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EP2606291B1 - Coolant condenser assembly - Google Patents

Coolant condenser assembly Download PDF

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Publication number
EP2606291B1
EP2606291B1 EP11745804.2A EP11745804A EP2606291B1 EP 2606291 B1 EP2606291 B1 EP 2606291B1 EP 11745804 A EP11745804 A EP 11745804A EP 2606291 B1 EP2606291 B1 EP 2606291B1
Authority
EP
European Patent Office
Prior art keywords
refrigerant
cooling tubes
supercooling
region
condenser assembly
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.)
Active
Application number
EP11745804.2A
Other languages
German (de)
French (fr)
Other versions
EP2606291A1 (en
Inventor
Guillaume David
Uwe FÖRSTER
Matthias Jung
Andreas Kemle
Christoph Walter
Herbert Hofmann
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.)
Mahle Behr GmbH and Co KG
Original Assignee
Mahle Behr GmbH and Co KG
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 Mahle Behr GmbH and Co KG filed Critical Mahle Behr GmbH and Co KG
Publication of EP2606291A1 publication Critical patent/EP2606291A1/en
Application granted granted Critical
Publication of EP2606291B1 publication Critical patent/EP2606291B1/en
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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
    • F25B39/00Evaporators; Condensers
    • F25B39/04Condensers
    • 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
    • F25B2339/00Details of evaporators; Details of condensers
    • F25B2339/04Details of condensers
    • F25B2339/044Condensers with an integrated receiver
    • 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
    • F25B2500/00Problems to be solved
    • F25B2500/01Geometry problems, e.g. for reducing size
    • 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
    • F25B40/00Subcoolers, desuperheaters or superheaters
    • F25B40/02Subcoolers
    • 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
    • F25B40/00Subcoolers, desuperheaters or superheaters
    • F25B40/04Desuperheaters
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D21/00Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
    • F28D2021/0019Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
    • F28D2021/008Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for vehicles
    • F28D2021/0084Condensers

Definitions

  • the present invention relates to a refrigerant condenser assembly according to the preambles of claim 1.
  • refrigerant condenser assemblies for a power tool air conditioning system
  • vaporous refrigerant is converted into a liquid state of aggregation and then the liquid refrigerant is further "subcooled" in a subcooling region.
  • the refrigerant condenser assembly forms part of a refrigeration circuit of an automotive air conditioning system with an evaporator, an expansion device and a compressor.
  • the DE 10 2007 018 722 A1 shows a condenser for the air conditioning system of a motor vehicle having two manifolds and a container arranged adjacent to the one collecting tube for receiving the desiccant of the refrigerant of the air conditioner.
  • the refrigeration cycle of an automotive air conditioning system is reduced by up to 10%.
  • the performance of a refrigeration circuit in a Kraftmairnastrom can be increased inter alia, that at a subcooling of the refrigerant condenser assembly, the already liquefied refrigerant is cooled more.
  • the refrigerant in gaseous form enters the refrigerant condenser assembly at an inlet port and is cooled to a saturation temperature at an overheat region. Subsequently, the refrigerant flows into a condensation region and in this the gaseous refrigerant is further cooled and liquefied. Subsequently, the liquid refrigerant flows into a subcooling region and is cooled below the boiling point, for example to a temperature of 6 or 7 K below the boiling temperature of the refrigerant. By a greater cooling of the refrigerant in the Uhterkühlungs Scheme below the boiling point of the refrigerant higher power of the refrigerant circuit can be achieved.
  • the refrigerant capacitor assembly within the motor vehicle a predetermined space, for example given by a certain depth, height and width available, so that although a greater cooling of the refrigerant at the subcooling by a larger surface at the subcooling and a larger space associated therewith
  • refrigerant condenser assembly is possible, but in general due to the predetermined dimensions of the space for the refrigerant condenser assembly no larger space is available.
  • the aim is to increase the subcooling to, for example, 15 K.
  • more cooling tubes or proportionally more area required by the capacitor This has the consequence that less space is available for the condensation area, the cooling takes place at a higher saturation temperature and the associated saturation pressure increases. This causes a negative effect on the cooling capacity in the refrigeration cycle, which reduces or even nullifies the desired advantage.
  • the object of the present invention is to provide a refrigerant condenser assembly in which the refrigerant is strongly cooled in a subcooling region of the refrigerant condenser assembly without substantially increasing the condensing pressure in the refrigerant condenser assembly.
  • a refrigerant condenser assembly for an automotive air conditioning system comprising cooling tubes for passing a refrigerant, two header tubes for fluidly connecting the cooling tubes, preferably a header with at least one overflow opening by means of which the header is in fluid communication with the cooling tubes and / or a header, the cooling tubes an overheating section for cooling the vapor refrigerant, a condensing section for condensing the refrigerant as at least a parallel section, and a subcooling section as a subcooler parallel section for cooling the liquid refrigerant, wherein the flow cross sectional areas of the cooling tubes, particularly all of the cooling tubes, of the subcooling section are smaller than the product of 0.9 or 0.7 or 0.5 and the flow cross-sectional areas of the cooling tubes, in particular of all cooling tubes, the overheating area and / or the condensation area.
  • the flow cross-sectional area is the cross-sectional area of the cooling tubes for passing the refrigerant.
  • the cooling tubes of the subcooling region thus have a smaller flow cross-sectional area than the cooling tubes of the overheating region and / or the condensation region.
  • a smaller flow cross-sectional area can be achieved, for example, by cooling tubes with a smaller cross-sectional area or by cooling tubes with the same cross-sectional area, wherein turbulence inserts in the cooling tubes of the sub-cooling area reduce the flow cross-sectional area.
  • the refrigerant can be cooled more advantageously at the subcooling, for example, to a temperature of 14 K below the boiling temperature of the refrigerant without thereby increasing the dimensions of the refrigerant condenser assembly and thus the refrigerant condenser assembly finds place in a given space of a motor vehicle.
  • the performance of a refrigeration circuit of an automotive air conditioning system can be improved and thereby the power reduction when using the new refrigerant R1234yf be at least partially compensated.
  • An increased pressure drop in the subcooling area is not detrimental to the performance of the refrigerant condenser assembly or performance reducing. This is due to the fact that the pressure drop takes place after the wet steam area, while the system's high pressure is oriented at the saturation temperature before the subcooling area or after the condensation area.
  • At least two cooling tubes act as the first subcooler in parallel with the refrigerant
  • the refrigerant flowing out of the first subcooler enters into a first subcooling passage and the first subcooling passage opens into at least two cooling tubes as the second subcooler and preferably flows into the subcooling region second subcooling parallel section into a second subcooling intermediate flow channel and the second subcooling intermediate flow channel opens into at least two cooling tubes as the third subcooler parallel section.
  • the subcooling region of the refrigerant condenser assembly is thus divided into a total of two or three subcooler parallel sections, each interconnected by the subcooling intercooler passage. As a result, the refrigerant at the subcooling region can be cooled even further below the boiling point of the refrigerant.
  • the subcooling region of the refrigerant condenser assembly is thus subdivided into a first and a second subcooler parallel section, and in the subcooler parallel sections, at least two cooling tubes are respectively hydraulically or fluid-conductively supplied in parallel with the refrigerant.
  • the refrigerant exiting from the first subcooler parallel section is introduced into and mixed in a first subcooling intermediate flow channel, and the refrigerant is introduced into the second subcooler parallel section from the first subcooling intermediate flow channel.
  • the refrigerant is conducted in parallel in the subcooling region, for example, by four, seven or nine cooling tubes.
  • the first and second subcooler parallel sections have, for example, two, three or five cooling tubes.
  • the refrigerant has a smaller flow cross-sectional area at the first and second subcooler parallel sections as in the refrigerant condenser assembly known in the art, thereby causing a larger flow velocity of the refrigerant to occur at the subcooling region and thereby improve or increase the heat transfer from the refrigerant to the air flowing around the refrigerant condenser assembly.
  • one subcooler parallel section or the subcooling region between two or eight cooling tubes acted upon in parallel and / or the surface of the cooling tubes and preferably the headers of the subcooling region is less than 50%, 40%, 35%, 30%, 25% or 15% of the surface of the heat exchanger of the refrigerant condenser assembly and in particular, the heat exchanger consists of the cooling tubes and preferably the headers.
  • At least two cooling tubes are acted upon as a first parallel section in a fluid-conducting manner in parallel.
  • the refrigerant flowing out of the first parallel section opens into a first intermediate flow channel and the first intermediate flow channel opens into at least two cooling tubes as the second parallel section.
  • a first and a second parallel section In the flow direction of the refrigerant before the first subcooler parallel section, ie before the subcooling region of the refrigerant condenser group, ie thus at the overheating region and / or at the condensation region of the refrigerant condenser assembly is thus arranged a first and a second parallel section.
  • the overheating region and / or the condensation region are subdivided into the first and second subcooler parallel sections between which the refrigerant is conducted through the first intermediate flow channel.
  • the refrigerant flowing out of the second parallel section opens into a second intermediate flow channel and the second intermediate flow channel opens into at least two cooling tubes as the third parallel section.
  • the refrigerant condenser assembly is divided into a total of three parallel sections with at least two, preferably at least four or six or eight, cooling tubes, which are each fluid-conductively connected to each other through the intermediate flow channel.
  • a parallel section has a greater number of cooling tubes than a subcooler parallel section, and preferably the number of cooling tubes of a parallel section is two, three, five or seven cooling tubes greater than the number of cooling tubes of a subcooler parallel section.
  • the second parallel section opens into a second intermediate flow channel and the second intermediate flow channel opens into the collecting container or the third parallel section opens into a third intermediate flow channel and the third intermediate flow channel opens into the collecting container.
  • the overheating and / or condensation region of the refrigerant condenser assembly has the first and second parallel sections, then the refrigerant discharged from the second parallel section is introduced into the first subcooler section, or the overheating and / or condenser section has three parallel sections, that of the third parallel section discharged refrigerant introduced into the first subcooler parallel section, wherein in each case between condensing region and subcooling of the collecting container is arranged.
  • the overheating and / or condensation region is subdivided into more than three parallel sections, for example four or five parallel sections.
  • the sum of the flow cross-sectional areas of all the cooling tubes of a subcooler parallel section is smaller than the product of 1.0 or 0.9 or 0.7 or 0.5 or 0.3 or 0.1 and the sum of the flow cross-sectional areas of all the cooling tubes of a parallel section and / or the cooling tubes are formed as flat tubes and corrugated ribs are arranged between the flat tubes.
  • the filling amount of refrigerant can be reduced.
  • the cost can be reduced.
  • the width of the cooling tubes, in particular of all cooling tubes, a subcooling parallel section or the subcooling region is smaller than the product of 1.0 or 0.9 or 0.7 or 0.5 or 0.3 or 0.1 and the width of the Cooling tubes, in particular all cooling tubes, a parallel section.
  • the heat transfer in the subcooling can also be controlled by the individual corrugated fins, which are arranged between the individual cooling tubes.
  • the corrugated fins have a different geometry in the subcooling region than the corrugated fins in the overheating region and / or condensation region.
  • the corrugated fins in the subcooling region are preferably designed such that the air-side heat transfer in this region increases or improves.
  • the corrugated fins in the subcooling region could be of the same height as in the overheating region and / or condensation region, but have a different geometry due to increased corrugated rib density or gill fields, which improves the heat transfer in this region.
  • the corrugated fins in the subcooling region could be designed with a lower height than in the overheating region and / or condensation region.
  • narrower cooling tubes could be used in the subcooling area in order to increase the flow velocity and thus the heat transfer.
  • the corrugated fins could be designed in the subcooling with a higher height than in the overheating area and / or condensation area. In this case, the air-side heat transfer would be deteriorated. However, since fewer cooling tubes are arranged in parallel on the refrigerant side, the heat transfer on the refrigerant side would increase.
  • a method for operating a refrigeration cycle of an automotive air conditioning system comprising the steps of: passing refrigerant through conduits of a refrigerant circuit, compressing the gaseous refrigerant in a compressor so that the pressure of the gaseous refrigerant is increased, cooling and condensing the gaseous refrigerant in a refrigerant condenser assembly passed through cooling tubes by cooling the gaseous refrigerant in an overheating region to a saturation temperature, then cooling and liquefying the gaseous refrigerant to a boiling temperature in a condensation region and cooling the liquid refrigerant below the boiling temperature in a subcooling region; expanding the liquid Refrigerant on an expansion device, so that the pressure of the liquid refrigerant is reduced, heating and evaporation of the refrigerant in an evaporator, Le In the subcooling region, the refrigerant flows through cooling tubes with a smaller flow cross-sectional area into the gaseous refrigerant exiting from the steps of:
  • the refrigerant in the subcooling area, is passed in parallel through at least two cooling pipes of a first subcooler parallel section, the refrigerant flowing out of the first subcooling section is directed into a first subcooling intermediate channel, and the refrigerant passed through the first subcooling air channel is then passed in parallel through at least two cooling pipes of a second subcooler parallel section / or the condensation region and / or the refrigerant in the subcooling region is cooled by more than 7, 10, 12 or 14 K and is preferably cooled by less than 30 K or 20 K.
  • an automotive air conditioning system comprises a refrigerant condenser assembly, an evaporator, a compressor, preferably a blower, preferably a housing for accommodating the blower and the evaporator, the chill condenser assembly being a refrigerant condenser assembly described in this specification is formed and / or the vehicle air conditioning system described in this description method is executable.
  • the refrigerant is R1234yf or R134a.
  • the refrigerant condenser assembly has a closure device formed on the collecting container for closing a closure opening of the collecting container.
  • a dryer and / or a filter are arranged in the collecting container and / or in the closure device.
  • FIG. 1 and 2 a refrigerant condenser assembly 1 is shown in a perspective view.
  • the refrigerant condenser assembly 1 is part of an automotive air conditioning system with an evaporator and a compressor (not shown).
  • By horizontally arranged cooling tubes 2 as flat tubes 3 flows to be condensed and cooled refrigerant ( Fig. 1 and 2 ).
  • the cooling tubes 2 open at their respective ends in a vertical manifold 5, that is, there are two manifolds 5 respectively at the ends of the cooling tubes 2.
  • the collecting tube 5 has cooling tube openings through which the ends of the cooling tubes 2 project into the collecting tube 5.
  • baffles (not shown) are formed with which a certain flow path of the refrigerant can be achieved through the cooling tubes 2, so that the refrigerant through the cooling tubes 2 according to the flow diagram in Fig. 3 flows through the cooling tubes 2.
  • the cooling tubes 2 meandering corrugated fins 4 are arranged, which are in thermal communication with the cooling tubes 2 by means of heat conduction. This increases the area available for cooling the refrigerant.
  • the cooling tubes 2, the corrugated fins 4 and the two manifolds 4 are generally made of metal, in particular aluminum, and are materially connected together as a solder joint.
  • a fastening device 8 is arranged, with which the Kälternittelkondensatorbauteen on a motor vehicle, in particular on a body of a motor vehicle, can be attached.
  • a collecting container 6 is arranged ( Fig. 1 . 2 ).
  • the collecting container 6 is by means of two overflow openings (not shown) in fluid communication with the collecting tube 5 and thus also indirectly in fluid communication with the cooling tubes 2.
  • a dryer and a filter (not shown) is arranged in the collecting container 6.
  • the dryer is hygroscopic and can absorb water or moisture from the refrigerant.
  • the collecting container 6 is mechanically connected to the collecting tube 5 at the lower and upper ends with a concave support region. At the lower end of the collecting container 6 is closed by a closure device 7 fluid-tight.
  • the removable closure device 7 allows replacement of the dryer and filter in the sump 6.
  • the refrigerant condenser assembly 1 has an inlet port 9 for introducing the refrigerant R1234yf into the refrigerant condenser assembly 1, and an outlet port 10 for discharging the refrigerant from the refrigerant condenser assembly 1 (FIG. Fig. 1 and 3 ).
  • the ends of the cooling tubes 2 terminate in the manifolds 5.
  • baffles or flow guide plates, not shown, are arranged by means of which a certain predetermined flow diagram of the refrigerant can be achieved, ie with which flow path the refrigerant through the plurality of stacked Cooling tubes 2 of the refrigerant condenser assembly 1 flows. This in Fig.
  • the illustrated flow pattern serves only to illustrate the flow path of the refrigerant through the cooling tubes 2 and does not represent a geometric orientation of the cooling tubes 2 to each other in the refrigerant capacitor assembly 1.
  • a first intermediate flow passage 20, a second intermediate flow passage 22, a third intermediate flow passage 24 and a first sub-cooling intermediate flow passage 15th , what a Fig. 3 are shown are thus formed within the manifolds 5 of the flow guide plates, not shown.
  • the refrigerant condenser assembly 1 constitutes a heat exchanger for transferring heat from the refrigerant to air surrounding and circulating around the refrigerant condenser assembly 1.
  • the heat exchanger is essentially formed by the cooling tubes 2 and the two manifolds 5.
  • the heat exchanger as part of the refrigerant condenser assembly 1 in this case has an inlet opening 9 through which gaseous refrigerant is passed from a compressor, not shown, to the refrigerant condenser assembly 1.
  • the gaseous refrigerant is at an overheating region 11 to a saturation temperature cooled, ie at the saturation temperature occurs according to the existing pressure, a condensation of the refrigerant.
  • condensation region 12 follows, in which the refrigerant is condensed and thus liquefied.
  • the refrigerant liquefied in the condensation region 12 is supplied as liquid to the subcooling region 13 and cooled in the subcooling region 13 below the boiling temperature of the refrigerant.
  • condensation region 12 and subcooling region 13 may differ slightly during operation of an automotive air conditioning system, so that, for example, in a modification of the illustration in FIG Fig. 3 the overheating region 11 is slightly larger and thereby the condensation region 12 becomes smaller, so that, for example, a second parallel section 21 also partially forms the overheating region 11.
  • the overheating region and the condensation region may be arranged in exactly one parallel section.
  • the overheating region 11 is formed by the first parallel section 19.
  • the first parallel section 19 has eleven cooling tubes which are connected in parallel or flow through in a fluid-conducting or hydraulic manner. After flowing out of the refrigerant from the eleven cooling tubes 2 of the first parallel section 19, the refrigerant is introduced into the first intermediate flow passage 20 and introduced from the first intermediate flow passage 20 into the second parallel section 21.
  • the second parallel section 21 has eight cooling tubes 2, through which the refrigerant flows simultaneously in parallel. The refrigerant flowing out of the second parallel section 21 is introduced into the second intermediate flow passage 22 and introduced therefrom into the third parallel section 23 with likewise eight cooling tubes 2.
  • the refrigerant flowing out of the third parallel section 23 is introduced into the third intermediate flow passage 24, and is then supplied to the subcooling section 13 of the refrigerant condenser assembly 1.
  • the subcooling region 13 comprises a first subcooling parallel section 14 and a second subcooling parallel section 16.
  • the two subcooler parallel sections 14, 16 each have six cooling tubes 2.
  • the first sub-cooling parallel section 14 is connected to the second sub-cooling parallel section 16 through the first sub-cooling intermediate flow passage 15.
  • the parallel sections 19, 21 and 23 and the subcooler parallel sections 14, 16 are fluidly connected in series and the cooling tubes 2 at the parallel sections 19, 21 and 23 and at the subcool parallel sections 14, 16 and 18 are hydraulically or fluidly parallel connected.
  • the entire refrigerant passed through the refrigerant condenser assembly 1 thus flows through the respective parallel sections 19, 21 and 23 and the subcooler parallel sections 14, 16.
  • the subcooler parallel sections 14, 16 have a smaller number of cooling tubes 2 than the parallel sections 19, 21 and 23.
  • the flow cross-sectional area of the cooling tubes 2 of the subcooler parallel sections 14, 16 smaller than the flow cross-sectional area of the cooling tubes 2 of the parallel sections 19, 21 and 23, because the width of the cooling tubes 2 as flat tubes 3 at the parallel sections 19, 21, 23 1.8 mm and the width of Cooling tubes 2 at the subcooler parallel sections 14, 16 is 1.3 mm.
  • the distance between the cooling tubes 2 in the sub-cooling parallel sections 14, 16 with 6 mm smaller than the distance between the cooling tubes of the parallel sections 19, 21, 23 with 8 mm, so that the height of the corrugated fins 4 at the parallel sections 19, 21, 23 with 8 mm is greater than the height of the corrugated fins 4 at the sub-cooling parallel sections 14, 16 with 6 mm.
  • the width of the cooling tubes 2 in this case represents the expansion in a cross section of the cooling tubes 2 and the length of the cooling tubes 2 in the cross section corresponds to the depth of the refrigerant condenser assembly 1 to the cooling tubes 2, ie the expansion in the flow direction of the air passing through between the cooling tubes 2 the refrigerant condenser assembly 1 flows.
  • the refrigerant at the subcooler parallel sections 14, 16 Due to the fluid-conducting or hydraulic circuit of the refrigerant condenser assembly 1 is thus the refrigerant at the subcooler parallel sections 14, 16 a much smaller flow cross-sectional area than at the parallel sections 19, 21 and 23, because the cooling tubes 2 have different flow cross-sectional areas and further the number of cooling tubes. 2 is preferably smaller at the subcooler parallel sections 14, 16 than at the parallel sections 19, 21, and 23. As a result, the flow velocity is adjusted according to the density change.
  • the heat transfer from the refrigerant to the air in the subcooling region 13 can be increased, thereby transferring more heat from the refrigerant to the air flowing around the refrigerant condenser assembly 1
  • the refrigerant in the subcooling 13 are cooled more below the boiling temperature of the refrigerant, for example, be cooled by 14 K below the boiling temperature of the refrigerant. This can be increased advantageously the COP of a refrigerant circuit.
  • the pressure drop in the refrigerant condenser assembly 1 is not or only very slightly increased, so that the high pressure at the inlet opening 9 only slightly increases and thus the performance increase of the refrigeration circuit due to the greater cooling at the subcooling region 13 is substantially greater than the power reduction due to the possible increase of the high pressure at the inlet opening 9 is.
  • the overheating and condensation region 11, 12 may have only one or two parallel sections 19, 21.
  • the volume flow at the subcooling region 13 is greatly increased due to the smaller flow cross sectional area of the cooling tubes 2 in the subcooling region 13, and preferably because of the predetermined flow diagram, so that a stronger subcooling or cooling of the refrigerant can be achieved at the subcooling region 13 without the refrigerant condenser assembly 1 more Required space or surface, because due to the larger volume flow, the heat transfer from the refrigerant per surface unit of the refrigerant condenser assembly 1, in particular to the cooling tubes 2, the corrugated fins 4 or the manifolds 5 as a heat exchanger of the refrigerant condenser assembly 1, is increased.
  • the COP of a refrigeration circuit with the refrigerant condenser assembly 1 can be increased without requiring additional space for the refrigerant condenser assembly 1.
  • the reduction in COP due to the use of the refrigerant R1234yf can be at least partially compensated.

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Air-Conditioning For Vehicles (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Description

Die vorliegende Erfindung betrifft eine Kältemittelkondensatorbaugruppe gemäß den Oberbegriffen von Anspruch 1.The present invention relates to a refrigerant condenser assembly according to the preambles of claim 1.

In Kältemittelkondensatorbaugruppen für eine Kraftfallrzeugklimaanlage wird dampfförmiges Kältemittel in einen flüssigen Aggregatzustand übergeführt und anschließend das flüssige Kältemittel weiter in einem Unterkühlungsbereich "unterkühlt". Die Kältemittelkondensatorbaugruppe bildet einen Teil eines Kältekreises einer Kraftfahrzeugklimaanlage mit einem Verdampfer, einem Expansionsorgan und einem Verdichter.In refrigerant condenser assemblies for a power tool air conditioning system, vaporous refrigerant is converted into a liquid state of aggregation and then the liquid refrigerant is further "subcooled" in a subcooling region. The refrigerant condenser assembly forms part of a refrigeration circuit of an automotive air conditioning system with an evaporator, an expansion device and a compressor.

Die DE 10 2007 018 722 A1 zeigt einen Kondensator für die Klimaanlage eines Kraftfahrzeuges, der zwei Sammelrohre aufweist und einen neben dem einen Sammelrohr angeordneten Behälter zur Aufnahme des Trocknungsmittels des Kältemittels der Klimaanlage.The DE 10 2007 018 722 A1 shows a condenser for the air conditioning system of a motor vehicle having two manifolds and a container arranged adjacent to the one collecting tube for receiving the desiccant of the refrigerant of the air conditioner.

Beim Einsatz des neuen Kältemittels R1234yf im Vergleich zum bisherigen Kältemittel R134a kommt es aufgrund veränderter Stoffeigenschaften des neuen Kältemittels R1234yf zu einer Leistungsminderung des Kältekreises einer Kraftfahrzeugklimaanlage im Bereich von bis zu 10%. Die Leistung eines Kältekreises in einer Kraftfahrzeugklirnaanlage kann unter anderem dadurch erhöht werden, dass an einem Unterkühlungsbereich der Kältemittelkondensatorbaugruppe das bereits verflüssigte Kältemittel stärker abgekühlt wird.When using the new refrigerant R1234yf in comparison to the previous refrigerant R134a, due to changed material properties of the new refrigerant R1234yf, the refrigeration cycle of an automotive air conditioning system is reduced by up to 10%. The performance of a refrigeration circuit in a Kraftfahrzeugklirnaanlage can be increased inter alia, that at a subcooling of the refrigerant condenser assembly, the already liquefied refrigerant is cooled more.

In einer Kältemittelkondensatorbaugruppe tritt das Kältemittel in Gasform an einer Einlassöffnung in die Kältemittelkondensatorbaugruppe ein und wird an einem Überhitzungsbereich auf eine Sättigungstemperatur abgekühlt. Anschließend strömt das Kältemittel in einen Kondensationsbereich und in diesem wird das gasförmige Kältemittel weiter abgekühlt und damit verflüssigt. Anschließend strömt das flüssige Kältemittel in einen Unterkühlungsbereich und wird unterhalb der Siedetemperatur, beispielsweise auf eine Temperatur von 6 oder 7 K unterhalb der Siedetemperatur, des Kältemittels abgekühlt. Durch eine stärkere Abkühlung des Kältemittels in dem Uhterkühlungsbereich unterhalb der Siedetemperatur des Kältemittels kann eine höhere Leistung des Kältekreises erreicht werden. Im Allgemeinen steht jedoch der Kältemittelkondensatorbaugruppe innerhalb des Kraftfahrzeuges ein vorgegebener Bauraum, beispielsweise vorgegeben durch eine gewisse Bautiefe, Bauhöhe und Baubreite zur Verfügung, so dass zwar eine stärkere Abkühlung des Kältemittels am Unterkühlungsbereich durch eine größere Oberfläche an dem Unterkühlungsbereich und einem damit verbundenen größerem Bauraum der Kältemittelkondensatorbaugruppe zwar möglich ist, jedoch im Allgemeinen aufgrund der vorgegebenen Abmessungen des Bauraumes für die Kältemittelkondensatorbaugruppe kein größerer Bauraum zur Verfügung steht.In a refrigerant condenser assembly, the refrigerant in gaseous form enters the refrigerant condenser assembly at an inlet port and is cooled to a saturation temperature at an overheat region. Subsequently, the refrigerant flows into a condensation region and in this the gaseous refrigerant is further cooled and liquefied. Subsequently, the liquid refrigerant flows into a subcooling region and is cooled below the boiling point, for example to a temperature of 6 or 7 K below the boiling temperature of the refrigerant. By a greater cooling of the refrigerant in the Uhterkühlungsbereich below the boiling point of the refrigerant higher power of the refrigerant circuit can be achieved. In general, however, the refrigerant capacitor assembly within the motor vehicle, a predetermined space, for example given by a certain depth, height and width available, so that although a greater cooling of the refrigerant at the subcooling by a larger surface at the subcooling and a larger space associated therewith Although refrigerant condenser assembly is possible, but in general due to the predetermined dimensions of the space for the refrigerant condenser assembly no larger space is available.

Zur Leistungssteigerung des Kältemittelkreislaufs beziehungsweise zur Kompensation der Minderleistung des Kältemittels, insbesondere des Kältemittels R1234yf, wird angestrebt, die Unterkühlung auf beispielsweise 15 K zu erhöhen. Hierfür werden mehr Kühlrohre beziehungsweise anteilig mehr Fläche vom Kondensator benötigt. Dies hat zur Folge, dass für den Kondensationsbereich weniger Fläche zur Verfügung steht, die Abkühlung auf einer höheren Sättigungstemperatur erfolgt und der zugehörige Sättigungsdruck ansteigt. Dies bewirkt im Kältekreislauf einen negativen Effekt auf die Kälteleistung, was den angestrebten Vorteil mindert oder sogar zunichtemacht.To increase the performance of the refrigerant circuit or to compensate for the reduced performance of the refrigerant, in particular the refrigerant R1234yf, the aim is to increase the subcooling to, for example, 15 K. For this purpose, more cooling tubes or proportionally more area required by the capacitor. This has the consequence that less space is available for the condensation area, the cooling takes place at a higher saturation temperature and the associated saturation pressure increases. This causes a negative effect on the cooling capacity in the refrigeration cycle, which reduces or even nullifies the desired advantage.

Die Aufgabe der vorliegenden Erfindung besteht deshalb darin, eine Kältemittelkondensatorbaugruppe zur Verfügung zu stellen, bei der das Kältemittel in einem Unterkühlungsbereich der Kältemittelkondensatorbaugruppe stark abgekühlt wird, ohne dass in der Kältemittelkondensatorbaugruppe der Kondensationsdruck wesentlich ansteigt.Therefore, the object of the present invention is to provide a refrigerant condenser assembly in which the refrigerant is strongly cooled in a subcooling region of the refrigerant condenser assembly without substantially increasing the condensing pressure in the refrigerant condenser assembly.

Diese Aufgabe wird gelöst mit einer Kältemittelkondensatorbaugruppe für eine Kraftfahrzeugklimaanlage, umfassend Kühlrohre zum Durchleiten eines Kältemittels, zwei Sammelrohre zum Fluidverbinden der Kühlrohre, vorzugsweise einen Sammelbehälter mit wenigstens einer Überströmöffnung mittels der der Sammelbehälter in Fluidverbindung zu den Kühlrohren und/oder einem Sammelrohr steht, die Kühlrohre einen Überhitzungsbereich zum Kühlen des dampfförmigen Kältemittels, einen Kondensationsbereich zum Kondensieren des Kältemittels als wenigstens einen Parallelabschnitt und einen Unterkühlungsbereich als Unterkühlparallelabschnitt zum Kühlen des flüssigen Kältemittels, wobei die Strömungsquerschnittsflächen der Kühlrohre, insbesondere sämtlicher Kühlrohre, des Unterkühlungsbereiches kleiner sind als das Produkt aus 0,9 oder 0,7 oder 0,5 und der Strömungsquerschnittsflächen der Kühlrohre, insbesondere sämtlicher Kühlrohre, des Überhitzungsbereiches und/oder des Kondensationsbereiches. Die Strömungsquerschnittsfläche ist die Querschnittsfläche der Kühlrohre zum Durchleiten des Kältemittels. Die Kühlrohre des Unterkühlungsbereiches weisen damit eine kleinere Strömungsquerschnittsfläche auf als die Kühlrohre des Überhitzungsbereiches und/oder des Kondensationsbereiches. Eine kleinere Strömungsquerschnittsfläche kann beispielsweise durch Kühlrohre mit einer kleineren Querschnittsfläche oder durch Kühlrohre mit dergleichen Querschnittsfläche, wobei Turbulenzeinlagen in den Kühlrohren des Unterkühlungsbereiches die Strömungsquerschnittsfläche verringern, erreicht werden.This object is achieved with a refrigerant condenser assembly for an automotive air conditioning system comprising cooling tubes for passing a refrigerant, two header tubes for fluidly connecting the cooling tubes, preferably a header with at least one overflow opening by means of which the header is in fluid communication with the cooling tubes and / or a header, the cooling tubes an overheating section for cooling the vapor refrigerant, a condensing section for condensing the refrigerant as at least a parallel section, and a subcooling section as a subcooler parallel section for cooling the liquid refrigerant, wherein the flow cross sectional areas of the cooling tubes, particularly all of the cooling tubes, of the subcooling section are smaller than the product of 0.9 or 0.7 or 0.5 and the flow cross-sectional areas of the cooling tubes, in particular of all cooling tubes, the overheating area and / or the condensation area. The flow cross-sectional area is the cross-sectional area of the cooling tubes for passing the refrigerant. The cooling tubes of the subcooling region thus have a smaller flow cross-sectional area than the cooling tubes of the overheating region and / or the condensation region. A smaller flow cross-sectional area can be achieved, for example, by cooling tubes with a smaller cross-sectional area or by cooling tubes with the same cross-sectional area, wherein turbulence inserts in the cooling tubes of the sub-cooling area reduce the flow cross-sectional area.

Dadurch tritt in den Kühlrohren des Unterkühlungsbereiches ein gleich großer Volumenstrom des Kältemittels auf wie in den Kühlrohren des Überhitzungsbereiches und/oder des Kondensationsbereiches, so dass die Wärme besser von dem Kältemittel auf die Luft übertragen werden kann. Damit kann in vorteilhafter Weise am Unterkühlungsbereich das Kältemittel stärker abgekühlt werden, beispielsweise auf eine Temperatur von 14 K unterhalb der Siedetemperatur des Kältemittels, ohne dass dabei die Abmessungen der Kältemittelkondensatorbaugruppe zu erhöhen sind und damit die Kältemittelkondensatorbaugruppe in einen vorgegebenen Bauraum eines Kraftfahrzeuges Platz findet. Damit kann die Leistung eines Kältekreises einer Kraftfahrzeugklimaanlage verbessert werden und dadurch die Leistungsminderung beim Einsatz des neuen Kältemittels R1234yf wenigstens teilweise ausgeglichen werden.As a result, an equal volume flow of the refrigerant occurs in the cooling tubes of the subcooling region as in the cooling tubes of the overheating region and / or the condensation region, so that the heat can be better transferred from the refrigerant to the air. Thus, the refrigerant can be cooled more advantageously at the subcooling, for example, to a temperature of 14 K below the boiling temperature of the refrigerant without thereby increasing the dimensions of the refrigerant condenser assembly and thus the refrigerant condenser assembly finds place in a given space of a motor vehicle. Thus, the performance of a refrigeration circuit of an automotive air conditioning system can be improved and thereby the power reduction when using the new refrigerant R1234yf be at least partially compensated.

Ein erhöhter Druckabfall im Unterkühlungsbereich, ist für die Leistung der Kältemittelkondensatorbaugruppe hierbei nicht schädlich beziehungsweise leistungsmindernd. Dies ist darauf zurückzuführen, dass der Druckabfall nach dem Nassdampfgebiet stattfindet, während sich der Hochdruck des Systems an der Sättigungstemperatur vor dem Unterkühlungsbereich beziehungsweise nach dem Kondensationsbereich orientiert.An increased pressure drop in the subcooling area is not detrimental to the performance of the refrigerant condenser assembly or performance reducing. This is due to the fact that the pressure drop takes place after the wet steam area, while the system's high pressure is oriented at the saturation temperature before the subcooling area or after the condensation area.

In einer Variante sind im Unterkühlungsbereich wenigstens zwei Kühlrohre als erster Unterkühlparallelabschnitt fluidleitend mit dem Kältemittel parallel beaufschlagt, wobei das aus dem ersten Unterkühlparallelabschnitt ausströmende Kältemittel in einen ersten Unterkühlzwischenströmungskanal mündet und der erste Unterkühlzwischenströmungskanal in wenigstens zwei Kühlrohre als zweiter Unterkühlparallelabschnitt mündet und vorzugsweise mündet im Unterkühlungsbereich der zweite Unterkühlparallelabschnitt in einen zweiten Unterkühlzwischenströmungskanal und der zweite Unterkühlzwischenströmungskanal mündet in wenigstens zwei Kühlrohre als dritter Unterkühlparallelabschnitt. Der Unterkühlungsbereich der Kältemittelkondensatorbaugruppe ist damit in insgesamt zwei oder drei Unterkühlparallelabschnitte unterteilt, die jeweils durch den Unterkühlzwischenströmungskanal miteinander verbunden sind. Dadurch kann das Kältemittel an dem Unterkühlungsbereich noch weiter unterhalb der Siedetemperatur des Kältemittels abgekühlt werden.In a variant, in the subcooling region, at least two cooling tubes act as the first subcooler in parallel with the refrigerant, the refrigerant flowing out of the first subcooler enters into a first subcooling passage and the first subcooling passage opens into at least two cooling tubes as the second subcooler and preferably flows into the subcooling region second subcooling parallel section into a second subcooling intermediate flow channel and the second subcooling intermediate flow channel opens into at least two cooling tubes as the third subcooler parallel section. The subcooling region of the refrigerant condenser assembly is thus divided into a total of two or three subcooler parallel sections, each interconnected by the subcooling intercooler passage. As a result, the refrigerant at the subcooling region can be cooled even further below the boiling point of the refrigerant.

Der Unterkühlungsbereich der Kältemittelkondensatorbaugruppe ist somit in einen ersten und zweiten Unterkühlparallelabschnitt unterteilt und in den Unterkühlparallelabschnitten sind jeweils wenigstens zwei Kühlrohre hydraulisch bzw. fluidleitend parallel beaufschlagt mit dem Kältemittel. Dabei wird das Kältemittel, welches aus dem ersten Unterkühlparallelabschnitt austritt in einen ersten Unterkühlzwischenströmungskanal eingeleitet und in diesem vermischt und aus dem ersten Unterkühlzwischenströmungskanal wird das Kältemittel in den zweiten Unterkühlparallelabschnitt eingeleitet. In den aus dem Stand der Technik bekannten Kältemittelkondensatorbaugruppen wird im Unterkühlungsbereich das Kältemittel beispielsweise durch vier, sieben oder neun Kühlrohre parallel geleitet. In der erfindungsgemäßen Kältemittelkondensatorbaugruppe weist der erste und zweite Unterkühlparallelabschnitt beispielsweise zwei, drei oder fünf Kühlrohre auf. Dadurch steht dem Kältemittel am ersten und zweiten Unterkühlparallelabschnitt eine geringere Strömungsquerschnittsfläche als bei dem aus dem Stand der Technik bekannten Kältemittelkondensatorbaugruppe zur Verfügung, so dass dadurch eine größere Strömungsgeschwindigkeit des Kältemittels an dem Unterkühlungsbereich auftritt und dadurch die Wärmeübertragung von dem Kältemittel auf die Luft, welche die Kältemittelkondensatorbaugruppe umströmt, verbessert oder erhöht werden kann.The subcooling region of the refrigerant condenser assembly is thus subdivided into a first and a second subcooler parallel section, and in the subcooler parallel sections, at least two cooling tubes are respectively hydraulically or fluid-conductively supplied in parallel with the refrigerant. In this case, the refrigerant exiting from the first subcooler parallel section is introduced into and mixed in a first subcooling intermediate flow channel, and the refrigerant is introduced into the second subcooler parallel section from the first subcooling intermediate flow channel. In the refrigerant condenser assemblies known from the prior art, the refrigerant is conducted in parallel in the subcooling region, for example, by four, seven or nine cooling tubes. In the refrigerant condenser assembly according to the invention, the first and second subcooler parallel sections have, for example, two, three or five cooling tubes. As a result, the refrigerant has a smaller flow cross-sectional area at the first and second subcooler parallel sections as in the refrigerant condenser assembly known in the art, thereby causing a larger flow velocity of the refrigerant to occur at the subcooling region and thereby improve or increase the heat transfer from the refrigerant to the air flowing around the refrigerant condenser assembly.

In einer weiteren Ausgestaltung weist je ein Unterkühlparallelabschnitt oder der Unterkühlungsbereich zwischen zwei oder acht parallel beaufschlagte Kühlrohre auf und/oder die Oberfläche der Kühlrohre und vorzugsweise der Sammelrohre des Unterkühlungsbereiches beträgt weniger als 50 %, 40 %, 35 %, 30 %, 25 % oder 15 % der Oberfläche des Wärmeübertragers der Kältemittelkondensatorbaugruppe und insbesondere besteht der Wärmeübertrager aus den Kühlrohren und vorzugsweise den Sammelrohren.In a further embodiment, one subcooler parallel section or the subcooling region between two or eight cooling tubes acted upon in parallel and / or the surface of the cooling tubes and preferably the headers of the subcooling region is less than 50%, 40%, 35%, 30%, 25% or 15% of the surface of the heat exchanger of the refrigerant condenser assembly and in particular, the heat exchanger consists of the cooling tubes and preferably the headers.

In einer ergänzenden Ausführungsform sind in Strömungsrichtung des Kältemittels vor dem ersten Unterkühlparallelabschnitt wenigstens zwei Kühlrohre als erster Parallelabschnitt fluidleitend parallel beaufschlagt. Das aus dem ersten Parallelabschnitt ausströmende Kältemittel mündet in einen ersten Zwischenströmungskanal und der erste Zwischenströmungskanal mündet in wenigstens zwei Kühlrohre als zweiter Parallelabschnitt. In Strömungsrichtung des Kältemittels vor dem ersten Unterkühlparallelabschnitt, d. h. vor dem Unterkühlungsbereich der Kältemittelkondensatorgruppe, d. h. damit am Überhitzungsbereich und/oder am Kondensationsbereich der Kältemittelkondensatorbaugruppe ist damit ein erster und ein zweiter Parallelabschnitt angeordnet. Damit sind der Überhitzungsbereich und/oder der Kondensationsbereich in den ersten und zweiten Unterkühlparallelabschnitt unterteilt zwischen denen das Kältemittel durch den ersten Zwischenströmungskanal geleitet wird.In a supplementary embodiment, in the flow direction of the refrigerant before the first subcool parallel section, at least two cooling tubes are acted upon as a first parallel section in a fluid-conducting manner in parallel. The refrigerant flowing out of the first parallel section opens into a first intermediate flow channel and the first intermediate flow channel opens into at least two cooling tubes as the second parallel section. In the flow direction of the refrigerant before the first subcooler parallel section, ie before the subcooling region of the refrigerant condenser group, ie thus at the overheating region and / or at the condensation region of the refrigerant condenser assembly is thus arranged a first and a second parallel section. Thus, the overheating region and / or the condensation region are subdivided into the first and second subcooler parallel sections between which the refrigerant is conducted through the first intermediate flow channel.

In einer ergänzenden Ausführungsform mündet in Strömungsrichtung des Kältemittels vor dem ersten Unterkühlparallelabschnitt das aus dem zweiten Parallelabschnitt ausströmende Kältemittel in einen zweiten Zwischenströmungskanal und der zweite Zwischenströmungskanal mündet in wenigstens zwei Kühlrohre als dritter Parallelabschnitt. Vor dem Unterkühlungsbereich, d. h. damit am Überhitzungsbereich und/oder am Kondensationsbereich der Kältemittelkondensatorbaugruppe, ist somit die Kältemittelkondensatorbaugruppe in insgesamt drei Parallelabschnitte mit wenigstens zwei, vorzugsweise wenigstens vier oder sechs oder acht, Kühlrohre unterteilt, die jeweils durch den Zwischenströmungskanal miteinander fluidleitend verbunden sind. Vorzugsweise weist dabei ein Parallelabschnitt eine größere Anzahl an Kühlrohren auf als ein Unterkühlparallelabschnitt und vorzugsweise ist die Anzahl der Kühlrohre eines Parallelabschnittes um zwei, drei, fünf oder sieben Kühlrohre größer als die Anzahl der Kühlrohre eines Unterkühlparallelabschnittes.In a supplementary embodiment, in the flow direction of the refrigerant before the first subcooler parallel section, the refrigerant flowing out of the second parallel section opens into a second intermediate flow channel and the second intermediate flow channel opens into at least two cooling tubes as the third parallel section. Before the subcooling area, d. H. Thus, at the overheating region and / or at the condensation region of the refrigerant condenser assembly, thus the refrigerant condenser assembly is divided into a total of three parallel sections with at least two, preferably at least four or six or eight, cooling tubes, which are each fluid-conductively connected to each other through the intermediate flow channel. Preferably, a parallel section has a greater number of cooling tubes than a subcooler parallel section, and preferably the number of cooling tubes of a parallel section is two, three, five or seven cooling tubes greater than the number of cooling tubes of a subcooler parallel section.

Vorzugsweise mündet der zweite Parallelabschnitt in einen zweiten Zwischenströmungskanal und der zweite Zwischenströmungskanal mündet in den Sammelbehälter oder der dritte Parallelabschnitt mündet in einen dritten Zwischenströmungskanal und der dritte Zwischenströmungskanal mündet in den Sammelbehälter. Weist der Überhitzungs- und/oder Kondensationsbereich der Kältemittelkondensatorbaugruppe den ersten und zweiten Parallelabschnitt auf, wird somit das aus dem zweiten Parallelabschnitt ausgeleitete Kältemittel in den ersten Unterkühlparallelabschnitt eingeleitet oder der Überhitzungs- und/oder Kondensationsbereich weist drei Parallelabschnitte auf, wird das aus dem dritten Parallelabschnitt ausgeleitete Kältemittel in den ersten Unterkühlparallelabschnitt eingeleitet, wobei jeweils zwischen Kondensationsbereich und Unterkühlungsbereich der Sammelbehälter angeordnet ist. Dies gilt auch analog, sofern der Überhitzungs- und/oder Kondensationsbereich in mehr als drei Parallelabschnitte, beispielsweise vier oder fünf Parallelabschnitte, unterteilt ist.Preferably, the second parallel section opens into a second intermediate flow channel and the second intermediate flow channel opens into the collecting container or the third parallel section opens into a third intermediate flow channel and the third intermediate flow channel opens into the collecting container. If the overheating and / or condensation region of the refrigerant condenser assembly has the first and second parallel sections, then the refrigerant discharged from the second parallel section is introduced into the first subcooler section, or the overheating and / or condenser section has three parallel sections, that of the third parallel section discharged refrigerant introduced into the first subcooler parallel section, wherein in each case between condensing region and subcooling of the collecting container is arranged. This also applies analogously if the overheating and / or condensation region is subdivided into more than three parallel sections, for example four or five parallel sections.

In einer Variante ist die Summe der Strömungsquerschnittsflächen sämtlicher Kühlrohre eines Unterkühlparallelabschnittes kleiner als das Produkt aus 1,0 oder 0,9 oder 0,7 oder 0,5 oder 0,3 oder 0,1 und der Summe der Strömungsquerschnittsflächen sämtlicher Kühlrohre eines Parallelabschnittes und/oder die Kühlrohre sind als Flachrohre ausgebildet und zwischen den Flachrohren sind Wellrippen angeordnet. Somit kann insbesondere die Füllmenge an Kältemittel reduziert werden. Somit können insbesondere für Kältemittelkreisläufe mit dem teuren Kältemittel R1234yf die Kosten reduziert werden.In one variant, the sum of the flow cross-sectional areas of all the cooling tubes of a subcooler parallel section is smaller than the product of 1.0 or 0.9 or 0.7 or 0.5 or 0.3 or 0.1 and the sum of the flow cross-sectional areas of all the cooling tubes of a parallel section and / or the cooling tubes are formed as flat tubes and corrugated ribs are arranged between the flat tubes. Thus, in particular, the filling amount of refrigerant can be reduced. Thus, especially for refrigerant circuits with the expensive refrigerant R1234yf the cost can be reduced.

In einer Variante ist die Breite der Kühlrohre, insbesondere sämtlicher Kühlrohre, eines Unterkühlparallelabschnittes oder des Unterkühlungsbereiches kleiner als das Produkt aus 1,0 oder 0,9 oder 0,7 oder 0,5 oder 0,3 oder 0,1 und der Breite der Kühlrohre, insbesondere sämtlicher Kühlrohre, eines Parallelabschnittes.In one variant, the width of the cooling tubes, in particular of all cooling tubes, a subcooling parallel section or the subcooling region is smaller than the product of 1.0 or 0.9 or 0.7 or 0.5 or 0.3 or 0.1 and the width of the Cooling tubes, in particular all cooling tubes, a parallel section.

Unabhängig davon kann der Wärmeübergang im Unterkühlungsbereich auch durch die einzelnen Wellrippen gesteuert werden, die zwischen den einzelnen Kühlrohren angeordnet sind. Erfindungsgemäß wird deshalb vorgeschlagen, dass die Wellrippen im Unterkühlungsbereich eine andere Geometrie aufweisen als die Wellrippen im Überhitzungsbereich und/oder Kondensationsbereich. Bevorzugt sind hierbei die Wellrippen im Unterkühlungsbereich derartig ausgeführt, dass sich der luftseitige Wärmeübergang in diesem Bereich vergrößert beziehungsweise verbessert.Regardless, the heat transfer in the subcooling can also be controlled by the individual corrugated fins, which are arranged between the individual cooling tubes. According to the invention, it is therefore proposed that the corrugated fins have a different geometry in the subcooling region than the corrugated fins in the overheating region and / or condensation region. In this case, the corrugated fins in the subcooling region are preferably designed such that the air-side heat transfer in this region increases or improves.

Beispielsweise könnten die Wellrippen im Unterkühlungsbereich gleich hoch ausgeführt sein, wie im Überhitzungsbereich und/oder Kondensationsbereich, jedoch durch eine erhöhte Wellrippendichte oder durch Kiemenfelder eine andere Geometrie aufweisen, die den Wärmeübergang in diesem Bereich verbessert.For example, the corrugated fins in the subcooling region could be of the same height as in the overheating region and / or condensation region, but have a different geometry due to increased corrugated rib density or gill fields, which improves the heat transfer in this region.

Alternativ könnten die Wellrippen im Unterkühlungsbereich mit einer geringeren Höhe ausgeführt sein als im Überhitzungsbereich und/oder Kondensationsbereich.Alternatively, the corrugated fins in the subcooling region could be designed with a lower height than in the overheating region and / or condensation region.

Alternativ könnten im Unterkühlungsbereich schmalere Kühlrohre eingesetzt werden, um die Strömungsgeschwindigkeit und somit den Wärmeübergang zu erhöhen.Alternatively, narrower cooling tubes could be used in the subcooling area in order to increase the flow velocity and thus the heat transfer.

Alternativ könnten die Wellrippen im Unterkühlungsbereich mit einer größeren Höhe ausgeführt sein als im Überhitzungsbereich und/oder Kondensationsbereich. In diesem Fall würde der luftseitige Wärmeübergang verschlechtert werden. Da jedoch kältemittelseitig weniger Kühlrohre parallel angeordnet sind, würde sich der kältemittelseitige Wärmeübergang erhöhen.Alternatively, the corrugated fins could be designed in the subcooling with a higher height than in the overheating area and / or condensation area. In this case, the air-side heat transfer would be deteriorated. However, since fewer cooling tubes are arranged in parallel on the refrigerant side, the heat transfer on the refrigerant side would increase.

Beschrieben sei auch ein Verfahren zum Betreiben eines Kältekreises einer Kraftfahrzeugklimaanlage mit den Schritten: Leiten von Kältemittel durch Leitungen eines Kältemittelkreislaufes, Verdichten des gasförmigen Kältemittels in einem Verdichter, so dass der Druck des gasförmigen Kältemittels erhöht wird, Kühlen und Kondensieren des gasförmigen Kältemittels in einer Kältemittelkondensatorbaugruppe, das durch Kühlrohre geleitet wird, indem das gasförmige Kältemittel in einem Überhitzungsbereich auf eine Sättigungstemperatur abgekühlt wird, anschließend in einem Kondensationsbereich das gasförmige Kältemittel auf eine Siedetemperatur abgekühlt und verflüssigt wird und in einem Unterkühlungsbereich das flüssige Kältemittel unterhalb der Siedetemperatur abgekühlt wird, Expandieren des flüssigen Kältemittels an einem Expansionsorgan, so dass der Druck des flüssigen Kältemittels reduziert wird, Erwärmen und Verdampfen des Kältemittels in einem Verdampfer, Leiten des aus dem Verdampfer austretenden gasförmigen Kältemittels zu dem Verdichter, wobei in dem Unterkühlungsbereich das Kältemittel durch Kühlrohre mit einer kleineren Strömungsquerschnittsfläche geleitet wird als das Kältemittel das durch die Kühlrohre des Überhitzungsbereiches und/oder des Kondensationsbereiches geleitet wird, so dass das durch die Kühlrohre in dem Unterkühlungsbereich geleitete Kältemittel einen gleich großen Volumenstrom aufweist wie das in dem Überhitzungsbereich und/oder dem Kondensationsbereich durch die Kühlrohre geleitete Kältemittel.Also described is a method for operating a refrigeration cycle of an automotive air conditioning system comprising the steps of: passing refrigerant through conduits of a refrigerant circuit, compressing the gaseous refrigerant in a compressor so that the pressure of the gaseous refrigerant is increased, cooling and condensing the gaseous refrigerant in a refrigerant condenser assembly passed through cooling tubes by cooling the gaseous refrigerant in an overheating region to a saturation temperature, then cooling and liquefying the gaseous refrigerant to a boiling temperature in a condensation region and cooling the liquid refrigerant below the boiling temperature in a subcooling region; expanding the liquid Refrigerant on an expansion device, so that the pressure of the liquid refrigerant is reduced, heating and evaporation of the refrigerant in an evaporator, Le In the subcooling region, the refrigerant flows through cooling tubes with a smaller flow cross-sectional area into the gaseous refrigerant exiting from the evaporator to the compressor is passed as the refrigerant which is passed through the cooling tubes of the superheating region and / or the condensation region, so that the refrigerant passed through the cooling tubes in the subcooling region has an equal volume flow as the refrigerant conducted in the superheating region and / or the condensation region through the cooling tubes ,

Zweckmäßig wird in dem Unterkühlungsbereich das Kältemittel durch wenigstens zwei Kühlrohre eines ersten Unterkühlparallelabschnittes parallel geleitet, das aus dem ersten Unterkühlparaiielabschnitt ausströmende Kältemittel wird in einen ersten Unterkühlzwischenströmungskanal geleitet und das durch den ersten Unterkühlzwischenströmungskanal geleitete Kältemittel wird anschließend durch wenigstens zwei Kühlrohre eines zweiten Unterkühlparallelabschnittes parallel geleitet und/oder des Kondensationsbereiches und/oder das Kältemittel in dem Unterkühlungsbereich wird um mehr als 7, 10, 12 oder 14 K abgekühlt und wird vorzugsweise um weniger als 30 K oder 20 K abgekühlt. Aufgrund des großen Volumenstromes des Kältemittels in den Kühlrohren des Unterkühlungsbereiches und der damit verbundenen größeren Strömungsgeschwindigkeit des Kältemittels im Unterkühlungsbereich kann dadurch eine bessere Wärmeübertragung von dem Kältemittel auf die Luft, welche die Kältemittelköndensatorbaugruppe umströmt, erreicht werden.Conveniently, in the subcooling area, the refrigerant is passed in parallel through at least two cooling pipes of a first subcooler parallel section, the refrigerant flowing out of the first subcooling section is directed into a first subcooling intermediate channel, and the refrigerant passed through the first subcooling air channel is then passed in parallel through at least two cooling pipes of a second subcooler parallel section / or the condensation region and / or the refrigerant in the subcooling region is cooled by more than 7, 10, 12 or 14 K and is preferably cooled by less than 30 K or 20 K. Due to the large volume flow of the refrigerant in the cooling tubes of the subcooling region and the associated greater flow velocity of the refrigerant in the subcooling region, this can achieve better heat transfer from the refrigerant to the air flowing around the refrigerant condenser assembly.

In einer Weiterbildung umfasst eine Kraftfahrzeugklimaanlage eine Kältemittelkondensatorbaugruppe, einen Verdampfer, einen Verdichter, vorzugsweise ein Gebläse, vorzugsweise ein Gehäuse zur Aufnahme des Gebläses und des Verdampfers, wobei die Kältemättelköndensatorbaugruppe als eine in dieser Beschreibung beschriebene Kältemittelkondensatorbaugruppe ausgebildet ist und/oder von der Kraftfahrzeugklimaanlage ein in dieser Beschreibung beschriebenes Verfahren ausführbar ist.In a further development, an automotive air conditioning system comprises a refrigerant condenser assembly, an evaporator, a compressor, preferably a blower, preferably a housing for accommodating the blower and the evaporator, the chill condenser assembly being a refrigerant condenser assembly described in this specification is formed and / or the vehicle air conditioning system described in this description method is executable.

In einer zusätzlichen Ausführungsform ist das Kältemittel R1234yf oder R134a.In an additional embodiment, the refrigerant is R1234yf or R134a.

In einer Variante weist die Kältemittelkondensatorbaugruppe eine an dem Sammelbehälter ausgebildete Verschlusseinrichtung zum Verschließen einer Verschlussöffnung des Sammelbehälters auf.In a variant, the refrigerant condenser assembly has a closure device formed on the collecting container for closing a closure opening of the collecting container.

Vorzugsweise sind im Sammelbehälter und/oder in der Verschlusseinrichtung ein Trockner und/oder ein Filter angeordnet.Preferably, a dryer and / or a filter are arranged in the collecting container and / or in the closure device.

Im Nachfolgenden wird ein Ausführungsbeispiel der Erfindung unter Bezugnahme auf die beigefügten Zeichnungen näher beschrieben. Es zeigt:

Fig. 1
eine perspektivische Ansicht einer Kältemittelkondensatorbaugruppe,
Fig. 2
eine perspektivische Teilansicht der Kältemittelkondensatorbaugruppe gemäß Fig. 1 und
Fig. 3
ein Strömungsschaltbild des Kältemittels in der Kältemittelkondensatorbaugruppe gemäß Fig. 1.
In the following, an embodiment of the invention will be described in more detail with reference to the accompanying drawings. It shows:
Fig. 1
a perspective view of a refrigerant condenser assembly,
Fig. 2
a partial perspective view of the refrigerant condenser assembly according to Fig. 1 and
Fig. 3
a flow diagram of the refrigerant in the refrigerant condenser assembly according to Fig. 1 ,

In Figur 1 und 2 ist eine Kältemittelkondensatorbaugruppe 1 in einer perspektivischen Ansicht dargestellt. Die Kältemittelkondensatorbaugruppe 1 ist Bestandteil einer Kraftfahrzeugklimaanlage mit einem Verdampfer und einem Verdichter (nicht dargestellt). Durch horizontal angeordnete Kühlrohre 2 als Flachrohre 3 strömt zu kondensierendes und zu kühlendes Kältemittel (Fig. 1 und 2). Die Kühlrohre 2 münden an ihren jeweiligen Enden in ein vertikales Sammelrohr 5, d. h. es sind zwei Sammelrohre 5 jeweils an den Enden der Kühlrohre 2 vorhanden. In Fig. 2 ist nur ein Sammelrohr 5 dargestellt. Das Sammelrohr 5 weist hierfür Kühlrohröffnungen auf, durch welche die Enden der Kühlrohre 2 in das Sammelrohr 5 ragen. Innerhalb der Sammelrohre 5 sind Leitbleche (nicht dargestellt) ausgebildet mit denen ein bestimmter Strömungsweg des Kältemittels durch die Kühlrohre 2 erreicht werden kann, so dass das Kältemittel durch die Kühlrohre 2 gemäß dem Strömungsschaltbild in Fig, 3 durch die Kühlrohre 2 strömt.In FIG. 1 and 2 a refrigerant condenser assembly 1 is shown in a perspective view. The refrigerant condenser assembly 1 is part of an automotive air conditioning system with an evaporator and a compressor (not shown). By horizontally arranged cooling tubes 2 as flat tubes 3 flows to be condensed and cooled refrigerant ( Fig. 1 and 2 ). The cooling tubes 2 open at their respective ends in a vertical manifold 5, that is, there are two manifolds 5 respectively at the ends of the cooling tubes 2. In Fig. 2 only one manifold 5 is shown. For this purpose, the collecting tube 5 has cooling tube openings through which the ends of the cooling tubes 2 project into the collecting tube 5. Within the manifolds 5 baffles (not shown) are formed with which a certain flow path of the refrigerant can be achieved through the cooling tubes 2, so that the refrigerant through the cooling tubes 2 according to the flow diagram in Fig. 3 flows through the cooling tubes 2.

Zwischen den Kühlrohren 2 sind mäanderförmige Wellrippen 4 angeordnet, welche mit den Kühlrohren 2 in thermischer Verbindung mittels Wärmeleitung stehen. Dadurch wird die Fläche vergrößert, welche zum Kühlen des Kältemittels zur Verfügung steht. Die Kühlrohre 2, die Wellrippen 4 und die beiden Sammelrohre 4 bestehen im Allgemeinen aus Metall, insbesondere Aluminium, und sind stoffschlüssig als Lötverbindung miteinander verbunden. In vier Eckbereichen der Kältemittelkondensalorbaugruppe 1 ist eine Befestigungseinrichtung 8 angeordnet, mit der die Kälternittelkondensatorbaugruppe an einem Kraftfahrzeug, insbesondere an einer Karosserie eines Kraftfahrzeuges, befestigt werden kann.Between the cooling tubes 2 meandering corrugated fins 4 are arranged, which are in thermal communication with the cooling tubes 2 by means of heat conduction. This increases the area available for cooling the refrigerant. The cooling tubes 2, the corrugated fins 4 and the two manifolds 4 are generally made of metal, in particular aluminum, and are materially connected together as a solder joint. In four corner regions of the Kältemittelkondensalorbaugruppe 1, a fastening device 8 is arranged, with which the Kälternittelkondensatorbaugruppe on a motor vehicle, in particular on a body of a motor vehicle, can be attached.

An dem Sammelrohr 4 ist, ebenfalls vertikal ausgerichtet, ein Sammelbehälter 6 angeordnet (Fig. 1, 2). Der Sammelbehälter 6 steht mittels zweier Überströmöffnungen (nicht dargestellt) in Fluidverbindung mit dem Sammelrohr 5 und damit auch mittelbar in Fluidverbindung mit den Kühlrohren 2. In dem Sammelbehälter 6 ist ein Trockner und ein Filter (nicht dargestellt) angeordnet. Der Trockner ist hygroskopisch und kann Wasser bzw. Feuchtigkeit aus dem Kältemittel aufnehmen. Der Sammelbehälter 6 ist am unteren und oberen Ende mit dem Sammelrohr 5 mechanisch mit einem konkaven Auflagebereich verbunden. Am unteren Ende ist der Sammelbehälter 6 von einer Verschlusseinrichtung 7 fluiddicht verschlossen. Die abnehmbare Verschlusseinrichtung 7 ermöglicht einen Austausch des Trockners und des Filters in dem Sammelbehälter 6.At the manifold 4, also vertically aligned, a collecting container 6 is arranged ( Fig. 1 . 2 ). The collecting container 6 is by means of two overflow openings (not shown) in fluid communication with the collecting tube 5 and thus also indirectly in fluid communication with the cooling tubes 2. In the collecting container 6, a dryer and a filter (not shown) is arranged. The dryer is hygroscopic and can absorb water or moisture from the refrigerant. The collecting container 6 is mechanically connected to the collecting tube 5 at the lower and upper ends with a concave support region. At the lower end of the collecting container 6 is closed by a closure device 7 fluid-tight. The removable closure device 7 allows replacement of the dryer and filter in the sump 6.

Die Kältemittelkondensatorbaugruppe 1 weist eine Einlassöffnung 9 zum Einleiten des Kältemittels R1234yf in die Kältemittelkondensatorbaugruppe 1 auf und eine Auslassöffnung 10 zum Ausleiten des Kältemittels aus der Kältemittelkondensatorbaugruppe 1 (Fig. 1 und 3). Die Enden der Kühlrohre 2 enden dabei in den Sammelrohren 5. In den Sammelrohren 5 sind nicht dargestellte Leitbleche bzw. Strömungsführungsbleche angeordnet, mit Hilfe denen ein bestimmtes vorgegebenes Strömungsschaltbild des Kältemittels erzielt werden kann, d. h. mit welchem Strömungsweg das Kältemittel durch die Vielzahl von übereinander angeordneten Kühlrohre 2 der Kältemittelkondensatorbaugruppe 1 strömt. Das in Fig. 3 dargestellte Strömungsschallbild dient nur zur anschaulichen Darstellung des Strömungsweges des Kältemittels durch die Kühlrohre 2 und stellt nicht eine geometrische Ausrichtung der Kühlrohre 2 zueinander in der Kältemittelkondensatorbaugruppe 1 dar. Ein erster Zwischenströmungskanal 20, ein zweiter Zwischenströmungskanal 22, ein dritter Zwischenströmungskanal 24 sowie ein erster Unterkühlzwischenströmungskanal 15, welche in Fig. 3 dargestellt sind, werden somit innerhalb der Sammelrohre 5 von den nicht dargestellten Strömungsleitblechen gebildet.The refrigerant condenser assembly 1 has an inlet port 9 for introducing the refrigerant R1234yf into the refrigerant condenser assembly 1, and an outlet port 10 for discharging the refrigerant from the refrigerant condenser assembly 1 (FIG. Fig. 1 and 3 ). The ends of the cooling tubes 2 terminate in the manifolds 5. In the manifolds 5 baffles or flow guide plates, not shown, are arranged by means of which a certain predetermined flow diagram of the refrigerant can be achieved, ie with which flow path the refrigerant through the plurality of stacked Cooling tubes 2 of the refrigerant condenser assembly 1 flows. This in Fig. 3 The illustrated flow pattern serves only to illustrate the flow path of the refrigerant through the cooling tubes 2 and does not represent a geometric orientation of the cooling tubes 2 to each other in the refrigerant capacitor assembly 1. A first intermediate flow passage 20, a second intermediate flow passage 22, a third intermediate flow passage 24 and a first sub-cooling intermediate flow passage 15th , what a Fig. 3 are shown are thus formed within the manifolds 5 of the flow guide plates, not shown.

Die Kältemittelkondensatorbaugruppe 1 stellt einen Wärmeübertrager zur Übertragung von Wärme von dem Kältemittel auf Luft dar, welche die Kältemittelkondensatorbaugruppe 1 umgibt und diese umströmt. Dabei wird der Wärmeübertrager im Wesentlichen von den Kühlrohren 2 und den beiden Sammelrohren 5 gebildet. Der Wärmeübertrager als Teil der Kältemittelkondensatorbaugruppe 1 weist dabei eine Einlassöffnung 9 auf, durch welche gasförmiges Kältemittel von einem nicht dargestellten Verdichter zu der Kältemittelkondensatorbaugruppe 1 geleitet wird. Das gasförmige Kältemittel wird dabei an einem Überhitzungsbereich 11 auf eine Sättigungstemperatur abgekühlt, d. h. an der Sättigungstemperatur tritt entsprechend dem vorhandenen Druck eine Kondensation des Kältemittels ein. In der Strömungsrichtung des Kältemittels nach dem Überhitzungsbereich 11 schließt sich ein Kondensationsbereich 12 an, in welchem das Kältemittel kondensiert und somit verflüssigt wird, Das im Kondensationsbereich 12 verflüssigte Kältemittel wird als Flüssigkeit dem Unterkühlungsbereich 13 zugeführt und im Unterkühlungsbereich 13 unterhalb der Siedetemperatur des Kältemittels abgekühlt. Die in Fig. 3 vorgegebene klare Trennung in Überhitzungsbereich 11, Kondensationsbereich 12 und Unterkühlungsbereich 13 kann dabei beim Betrieb einer Kraftfahrzeugklimaanlage geringfügig abweichen, so dass beispielsweise in Abänderung von der Darstellung in Fig. 3 der Überhitzungsbereich 11 geringfügig größer ist und dadurch der Kondensationsbereich 12 kleiner wird, so dass beispielsweise ein zweiter Parallelabschnitt 21 auch teilweise den Überhitzungsbereich 11 bildet.The refrigerant condenser assembly 1 constitutes a heat exchanger for transferring heat from the refrigerant to air surrounding and circulating around the refrigerant condenser assembly 1. In this case, the heat exchanger is essentially formed by the cooling tubes 2 and the two manifolds 5. The heat exchanger as part of the refrigerant condenser assembly 1 in this case has an inlet opening 9 through which gaseous refrigerant is passed from a compressor, not shown, to the refrigerant condenser assembly 1. The gaseous refrigerant is at an overheating region 11 to a saturation temperature cooled, ie at the saturation temperature occurs according to the existing pressure, a condensation of the refrigerant. In the flow direction of the refrigerant after the overheating region 11, a condensation region 12 follows, in which the refrigerant is condensed and thus liquefied. The refrigerant liquefied in the condensation region 12 is supplied as liquid to the subcooling region 13 and cooled in the subcooling region 13 below the boiling temperature of the refrigerant. In the Fig. 3 predetermined clear separation in the overheating region 11, condensation region 12 and subcooling region 13 may differ slightly during operation of an automotive air conditioning system, so that, for example, in a modification of the illustration in FIG Fig. 3 the overheating region 11 is slightly larger and thereby the condensation region 12 becomes smaller, so that, for example, a second parallel section 21 also partially forms the overheating region 11.

Alternativ ist es auch möglich, dass der Überhitzungsbereich und der Kondensationsbereich in genau einem Parallelabschnitt angeordnet sind.Alternatively, it is also possible for the overheating region and the condensation region to be arranged in exactly one parallel section.

Dies gilt in analoger Weise für die Trennung zwischen dem Kondensationsbereich 12 und dem Unterkühlungsbereich 13, der sich entweder in einen ersten Unterkühlparallelahschnitt 14 verschieben kann in Strömungsrichtung des Kältemittels oder in einen dritten Parallelabschnitt 23 entgegen der Strömungsrichtung des Kältemittels zurück verschieben kann.This applies analogously to the separation between the condensation region 12 and the subcooling region 13, which can either shift into a first subcooling parallel section 14 in the flow direction of the refrigerant or in a third parallel section 23 against the flow direction of the refrigerant.

Der Überhitzungsbereich 11 ist von dem ersten Parallelabschnitt 19 gebildet Der erste Parallelabschnitt 19 weist dabei elf Kühlrohre auf, die fluidleitend bzw. hydraulisch parallel geschalten sind bzw. durchströmt werden. Nach dem Ausströmen des Kältemittels aus den elf Kühlrohren 2 des ersten Parallelabschnittes 19 wird das Kältemittel in den ersten Zwischenströmungskanal 20 eingeleitet und von dem ersten Zwischenströmungskanal 20 in den zweiten Parallelabschnitt 21 eingeleitet. Der zweite Parallelabschnitt 21 weist acht Kühlrohre 2 auf, durch welche das Kältemittel gleichzeitig parallel strömt. Das aus dem zweiten Parallelabschnitt 21 ausströmende Kältemittel wird in den zweiten Zwischenströmungskanal 22 eingeleitet und von diesem in den dritten Parallelabschnitt 23 mit ebenfalls acht Kühlrohren 2 eingeleitet.The overheating region 11 is formed by the first parallel section 19. The first parallel section 19 has eleven cooling tubes which are connected in parallel or flow through in a fluid-conducting or hydraulic manner. After flowing out of the refrigerant from the eleven cooling tubes 2 of the first parallel section 19, the refrigerant is introduced into the first intermediate flow passage 20 and introduced from the first intermediate flow passage 20 into the second parallel section 21. The second parallel section 21 has eight cooling tubes 2, through which the refrigerant flows simultaneously in parallel. The refrigerant flowing out of the second parallel section 21 is introduced into the second intermediate flow passage 22 and introduced therefrom into the third parallel section 23 with likewise eight cooling tubes 2.

Das aus dem dritten Parallelabschnitt 23 ausströmende Kältemittel wird in den dritten Zwischenströmungskanal 24 eingeleitet und wird anschließend dem Unterkühlungsbereich 13 der Kältemittelkondensatorbaugruppe 1 zugeführt. Der Unterkühlungsbereich 13 umfasst einen ersten Unterkühlparallelabschnitt 14 und einen zweiten Unterkühlparallelabschnitt 16. Die zwei Unterkühlparallelabschnitte 14, 16 weisen dabei jeweils sechs Kühlrohre 2 auf. Der erste Unterkühlparallelabschnitt 14 ist mit dem zweiten Unterkühlparallelabschnitt 16 durch den ersten Unterkühlzwischenströmungskanal 15 verbunden. Damit sind in der Kältemittelkondensatorbaugruppe 1 die Parallelabschnitte 19, 21 und 23 sowie die Unterkühlparallelabschnitte 14, 16 fluidleitend in Reihe geschaltet und die Kühlrohre 2 an den Parallelabschnitten 19, 21 und 23 sowie an den Unterkühlparallelabschnitten 14, 16 und 18 sind hydraulisch bzw. fluidleitend parallel geschaltet.The refrigerant flowing out of the third parallel section 23 is introduced into the third intermediate flow passage 24, and is then supplied to the subcooling section 13 of the refrigerant condenser assembly 1. The subcooling region 13 comprises a first subcooling parallel section 14 and a second subcooling parallel section 16. The two subcooler parallel sections 14, 16 each have six cooling tubes 2. The first sub-cooling parallel section 14 is connected to the second sub-cooling parallel section 16 through the first sub-cooling intermediate flow passage 15. Thus, in the refrigerant condenser assembly 1, the parallel sections 19, 21 and 23 and the subcooler parallel sections 14, 16 are fluidly connected in series and the cooling tubes 2 at the parallel sections 19, 21 and 23 and at the subcool parallel sections 14, 16 and 18 are hydraulically or fluidly parallel connected.

Das gesamte durch die Kältemittelkondensatorbaugruppe 1 geleitete Kältemittel durchströmt somit jeweils die Parallelabschnitte 19, 21 und 23 sowie die Unterkühlparallelabschnitte 14, 16. Dabei weisen die Unterkühlparallelabschnitte 14, 16 eine geringere Anzahl an Kühlrohre 2 auf als die Parallelabschnitte 19, 21 und 23. Außerdem ist die Strömungsquerschnittsfläche der Kühlrohre 2 der Unterkühlparallelabschnitte 14, 16 kleiner als die Strömungsquerschnittsfläche der Kühlrohre 2 der Parallelabschnitte 19, 21 und 23, weil die Breite der Kühlrohre 2 als Flachrohre 3 an den Parallelabschnitten 19, 21, 23 1,8 mm und die Breite der Kühlrohre 2 an den Unterkühlparallelabschnitten 14, 16 1,3 mm beträgt. Ferner ist der Abstand zwischen den Kühlrohren 2 in den Unterkühlparallelabschnitten 14, 16 mit 6 mm kleiner als der Abstand zwischen den Kühlrohren der Parallelabschnitte 19, 21, 23 mit 8 mm, so dass die Höhe der Wellrippen 4 an den Parallelabschnitten 19, 21, 23 mit 8 mm größer ist als die Höhe der Wellrippen 4 an den Unterkühlparallelabschnitten 14, 16 mit 6 mm. Die Breite der Kühlrohre 2 stellt dabei die Ausdehnung in einem Querschnitt der Kühlrohre 2 dar und die Länge der Kühlrohre 2 in dem Querschnitt entspricht der Tiefe der Kältemittelkondensatorbaugruppe 1 an den Kühlrohren 2, d. h. der Ausdehnung in Strömungsrichtung der Luft, welche zwischen den Kühlrohren 2 durch die Kältemittelkondensatorbaugruppe 1 strömt.The entire refrigerant passed through the refrigerant condenser assembly 1 thus flows through the respective parallel sections 19, 21 and 23 and the subcooler parallel sections 14, 16. The subcooler parallel sections 14, 16 have a smaller number of cooling tubes 2 than the parallel sections 19, 21 and 23. In addition the flow cross-sectional area of the cooling tubes 2 of the subcooler parallel sections 14, 16 smaller than the flow cross-sectional area of the cooling tubes 2 of the parallel sections 19, 21 and 23, because the width of the cooling tubes 2 as flat tubes 3 at the parallel sections 19, 21, 23 1.8 mm and the width of Cooling tubes 2 at the subcooler parallel sections 14, 16 is 1.3 mm. Further, the distance between the cooling tubes 2 in the sub-cooling parallel sections 14, 16 with 6 mm smaller than the distance between the cooling tubes of the parallel sections 19, 21, 23 with 8 mm, so that the height of the corrugated fins 4 at the parallel sections 19, 21, 23 with 8 mm is greater than the height of the corrugated fins 4 at the sub-cooling parallel sections 14, 16 with 6 mm. The width of the cooling tubes 2 in this case represents the expansion in a cross section of the cooling tubes 2 and the length of the cooling tubes 2 in the cross section corresponds to the depth of the refrigerant condenser assembly 1 to the cooling tubes 2, ie the expansion in the flow direction of the air passing through between the cooling tubes 2 the refrigerant condenser assembly 1 flows.

Aufgrund der fluidleitenden bzw. hydraulischen Schaltung der Kältemittelkondensatorbaugruppe 1 steht damit dem Kältemittel an den Unterkühlparallelabschnitten 14, 16 eine wesentlich geringere Strömungsquerschnittsfläche zur Verfügung als an den Parallelabschnitten 19, 21 und 23, weil die Kühlrohre 2 unterschiedliche Strömungsquerschnittsflächen aufweisen und ferner die Anzahl der Kühlrohre 2 an den Unterkühlparallelabschnitten 14, 16 vorzugsweise kleiner ist als an den Parallelabschnitten 19, 21, und 23. Dadurch wird die Strömungsgeschwindigkeit entsprechend der Dichteänderung angepasst. Aufgrund der hohen Geschwindigkeit des Kältemittels an dem Unterkühlungsbereich 13 im Vergleich zu einem Unterkühlungsbereich mit lediglich einem Unterkühlparallelabschnitt kann die Wärmeübertragung von dem Kältemittel auf die Luft im Unterkühlungsbereich 13 erhöht werden und dadurch mehr Wärme von dem Kältemittel auf die die Kältemittelkondensatorbaugruppe 1 umströmende Luft übertragen werden und somit das Kältemittel im Unterkühlungsbereich 13 stärker unter die Siedetemperatur des Kältemittels abgekühlt werden, beispielsweise um 14 K unterhalb der Siedetemperatur des Kältemittels abgekühlt werden. Damit kann in vorteilhafter Weise der COP eines Kältekreises erhöht werden. Aufgrund der ausreichend dimensionierten Strömungsquerschnittsfläche am Unterkühlungsbereich 13 wird der Druckabfall in der Kältemittelkondensatorbaugruppe 1 nicht oder nur sehr geringfügig erhöht, so dass dadurch der Hochdruck an der Einlassöffnung 9 nur geringfügig ansteigt und somit die Leistungssteigerung des Kältekreises aufgrund der größeren Abkühlung an dem Unterkühlungsbereich 13 wesentlich größer ist, als die Leistungsminderung aufgrund des evtl. Anstieges des Hochdruckes an der Einlassöffnung 9 ist.Due to the fluid-conducting or hydraulic circuit of the refrigerant condenser assembly 1 is thus the refrigerant at the subcooler parallel sections 14, 16 a much smaller flow cross-sectional area than at the parallel sections 19, 21 and 23, because the cooling tubes 2 have different flow cross-sectional areas and further the number of cooling tubes. 2 is preferably smaller at the subcooler parallel sections 14, 16 than at the parallel sections 19, 21, and 23. As a result, the flow velocity is adjusted according to the density change. Due to the high velocity of the refrigerant at the subcooling region 13 compared to a subcooling region having only one subcooling parallel portion, the heat transfer from the refrigerant to the air in the subcooling region 13 can be increased, thereby transferring more heat from the refrigerant to the air flowing around the refrigerant condenser assembly 1 Thus, the refrigerant in the subcooling 13 are cooled more below the boiling temperature of the refrigerant, for example, be cooled by 14 K below the boiling temperature of the refrigerant. This can be increased advantageously the COP of a refrigerant circuit. Due to the adequately dimensioned flow cross-sectional area at the subcooling region 13, the pressure drop in the refrigerant condenser assembly 1 is not or only very slightly increased, so that the high pressure at the inlet opening 9 only slightly increases and thus the performance increase of the refrigeration circuit due to the greater cooling at the subcooling region 13 is substantially greater than the power reduction due to the possible increase of the high pressure at the inlet opening 9 is.

In einem weiteren Ausführungsbeispiel (nicht dargestellt) weist der Unterkühlungsbereich 13 neben dem ersten und zweiten Unterkühlparallelabschnitt 14, 16 auch einen dritten Unterkühlparallelabschnitt auf. In einem zusätzlichen nicht dargestellten Ausführungsbeispiel kann der Überhitzungs- und Kondensationsbereich 11, 12 nur ein oder zwei Parallelabschnitte 19, 21 aufweisen.In a further exemplary embodiment (not shown), the subcooling region 13, in addition to the first and second subcooling parallel sections 14, 16, also has a third subcooling parallel section. In an additional embodiment, not shown, the overheating and condensation region 11, 12 may have only one or two parallel sections 19, 21.

Insgesamt betrachtet sind mit der erfindungsgemäßen Kältemittelkondensatorbaugruppe 1 wesentliche Vorteile verbunden. Der Volumenstrom an dem Unterkühlungsbereich 13 wird aufgrund der kleineren Strömungsquerschnittsfläche der Kühlrohre 2 in dem Unterkühlungsbereich 13 und vorzugsweise wegen des vorgegebenen Strömungsschaltbildes stark erhöht, so dass dadurch eine stärkere Unterkühlung oder Abkühlung des Kältemittels am Unterkühlungsbereich 13 erreicht werden kann, ohne dass die Kältemittelkondensatorbaugruppe 1 mehr Bauraum oder Oberfläche benötigt, weil aufgrund des größeren Volumenstromes die Wärmeübertragung von dem Kältemittel auf die Luft je Oberflächeneinheit der Kältemittelkondensatorbaugruppe 1, insbesondere an den Kühlrohren 2, den Wellrippen 4 oder den Sammelrohren 5 als Wärmeübertrager der Kältemittelkondensatorbaugruppe 1, erhöht wird. Dadurch kann bei einem unveränderten Bauraum für die Kältemittelkondensatorbaugruppe 1 der COP eines Kältekreises mit der Kältemittelkondensatorbaugruppe 1 erhöht werden, ohne dass zusätzlicher Bauraum für die Kältemittelkondensatorbaugruppe 1 erforderlich ist. Damit kann die Verringerung des COP aufgrund der Verwendung des Kältemittels R1234yf wenigstens teilweise ausgeglichen werden.Overall, significant advantages are associated with the inventive refrigerant capacitor assembly 1. The volume flow at the subcooling region 13 is greatly increased due to the smaller flow cross sectional area of the cooling tubes 2 in the subcooling region 13, and preferably because of the predetermined flow diagram, so that a stronger subcooling or cooling of the refrigerant can be achieved at the subcooling region 13 without the refrigerant condenser assembly 1 more Required space or surface, because due to the larger volume flow, the heat transfer from the refrigerant per surface unit of the refrigerant condenser assembly 1, in particular to the cooling tubes 2, the corrugated fins 4 or the manifolds 5 as a heat exchanger of the refrigerant condenser assembly 1, is increased. As a result, with an unchanged installation space for the refrigerant condenser assembly 1, the COP of a refrigeration circuit with the refrigerant condenser assembly 1 can be increased without requiring additional space for the refrigerant condenser assembly 1. Thus, the reduction in COP due to the use of the refrigerant R1234yf can be at least partially compensated.

BezugszeichenlisteLIST OF REFERENCE NUMBERS

11
KältemittelkondensatorbaugruppeRefrigerant condenser assembly
22
Kühlrohrcooling pipe
33
Flachrohrflat tube
44
Wellrippecorrugated fin
55
Sammelrohrmanifold
66
SammelbehälterClippings
77
Verschlusseinrichtung am SammelbehälterClosing device on the collecting container
88th
Befestigungseinrichtungfastening device
99
Einlassöffnunginlet port
1010
Auslassöffnungoutlet
1111
Überhitzungsbereichoverheating area
1212
Kondensationsbereichcondensation region
1313
UnterkühlungshereichUnterkühlungshereich
1414
Erster UnterkühlparallelabschnittFirst subcooler parallel section
1515
Erster UnterkühlzwischenströmungskanalFirst subcooler intermediate flow channel
1616
Zweiter UnterkühlparallelabschrittSecond subcooling parallel step
1717
--
1818
--
1919
Erster ParallelabschnittFirst parallel section
2020
Erster ZwischenströmungskahalFirst intermediate flow channel
2121
Zweiter ParallelabschnittSecond parallel section
2222
Zweiter ZwischenströmungskanalSecond intermediate flow channel
2323
Dritter ParallelabschnittThird parallel section
2424
Dritter ZwischenströmungskanalThird intermediate flow channel

Claims (9)

  1. A refrigerant condenser assembly (1) for a motor vehicle air-conditioning system, comprising
    - cooling tubes (2) for conducting a refrigerant,
    - two collecting tubes (5) for fluidically connecting the cooling tubes (2),
    - preferably a collecting tank (6) having at least one flow transfer opening via which the collecting tank (6) is fluidically connected to the cooling tubes (2) and/or to the collecting tube (5),
    - the cooling tubes (2) have a superheat region (11) for cooling the vaporous refrigerant, a condensation region (12) for condensing the refrigerant as at least one parallel portion (19, 21, 23), and a supercooling region (13) as a supercooling parallel portion for cooling the liquid refrigerant,
    characterised in that
    the flow cross-sectional areas of the cooling tubes (2) of the supercooling region (13) are less than the product of 0.9 or 0.7 or 0.5 and the flow cross-sectional areas of the cooling tubes (2) of the superheat region (11) and the condensation region (12) .
  2. The refrigerant condenser assembly as claimed in claim 1, characterised in that in the supercooling region (13), at least two cooling tubes (2) as a first supercooling parallel portion (14) are charged with the refrigerant in parallel in terms of fluid conduction, the refrigerant flowing out of the first supercooling parallel portion (14) issues into a first supercooling intermediate flow duct (15), and the first supercooling intermediate flow duct (15) issues into at least two cooling tubes (2) as a second supercooling parallel portion (16) and preferably, in the supercooling region (13), the second supercooling parallel portion (16) issues into a second supercooling intermediate flow duct and the second supercooling intermediate flow duct issues into at least two cooling tubes (2) as a third supercooling parallel portion.
  3. The refrigerant condenser assembly as claimed in claim 1 or 2, characterised in that in each case one supercooling parallel portion (14, 16) or the supercooling region (13) has between two or eight cooling tubes (2) which are charged in parallel, and/or the surface area of the cooling tubes (2) and preferably of the collecting tubes (5) of the supercooling region (13) amounts to less than 50%, 40%, 35%, 30%, 25% or 15% of the surface area of the heat exchanger of the refrigerant condenser assembly (1), and in particular, the heat exchanger is composed of the cooling tubes (2) and preferably the collecting tubes (5).
  4. The refrigerant condenser assembly as claimed in one or more of the preceding claims, characterised in that, upstream of the first supercooling parallel portion (14) as viewed in the flow direction of the refrigerant, at least two cooling tubes (2) as a first parallel portion (19) are charged in parallel in terms of fluid conduction, the refrigerant flowing out of the first parallel portion (19) issues into a first intermediate flow duct (20), and the first intermediate flow duct (20) issues into at least two cooling tubes (2) as a second parallel portion (21).
  5. The refrigerant condenser assembly as claimed in claim 4, characterised in that, upstream of the first supercooling parallel portion (14) as viewed in the flow direction of the refrigerant, the refrigerant flowing out of the second parallel portion (21) issues into a second intermediate flow duct (22), and the second intermediate flow duct (22) issues into at least two cooling tubes (2) as a third parallel portion (23).
  6. The refrigerant condenser assembly as claimed in claim 4 or 5, characterised in that the second parallel portion (21) issues into a second intermediate flow duct (22) and the second intermediate flow duct (22) issues into the collecting tank, or the third parallel portion (23) issues into a third intermediate flow duct (24) and the third intermediate flow duct (24) issues into the collecting tank.
  7. The refrigerant condenser assembly as claimed in one or more of the preceding claims, characterised in that the sum total of the flow cross-sectional areas of all cooling tubes (2) of a supercooling parallel portion (14, 16, 18) is less than the product of 0.9 or 0.7 or 0.5 or 0.3 or 0.1 and the sum total of the flow cross-sectional areas of all cooling tubes (2) of a parallel portion (19, 21, 23), and/or the cooling tubes (2) are formed as flat tubes (3) and corrugated fins (4) are arranged between the flat tubes.
  8. The refrigerant condenser assembly (1) for a motor vehicle air-conditioning system as claimed in one of the preceding claims, comprising
    - corrugated fins which are arranged between the cooling tubes,
    characterised in that
    the geometry of the corrugated fins of the supercooling region (13) differs from the geometry of the corrugated fins of the superheat region (11) and/or the condensation region (12).
  9. A motor vehicle air-conditioning system, comprising
    - a refrigerant condenser assembly (1),
    - an evaporator,
    - a compressor,
    - preferably a fan,
    - preferably a housing for accommodating the fan and the evaporator,
    characterised in that
    the refrigerant condenser assembly (1) is designed as claimed in one or more of claims 1 to 8.
EP11745804.2A 2010-08-19 2011-08-19 Coolant condenser assembly Active EP2606291B1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE102010039518A DE102010039518A1 (en) 2010-08-19 2010-08-19 Refrigerant condenser assembly
PCT/EP2011/064322 WO2012022807A1 (en) 2010-08-19 2011-08-19 Coolant condenser assembly

Publications (2)

Publication Number Publication Date
EP2606291A1 EP2606291A1 (en) 2013-06-26
EP2606291B1 true EP2606291B1 (en) 2019-07-31

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EP11745804.2A Active EP2606291B1 (en) 2010-08-19 2011-08-19 Coolant condenser assembly

Country Status (3)

Country Link
EP (1) EP2606291B1 (en)
DE (1) DE102010039518A1 (en)
WO (1) WO2012022807A1 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102013204294A1 (en) * 2013-03-12 2014-10-02 Behr Gmbh & Co. Kg Condenser assembly for refrigerant
CN103438621B (en) * 2013-08-28 2015-11-18 广东志高空调有限公司 A kind of variable stream air-conditioning condenser

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US5482112A (en) * 1986-07-29 1996-01-09 Showa Aluminum Kabushiki Kaisha Condenser
DE3843306A1 (en) * 1988-12-22 1990-06-28 Thermal Waerme Kaelte Klima Flat pipe liquefier for a coolant of an air-conditioning system for a vehicle
JPH11211277A (en) * 1998-01-22 1999-08-06 Showa Alum Corp Subcool system condenser
JP2003021432A (en) * 2001-07-09 2003-01-24 Zexel Valeo Climate Control Corp Condenser
KR100872468B1 (en) * 2002-05-24 2008-12-08 한라공조주식회사 Multistage gas-liquid condenser
GB0326443D0 (en) * 2003-11-13 2003-12-17 Calsonic Kansei Uk Ltd Condenser
EP1577629A1 (en) * 2004-03-18 2005-09-21 Behr Lorraine S.A.R.L. Cap, header and heat exchanger
DE102007018722A1 (en) 2007-03-23 2008-09-25 Modine Manufacturing Co., Racine capacitor
JP2008281326A (en) * 2007-04-11 2008-11-20 Calsonic Kansei Corp Refrigerating unit and heat exchanger used for the refrigerating unit
FR2915793B1 (en) * 2007-05-03 2015-05-01 Valeo Systemes Thermiques IMPROVED HEAT EXCHANGER FOR AIR CONDITIONING CIRCUIT FOR MOTOR VEHICLE

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EP2606291A1 (en) 2013-06-26
DE102010039518A1 (en) 2012-02-23

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