold, may be in an optional further step, the effective opening area of the pressure regulating throttle to be changed.
  • the pressure in the indoor heat exchanger can be raised when additional heat needs to be provided for heating. This pressure increase leads to increased condensation of the coolant in the interior heat exchanger.
  • a part of the guided in the pressure line refrigerant through the outdoor heat exchanger to be passed.
  • the suction side of the at least one compressor of the compressor device is decoupled from the suction side of the other compressor and connected to the outdoor heat exchanger.
  • the outdoor heat exchanger is then used as described above as an additional evaporator which extracts heat from the ambient air of the outdoor space.
  • the heat pump operation of the outdoor heat exchanger can also be done independently of the pressure control by the pressure control throttle.
  • electrical heating means for heating the interior of the building or a buffer memory are switched on when the indoor temperature setpoint or the flow temperature setpoint is not reached and the outdoor temperature fourth outside temperature threshold, which is lower than the third outside temperature threshold.
  • a hot gas defrosting of the outdoor heat exchanger is provided.
  • the refrigerant pressure line is removed at a point in front of the condenser refrigerant and passed through the outdoor heat exchanger.
  • the refrigerant contained in the outdoor heat exchanger is exhausted from the compressor device via a throttle line.
  • the throttle line has a smaller cross-section than a refrigerant suction line connecting the outdoor heat exchanger with the suction line of the compressor device in the heat pump operation of the outdoor heat exchanger.
  • the branched hot gas is thus directed against the direction selected in the heat pump mode by the outdoor heat exchanger and ultimately fed to the refrigerant circuit on the pressure side again.
  • refrigerant Upon completion of the de-icing, refrigerant is at an unknown temperature level in the outdoor heat exchanger. In a transition to the heat pump operation could therefore be caused in the outer space heat exchanger associated compressor liquid hammer, whereby the compressor would be damaged.
  • the throttle line however, the pressure level of the refrigerant is lowered and prevents further liquefaction of the refrigerant.
  • the sucked into the throttle line refrigerant is fed into a refrigerant suction line, which serves at least one serving as a cooling evaporator -
  • a refrigerant suction line which serves at least one serving as a cooling evaporator -
  • an evaporator for deep freezing - connects to the compressor device.
  • the extracted refrigerant is thus fed into a refrigerant flow, which comes from the cooling points, and mixed with this, so that at most a metered supply of liquid residues to the compressor takes place and the risk of liquid blows is virtually eliminated.
  • the invention further relates to a refrigeration system with heat recovery, which has a compressor device, a connected thereto via a refrigerant pressure line and equipped with a ventilation device condenser and at least one serving as a cooling evaporator, which is arranged in an interior of a building and a refrigerant suction line connected to the compressor device.
  • the refrigerant pressure line is coupled to an indoor heat exchanger for dissipating heat to the interior.
  • Serving as a cooling evaporator in the interior of the building arranged outside the building exterior heat exchanger is connected in parallel, is supplied by the heat from the ambient air to the guided in the suction refrigerant.
  • the refrigeration system according to the invention has a control device which is designed to guide a portion of the refrigerant guided in the pressure line through the outer space heat exchanger as a function of at least the outside temperature.
  • a pressure regulating throttle is arranged in the pressure line, whose effective opening cross section is variably adjustable.
  • a refrigerant suction line of the outdoor heat exchanger through a throttle line with a refrigerant suction line is coupled, which connects at least one serving as a cooling evaporator - in particular an evaporator for deep freezing - with the compressor device.
  • the compressor device may comprise a plurality of compressors, wherein at least one compressor is selectively connectable to the refrigerant suction line of the at least one evaporator or to the refrigerant suction line of the outdoor heat exchanger.
  • control device is also designed such that, depending on at least the interior temperature, the ventilation device of the condenser is at least partially deactivatable and / or the effective opening cross section of the pressure control throttle is controllable.
  • the refrigeration system 10 comprises a compressor device 16 which has five compressors 18a, 18a ', 18b, 18b' and 18c.
  • the compressors 18a and 18a ' are connected to a deep-freeze suction line 20 and assigned to the deep-freezing point 12.
  • the compressors 18b and 18b ' are connected by a normal cooling suction line 22 to the normal cooling point 14.
  • the compressor 18c is also connected to the normal cooling suction line 22, but can be separated from it by the controllable solenoid valve MV1.
  • the refrigerant supplied via the suction lines 20, 22 of the compressor device 16 in a gaseous state is compressed by the compressors 18a, 18a ', 18b, 18b' and 18c and passed through the pressure line 24 to an indoor heat exchanger 26.
  • the indoor heat exchanger communicates via a buffer storage line 28 with a buffer memory 30 in connection.
  • the buffer tank 30 contains water that can be used for heating the interior of the building in which the cooling points 12, 14 are installed.
  • a heating cartridge 32 is arranged in the buffer memory 30, but it is also possible to provide a plurality of heating cartridges 32.
  • a pressure regulating throttle 34 is arranged in a second pressure line 24 '.
  • the pressure regulating throttle 34 allows the regulation of the pressure level of the refrigerant in the pressure line 24 '.
  • the pressure line 24 'establishes a connection between the interior heat exchanger 26 and a condenser 36 with a ventilation device 38.
  • the pressure and temperature level in the condenser 36 can be influenced by the ventilation device 38.
  • a refrigerant collector 40 is provided in the flow direction of the coolant behind the condenser 36.
  • the refrigerant collector 40 is in turn connected by a refrigerant line 42 to the cooling points 12, 14.
  • the refrigerant line 42 has a connection to an outside of the building arranged outdoor heat exchanger 44, which can be interrupted by a valve V.
  • the dashed rectangle around the exterior heat exchanger 44 makes it clear that this is not in the interior of the building in which the cooling points 12, 14 are installed.
  • the outdoor heat exchanger 44 communicates with the compressor 18c via a heat exchanger suction line 46.
  • the heat exchanger suction line 46 has a solenoid valve MV2, through which the connection between the outdoor heat exchanger 44 and the compressor 18c can be interrupted.
  • a throttle line 48 Between the heat exchanger suction line 46 and the normal cooling suction line 20 is a compound which is formed by a throttle line 48, wherein the cross section of the throttle line 48 is smaller than the cross section of the heat exchanger suction line 46. Further, there is between the heat exchanger suction line 46 and the pressure line 24 a hot gas connection 50. Solenoid valves MV3 and MV4 allow the throttle line 48 and the hot gas connection 50 to close.
  • the compressors 18a and 18a 'and the compressors 18b, 18b' and 18c form two groups of compressors. Since the cooling points 12, 14 operate at different temperature levels, there are also different pressures in the suction lines 20, 22. This circumstance is taken into account by the formation of the separate compressor groups.
  • a heater pump not shown, is turned on, so that heating water of the buffer memory 30 flows through the indoor heat exchanger 26. In this case, 26 heat of dissipation of the refrigerant is discharged to the heating water in the indoor heat exchanger.
  • the ventilation device 38 is down-regulated or completely deactivated, whereby the effective capacitor area is reduced and the temperature level and the pressure level in the pressure line 24 'are slightly increased.
  • the refrigerant in the indoor heat exchanger 26 at least partially condenses. The resulting heat benefits the heating of the building.
  • the next step in increasing the heat output is to extract heat in a heat pump operation from the ambient air in the exterior of the building and supply it to the refrigerant circuit.
  • the solenoid valve MV 1 are closed and the solenoid valve MV2 and the valve V open.
  • the refrigeration system ultimately comprises three evaporators, wherein the outdoor heat exchanger 44, in contrast to the cooling points 12, 14 takes heat from the outer space of the building and supplies the refrigerant circuit.
  • the three different temperature and pressure levels of the suction lines 20, 22, 46 are each associated with their own compressor 18c or compressor groups 18a, 18a 'and 18b, 18b'.
  • the compressor capacity not required at low outside temperatures T A is thus used in this stage in a heat pump operation for heating the building. On a conventional building heating can therefore be dispensed with.
  • the solenoid valve MV2 and the valve V are closed and the solenoid valve MV1 is opened.
  • the compressor 18c then works again in conjunction with the compressors 18b and 18b '.
  • the outdoor heat exchanger 44 may be de-iced by hot gas as needed or at fixed intervals, particularly prior to its use in heat pump operation.
  • the solenoid valves MV1 and MV2 closed and the compressor 18c thus dissolved out of the normal cooling point 14 associated compressor group.
  • the solenoid valve MV4 in the hot gas connection 50 and the valve V are opened, whereby now hot gas from the pressure line 24 is directed against the flow direction in heat pump operation by the outdoor heat exchanger 44 until an end of the defrosting process is reached.
  • the valve V is formed by an electrically controllable solenoid valve and a check valve connected in parallel in a bypass line, wherein the check valve opens against the flow direction in the heat pump mode, ie, the check valve opens passively.
  • solenoid valve MV4 and valve V are closed, and solenoid valve MV3 in choke line 48 is opened, thereby establishing communication with vacuum refrigeration line 20.
  • the refrigerant used for deicing is sucked off and the pressure in the outdoor heat exchanger 44 is lowered to a desired value.
  • the fans of the outdoor heat exchanger 44 run.
  • the solenoid valve MV3 is closed.
  • the solenoid valve MV2 and the valve V are then opened.
  • the compressor 18c starts its work and compresses the refrigerant coming from the outdoor heat exchanger.
  • step 110 After the start of the control in step 100, a query is made in step 110 as to whether the outside temperature T A is lower than 18 ° C. If this is not the case (N), the system returns to step 100.
  • a heating pump is turned on in step 120.
  • the indoor heat exchanger 26 now outputs heat of enhancement to the heating water.
  • a target condensation temperature T K is automatically raised from 28 ° C (summer operation) to 32 ° C (transitional period) in step 125. As a result, the operation of the ventilation device 38 of the capacitor 36 is influenced.
  • step 130 it is queried whether the outside temperature T A falls below a second threshold value of 15 ° C. If the outside temperature T A is higher, it is returned to step 110, that is, it is again checked whether the outside temperature T A is less than 18 ° C. If appropriate, the heating pump remains switched on (step 120), and the target condensation temperature T K remains at the raised value (32 ° C., step 125). On the other hand, if it is determined in step 130 that the outside temperature T A is lower than 15 ° C, the target condensing temperature T K is raised to 38 ° C. A control device the cooling system 10 attempts in step 135 by raising the nominal condensation temperature T K to reach a flow temperature Tv of 35 ° C. If an interior temperature T I at 22 ° C, the desired flow temperature Tv is slid by up to 3 K slidably.
  • step 140 it is checked whether the outside temperature T A is smaller than 10 ° C, returning to step 130, if not, that is, the state of step 135 is maintained if necessary. If the outside temperature T A is below, the control device tries in step 145, depending on the interior temperature T I and the outside temperature T A, the required flow temperature Tv of 35 ° C to 45 ° C by controlling the pressure control throttle 34 and by raising the target condensation temperature T K to reach.
  • a compressor 18c is cold-separated from the compressor unit associated with the normal refrigeration units 14 of the refrigeration system 10. This compressor then operates in step 160 in heat pump operation in conjunction with the outdoor heat exchanger 44.
  • the solenoid valve MV 1 are closed and the solenoid valve MV2 and the valve V open.
  • the solenoid valves MV1 and MV2 are closed in step 200, and the solenoid valve MV4 and the valve V are opened. Heated refrigerant can now be passed through the outdoor heat exchanger 44 until a defrost end temperature Tw of about + 8 ° C is reached, which is queried in step 210.
  • the solenoid valves MV4 and V are closed and the solenoid valve MV3 is opened in step 220, which leads to a suction of the refrigerant contained in the outdoor heat exchanger 44. Suction is continued until a pressure threshold P of about 1.8 bar in the heat exchanger suction line 46 coming from the outdoor heat exchanger 44 is reached (step 225). As already explained above, when the pressure threshold value is reached, the suction process is ended in step 230, i. H. the solenoid valve MV3 is closed, the solenoid valves MV2 and V are opened, and the compressor 18c connectable to the outdoor heat exchanger 44 is released. This completes the hot gas defrost.
  • step 250 the compressor 18c is briefly turned off while the solenoid valve MV2 closed and the solenoid valve MV1 are opened, whereby the compressor 18c is again associated with the normal cooling point 14.
  • step 170 it is checked in step 170 whether the outside temperature T A is lower than -10 ° C. If the outside temperature T A falls below this value and the desired flow temperature Tv or the interior temperature T I is not reached (step 180), the heat pump operation is continued in step 185, ie the state according to step 230 of FIG. 3 is maintained, and time-delayed in step 190, a heating cartridge 32 is switched on to heat the heating water. It can be provided that several heating cartridges can be switched on as needed.
  • connection of the outdoor heat exchanger 44 can also be done without the prior regulation of the condensation temperature by the ventilation device 38 and / or the dynamic pressure control by means of the pressure control throttle 34.

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Air Conditioning Control Device (AREA)
  • Other Air-Conditioning Systems (AREA)
EP20070021952 2006-11-13 2007-11-12 Procédé de récuperation de chaleur Not-in-force EP1921401B1 (fr)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
AT18702006A AT504135B1 (de) 2006-11-13 2006-11-13 Verfahren zur wärmerückgewinnung

Publications (3)

Publication Number Publication Date
EP1921401A2 true EP1921401A2 (fr) 2008-05-14
EP1921401A3 EP1921401A3 (fr) 2009-12-16
EP1921401B1 EP1921401B1 (fr) 2014-01-08

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EP20070021952 Not-in-force EP1921401B1 (fr) 2006-11-13 2007-11-12 Procédé de récuperation de chaleur

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EP (1) EP1921401B1 (fr)
AT (1) AT504135B1 (fr)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2933484A1 (fr) * 2008-07-03 2010-01-08 2F2C Procede de refrigeration d'au moins un meuble et/ou une chambre frigorifique et de chauffage d'au moins un local, installation et echangeur de chaleur pour sa mise en oeuvre
EP2187148A1 (fr) * 2008-11-18 2010-05-19 Weska Kälteanlagen Gmbh Installation de refroidissement
NL2003228C2 (nl) * 2009-07-17 2011-01-18 Erney Errol Pinas Werkwijze voor het koppelen van een primair warmtepompsysteem bestemd voor het verwarmen van een gebouw en/of voor het verwarmen van tapwater aan een of meerdere secundaire warmtepompsystemen bestemd voor het verlagen van de temperatuur in een afgesloten ruimte en inrichting voor het uitvoeren van de werkwijze.
WO2014095290A1 (fr) * 2012-12-17 2014-06-26 Robert Bosch Gmbh Système de pompe à chaleur et procéder pour faire fonctionner un système de pompe à chaleur
CN108716771A (zh) * 2018-06-07 2018-10-30 威海双信节能环保设备有限公司 工业废水余热复叠热功转换装置及方法
CN114087800A (zh) * 2021-11-22 2022-02-25 百尔制冷(无锡)有限公司 一种全自动热回收的并联机组及其热回收方法

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Publication number Priority date Publication date Assignee Title
DE102009029392A1 (de) * 2009-09-11 2011-03-24 WESKA Kälteanlagen GmbH Explosionsgeschützte Kälteanlage mit brennbarem Kältemittel

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EP0473286A2 (fr) 1990-08-30 1992-03-04 Union Kogyo Kabushiki Kaisha Dispositif et procédé pour réchauffage et sa réfrigération par un réfrigérant

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FR2539495A2 (fr) 1974-06-26 1984-07-20 Seitha Procede et dispositif de regulation d'un systeme frigorifique destine a une production de froid et de chaleur
EP0473286A2 (fr) 1990-08-30 1992-03-04 Union Kogyo Kabushiki Kaisha Dispositif et procédé pour réchauffage et sa réfrigération par un réfrigérant

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2933484A1 (fr) * 2008-07-03 2010-01-08 2F2C Procede de refrigeration d'au moins un meuble et/ou une chambre frigorifique et de chauffage d'au moins un local, installation et echangeur de chaleur pour sa mise en oeuvre
WO2010001071A3 (fr) * 2008-07-03 2010-04-08 2F2C Installation de réfrigération d'au moins un meuble et/ou une chambre frigorifique et de chauffage d'au moins un local, et échangeur de chaleur à air pour cette installation
EP2187148A1 (fr) * 2008-11-18 2010-05-19 Weska Kälteanlagen Gmbh Installation de refroidissement
NL2003228C2 (nl) * 2009-07-17 2011-01-18 Erney Errol Pinas Werkwijze voor het koppelen van een primair warmtepompsysteem bestemd voor het verwarmen van een gebouw en/of voor het verwarmen van tapwater aan een of meerdere secundaire warmtepompsystemen bestemd voor het verlagen van de temperatuur in een afgesloten ruimte en inrichting voor het uitvoeren van de werkwijze.
WO2011008089A1 (fr) 2009-07-17 2011-01-20 Erney Errol Pinas Procédé de raccord d'un système de pompe à chaleur primaire destiné à chauffer un bâtiment et/ou à chauffer une eau de robinet avec un ou plusieurs systèmes de pompe à chaleur secondaires destinés à abaisser la température dans un espace clos et dispositif pour mettre en œuvre le procédé
WO2014095290A1 (fr) * 2012-12-17 2014-06-26 Robert Bosch Gmbh Système de pompe à chaleur et procéder pour faire fonctionner un système de pompe à chaleur
CN108716771A (zh) * 2018-06-07 2018-10-30 威海双信节能环保设备有限公司 工业废水余热复叠热功转换装置及方法
CN108716771B (zh) * 2018-06-07 2023-05-19 威海双信节能环保设备有限公司 工业废水余热复叠热功转换装置及方法
CN114087800A (zh) * 2021-11-22 2022-02-25 百尔制冷(无锡)有限公司 一种全自动热回收的并联机组及其热回收方法
CN114087800B (zh) * 2021-11-22 2023-03-10 百尔制冷(无锡)有限公司 一种全自动热回收的并联机组及其热回收方法

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AT504135B1 (de) 2008-03-15
EP1921401A3 (fr) 2009-12-16
EP1921401B1 (fr) 2014-01-08

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