US20120111547A1 - Condenser - Google Patents

Condenser Download PDF

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Publication number
US20120111547A1
US20120111547A1 US13/291,440 US201113291440A US2012111547A1 US 20120111547 A1 US20120111547 A1 US 20120111547A1 US 201113291440 A US201113291440 A US 201113291440A US 2012111547 A1 US2012111547 A1 US 2012111547A1
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US
United States
Prior art keywords
heat exchange
header tank
refrigerant
exchange tubes
tubular body
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.)
Abandoned
Application number
US13/291,440
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English (en)
Inventor
Shingo Suzuki
Kazumi Tokizaki
Yoshihiko Seno
Takayuki Fujii
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 Thermal Systems Japan Ltd
Original Assignee
Showa Denko KK
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
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Assigned to SHOWA DENKO K.K. reassignment SHOWA DENKO K.K. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: FUJII, TAKAYUKI, SENO, YOSHIHIKO, SUZUKI, SHINGO, TOKIZAKI, KAZUMI
Publication of US20120111547A1 publication Critical patent/US20120111547A1/en
Assigned to KEIHIN THERMAL TECHNOLOGY CORPORATION reassignment KEIHIN THERMAL TECHNOLOGY CORPORATION ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: SHOWA DENKO K.K.
Priority to US14/658,239 priority Critical patent/US9587862B2/en
Assigned to KEIHIN THERMAL TECHNOLOGY CORPORATION reassignment KEIHIN THERMAL TECHNOLOGY CORPORATION CORRECTIVE ASSIGNMENT TO CORRECT THE RECEIVING PARTY'S ADDRESS PREVIOUSLY RECORDED AT REEL: 028982 FRAME: 0429. ASSIGNOR(S) HEREBY CONFIRMS THE ASSIGNMENT. Assignors: SHOWA DENKO K.K.
Assigned to KEIHIN THERMAL TECHNOLOGY CORPORATION reassignment KEIHIN THERMAL TECHNOLOGY CORPORATION CORRECTIVE ASSIGNMENT TO CORRECT THE INCORRECT APPL. NO. 13/064,689 PREVIOUSLY RECORDED AT REEL: 028982 FRAME: 0429. ASSIGNOR(S) HEREBY CONFIRMS THE ASSIGNMENT. Assignors: SHOWA DENKO K.K.
Abandoned legal-status Critical Current

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Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B39/00—Evaporators; Condensers
    • F25B39/04—Condensers
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D1/00—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators
    • F28D1/02—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid
    • F28D1/04—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits
    • F28D1/053—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits the conduits being straight
    • F28D1/0535—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits the conduits being straight the conduits having a non-circular cross-section
    • F28D1/05366—Assemblies of conduits connected to common headers, e.g. core type radiators
    • F28D1/05391—Assemblies of conduits connected to common headers, e.g. core type radiators with multiple rows of conduits or with multi-channel conduits combined with a particular flow pattern, e.g. multi-row multi-stage radiators
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F1/00—Tubular elements; Assemblies of tubular elements
    • F28F1/10—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
    • F28F1/12—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element
    • F28F1/126—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element consisting of zig-zag shaped fins
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/02—Header boxes; End plates
    • F28F9/0202—Header boxes having their inner space divided by partitions
    • F28F9/0204—Header boxes having their inner space divided by partitions for elongated header box, e.g. with transversal and longitudinal partitions
    • F28F9/0209—Header boxes having their inner space divided by partitions for elongated header box, e.g. with transversal and longitudinal partitions having only transversal partitions
    • F28F9/0212—Header boxes having their inner space divided by partitions for elongated header box, e.g. with transversal and longitudinal partitions having only transversal partitions the partitions being separate elements attached to header boxes
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2339/00—Details of evaporators; Details of condensers
    • F25B2339/04—Details of condensers
    • F25B2339/044—Condensers with an integrated receiver
    • F25B2339/0441—Condensers with an integrated receiver containing a drier or a filter
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2339/00—Details of evaporators; Details of condensers
    • F25B2339/04—Details of condensers
    • F25B2339/044—Condensers with an integrated receiver
    • F25B2339/0442—Condensers with an integrated receiver characterised by the mechanical fixation of the receiver to the header

Definitions

  • the present invention relates to a condenser suitable for use in, for example, a car air conditioner, which is a refrigeration cycle mounted on an automobile.
  • FIG. 1 the upper side, lower side, left-hand side, and right-hand side of FIG. 1 will be referred to as “upper,” “lower,” “left,” and “right,” respectively.
  • a condenser for a car air conditioner which can reduce installation space has been demanded.
  • the applicant of the present invention has proposed a condenser which can reduce installation space (see the pamphlet of WO2010/047320).
  • the proposed condenser includes a plurality of heat exchange tubes disposed in parallel such that they are spaced apart from one another in a vertical direction and extend in a left-right direction; and header tanks which extend in the vertical direction and to which left and right end portions of the heat exchange tubes are connected, respectively.
  • Three or more heat exchange paths each formed by a plurality of heat exchange tubes successively arranged in the vertical direction are provided such that the heat exchange paths are juxtaposed in the vertical direction.
  • Refrigerant flows in the same direction through all the heat exchange tubes which form each heat exchange path, and the flow direction of refrigerant flowing through the heat exchange tubes which form one of two adjacent heat exchange paths is opposite the flow direction of refrigerant flowing through the heat exchange tubes which form the other heat exchange path.
  • a first header tank and a second header tank are individually provided at the left end or right end.
  • First heat exchange tubes which form at least two successively arranged heat exchange paths, including the heat exchange path at the lower end, are connected to the first header tank.
  • Second heat exchange tubes which form the heat exchange paths provided above the heat exchange paths formed by the first heat exchange tubes connected to the first header tank are connected to the second header tank.
  • the first header tank is disposed on the outer side of the second header tank with respect to the left-right direction, and the upper end of the first header tank is located above the lower end of the second header tank.
  • the first header tank has a function of separating gas and liquid from each other by making use of gravitational force and storing the separated liquid.
  • the upper-end heat exchange path among the heat exchange paths formed by the first heat exchange tubes connected to the first header tank, and the heat exchange paths formed by the second heat exchange tubes connected to the second header tank serve as refrigerant condensation paths for condensing refrigerant.
  • the heat exchange paths formed by the first heat exchange tubes connected to the first header tank, excluding the upper end heat exchange path serve as refrigerant super-cooling paths for super-cooling refrigerant.
  • the condenser disclosed in the pamphlet has been desired to be designed such that, when refrigerant is charged, the amount of refrigerant charged into a refrigeration cycle reaches, in an earlier stage, a proper level at which the degree of super-cooling becomes constant.
  • An object of the present invention is to meet the above-described demand and to provide a condenser in which the amount of refrigerant charged into a refrigeration cycle can be increased to a proper level in an early stage.
  • the present invention comprises the following modes.
  • a condenser comprising a plurality of heat exchange tubes disposed in parallel such that the heat exchange tubes are spaced apart from one another in a vertical direction and extend in a left-right direction; and header tanks which extend in the vertical direction and to which left and right end portions of the heat exchange tubes are connected, in which three or more heat exchange paths each formed by a plurality of heat exchange tubes successively arranged in the vertical direction are juxtaposed in the vertical direction, wherein
  • first and second header tanks are provided at a left or right end of the condenser, first heat exchange tubes which form at least two successively arranged heat exchange paths including a heat exchange path located at the lower end being connected to the first header tank, and second heat exchange tubes which form heat exchange paths provided above the heat exchange paths formed by the first heat exchange tubes connected to the first header thank being connected to the second header tank;
  • the first header tank is disposed on the outer side of the second header tank with respect to the left-right direction, has an upper end located above a lower end of the second header tank, and has a function of separating gas and liquid from each other and storing the liquid by making use of gravitational force;
  • an internal volume reduction portion for reducing an internal volume of the first header tank is provided in a region of the interior of the first header tank which region communicates with the first heat exchange tubes of the refrigerant super-cooling path.
  • a condenser according to par. 1) wherein a refrigerant passable tubular body is disposed in the first header tank, and a portion of the refrigerant passable tubular body constitutes at least a portion of the internal volume reduction portion.
  • a condenser according to par. 2) wherein a lower end closing portion of the first header tank has an inward projecting portion having a recess formed on an upper surface thereof, and a lower end portion of the refrigerant passable tubular body is fitted into the recess.
  • a condenser according to par. 2) wherein a partition portion is provided in the first header tank so as to divide the interior of the first header tank into upper and lower regions, a through hole is formed in the partition portion, and the refrigerant passable tubular body is passed through the through hole of the partition portion.
  • a condenser according to par. 5), wherein the partition portion divides the interior of the first header tank into a first region which communicates with the first heat exchange tubes of a refrigerant super-cooling path located adjacent to and downward of the refrigerant condensation path associated with the first header tank, and a second region located above the first region; at least a portion of the refrigerant passable tubular body is located in the first region of the interior of the first header tank; the refrigerant passable tubular body has a first communication opening opened to the first region and a second communication opening opened to the second region; and at least one of the first and second communication openings is covered with a filter.
  • an internal volume reduction portion for reducing the internal volume of the first header tank is provided in a region within the first header tank, which region communicates with the first heat exchange tubes of the refrigerant super-cooling path. Therefore, at the time of refrigerant charging, liquid-phase refrigerant easily accumulates within the first header tank up to a level equal to or higher than the upper-end heat exchange tube of the refrigerant super-cooling path located adjacent to and downward of the refrigerant condensation path associated with the first header tank. Accordingly, at the time of refrigerant charging, the interiors of the first heat exchange tubes of the refrigerant super-cooling path can be quickly filled with the liquid-phase refrigerant.
  • the amount of refrigerant charged into the refrigeration cycle can be increased, in an early stage, to a proper level at which the degree of super-cooling becomes constant.
  • the width of a stabilized range in which the degree of super-cooling becomes constant i.e., a range of the refrigerant charging amount which renders the degree of super-cooling constant, becomes wider, a super-cooling characteristic which is more stable against variation of load and leakage of refrigerant can be obtained.
  • the internal volume reduction portion can be provided in the first header tank relatively easily.
  • the internal volume reduction portion can be provided in the first header tank relatively easily.
  • refrigerant flows into the first header tank from a plurality of heat exchange tubes which constitute the refrigerant condensation path located at the lower end, and gas liquid separation is performed within the first header tank. Therefore, it is possible to suppress a drop in pressure, to thereby prevent re-vaporization of liquid-phase refrigerant.
  • FIG. 1 is a front view specifically showing the overall structure of the condenser according to the present invention
  • FIG. 2 is a front view schematically showing the condenser of FIG. 1 ;
  • FIG. 3 is a partially omitted vertical sectional view showing, on an enlarged scale, a portion of a first header tank of the condenser shown in FIG. 1 ;
  • FIG. 4 is a sectional view taken along line A-A of FIG. 3 ;
  • FIG. 5 is an exploded perspective view showing a portion of the first header tank of the condenser shown in FIG. 1 , and a refrigerant passable tubular body;
  • FIG. 6 is a graph showing the amount of charged refrigerant and the degree of supper-cooling in the condenser shown in FIG. 1 ;
  • FIG. 7 is a view corresponding to FIG. 3 and showing a modification of the refrigerant passable tubular body.
  • aluminum as used in the following description encompasses aluminum alloys in addition to pure aluminum.
  • FIG. 1 specifically shows the overall structure of a condenser according to the present invention
  • FIG. 2 schematically shows the condenser of the present invention.
  • individual heat exchange tubes are omitted, and corrugate fins, side plates, a refrigerant inlet member, and a refrigerant outlet member are also omitted.
  • FIGS. 3 and 5 show the structure of a main portion of the condenser of FIG. 1 .
  • a condenser 1 includes a plurality of flat heat exchange tubes 2 A, 2 B formed of aluminum, three header tanks 3 , 4 , 5 formed of aluminum, corrugate fins 6 A, 6 B formed of aluminum, and side plates 7 formed of aluminum.
  • the heat exchange tubes 2 A, 2 B are disposed such that their width direction coincides with a front-rear direction, their length direction coincides with a left-right direction, and they are spaced from one another in a vertical direction. Left and right end portions of the heat exchange tubes 2 A, 2 B are connected, by means of brazing, to the header tanks 3 , 4 , 5 , which extend in the vertical direction.
  • Each of the corrugate fins 6 A, 6 B is disposed between and brazed to adjacent heat exchange tubes 2 A, 2 B, or is disposed on the outer side of the uppermost or lowermost heat exchange tube 2 A, 2 B and brazed to the corresponding heat exchange tube 2 A, 2 B.
  • the side plates 7 are disposed on the corresponding outer sides of the uppermost and lowermost corrugate fins 6 A, 6 B, and are brazed to these corrugate fins 6 A, 6 B.
  • Three or more heat exchange paths (in the present embodiment, four heat exchange paths P 1 , P 2 , P 3 , P 4 ) each formed by a plurality of heat exchange tubes 2 A, 2 B successively arranged in the vertical direction are juxtaposed in the vertical direction.
  • the four heat exchange paths will be referred to as the first to fourth heat exchange paths P 1 , P 2 , P 3 , P 4 from the upper side.
  • the flow direction of refrigerant is the same among all the heat exchange tubes 2 A, 2 B which form the respective heat exchange paths P 1 , P 2 , P 3 , P 4 .
  • the flow direction of refrigerant in the heat exchange tubes 2 A, 2 B which form a certain heat exchange path is opposite the flow direction of refrigerant in the heat exchange tubes 2 A, 2 B which form another heat exchange path adjacent to the certain heat exchange path.
  • a first header tank 3 and a second header tank 4 are individually provided at the left end of the condenser 1 .
  • the heat exchange tubes 2 A which form at least two successively arranged heat exchange paths, including the lower-end heat exchange path, (in the present embodiment, the third and fourth heat exchange paths P 3 , P 4 ), are connected to the first header tank 3 by means of brazing.
  • the heat exchange tubes 2 B which form the first and second heat exchange paths P 1 , P 2 are connected to the second header tank 4 by means of brazing.
  • the heat exchange tubes 2 A connected to the first header tank 3 will be referred to as the first heat exchange tubes
  • the heat exchange tubes 2 B connected to the second header tank 4 will be referred to as the second heat exchange tubes.
  • the corrugate fins 6 A disposed between the adjacent first heat exchange tubes 2 A and between the lower-end first heat exchange tube 2 A and the lower side plate 7 will be referred to as the first corrugate fins.
  • the corrugate fins 6 B disposed between the adjacent second heat exchange tubes 2 B and between the upper-end second heat exchange tube 2 B and the upper side plate 7 will be referred to as the second corrugate fins.
  • first header tank 3 and the second header tank 4 are approximately equal to each other in terms of the dimension along the front-rear direction, the first header tank 3 is greater than the second header tank 4 in terms of the horizontal cross sectional area.
  • the first header tank 3 is disposed on the left side (on the outer side with respect to the left-right direction) of the second header tank 4 .
  • the center of the first header tank 3 with respect to the left-right direction is located on the outer side (with respect to the left-right direction) of the center of the second header tank 4 with respect to the left-right direction.
  • the centers of the first and second header tanks 3 , 4 with respect to the front-rear direction are located on a common vertical plane extending in the left-right direction.
  • the first header tank 3 and the second header tank 4 are offset from each other such that they do not overlap as viewed from above.
  • the upper end of the first header tank 3 is located above the lower end of the second header tank 4 .
  • the upper end of the first header tank 3 is located at a position which is substantially the same height as the upper end of the second header tank 4 .
  • the first header tank 3 serves as a liquid receiver which separates gas and liquid from each other through utilization of gravitational force, and stores the separated liquid.
  • the internal volume of the first header tank 3 is determined such that a portion of gas-liquid mixed phase refrigerant having flowed into the first header tank 3 ; i.e., liquid-predominant mixed phase refrigerant, accumulates in a lower region within the first header tank 3 because of gravitational force, and the gas phase component of the gas-liquid mixed phase refrigerant accumulates in an upper region within the first header tank 3 because of gravitational force, whereby only the liquid-predominant mixed phase refrigerant flows into the first heat exchange tubes 2 A of the fourth heat exchange path P 4 .
  • the third header tank 5 is disposed at the right end of the condenser 1 , and all the heat exchange tubes 2 A, 2 B which form the first to fourth heat exchange paths P 1 -P 4 are connected to the third header tank 5 .
  • the transverse cross sectional shape of the third header tank 5 is identical with that of the second header tank 4 .
  • the interior of the third header tank 5 is divided into an upper header section 11 , an intermediate header section 12 , and a lower header section 13 by aluminum partition plates 8 , 9 , which are provided at a height between the first heat exchange path P 1 and the second heat exchange path P 2 and a height between the third heat exchange path P 3 and the fourth heat exchange path P 4 , respectively.
  • Left end portions of the second heat exchange tubes 2 B of the first heat exchange path P 1 are connected to the second header tank 4 , and right end portions thereof are connected to the upper header section 11 of the third header tank 5 .
  • Left end portions of the second heat exchange tubes 2 B of the second heat exchange path P 2 are connected to the second header tank 4 , and right end portions thereof are connected to the intermediate header section 12 of the third header tank 5 .
  • Left end portions of the first heat exchange tubes 2 A of the third heat exchange path P 3 are connected to the first header tank 3 , and right end portions thereof are connected to the intermediate header section 12 of the third header tank 5 .
  • Left end portions of the first heat exchange tubes 2 A of the fourth heat exchange path P 4 are connected to the first header tank 3 , and right end portions thereof are connected to the lower header section 13 of the third header tank 5 .
  • the second header tank 4 a portion of the first header tank 3 to which the first heat exchange tubes 2 A of the third heat exchange path P 3 are connected, the upper and intermediate header sections 11 and 12 of the third header tank 5 , and the first to third heat exchange paths P 1 -P 3 form a condensation section 1 A, which condenses refrigerant.
  • a portion of the first header tank 3 to which the first heat exchange tubes 2 A of the fourth heat exchange path P 4 are connected, the lower header section 13 of the third header tank 5 , and the fourth heat exchange path P 4 form a super-cooling section 1 B, which super-cools refrigerant.
  • Each of the first to third heat exchange paths P 1 -P 3 serves as a refrigerant condensation path for condensing refrigerant
  • the fourth heat exchange path P 4 serves as a refrigerant super-cooling path for super-cooling refrigerant.
  • a refrigerant inlet 14 is formed at the upper header section 11 of the third header tank 5 , which partially forms the condensation section 1 A, and a refrigerant outlet 15 is formed at the lower header section 13 of the third header tank 5 , which partially forms the super-cooling section 1 B.
  • a refrigerant inlet member 16 which communicates with the refrigerant inlet 14 and a refrigerant outlet member 17 which communicates with the refrigerant outlet 15 are joined to the third header tank 5 .
  • the first header tank 3 is composed of a cylindrical tubular body 21 having opened upper and lower ends, a lower end closing member 22 (a lower end closing portion), which is brazed to the lower end of the cylindrical tubular body 21 , and closes a lower end opening of the cylindrical tubular body 21 , and a lid 23 , which is removably attached to the upper end of the cylindrical tubular body 21 , and closes an upper end opening of the cylindrical tubular body 21 . As shown in FIG.
  • the lower end closing member 22 of the first header tank 3 has an inward projecting portion 24 , which is composed of a cylindrical tubular portion 24 a extending along the inner circumferential surface of the circumferential wall of the cylindrical tubular body 21 of the first header tank 3 , and a top wall 24 b integrally formed at the upper end of the cylindrical tubular portion 24 a .
  • the top wall 24 b of the inward projecting portion 24 is located below the lower-end first heat exchange tube 2 A of the fourth heat exchange path P 4 .
  • a recess 25 is provided on the upper surface of the inward projecting portion 24 by means of downwardly deforming a portion of the top wall 24 b in a recess shape.
  • the recess 25 is opened upward and has a conical wall surface tapered such that its diameter decreases downward.
  • a plate member 28 is fixed to a circumferential wall 21 a of the cylindrical tubular body 21 of the first header tank 3 .
  • the plate member 28 serves as a partition portion for dividing the interior of the first header tank 3 into a first region 26 , with which the first heat exchange tubes 2 A of the fourth heat exchange path P 4 communicate, and a second region 27 located above the first region 26 .
  • the plate member 28 is externally inserted into a slit 21 b formed in the circumferential wall 21 a of the cylindrical tubular body 21 of the first header tank 3 , and is brazed to the circumferential wall 21 a .
  • the plate member 28 has a circular through hole 29 formed at a position located on the outer side of the center of the plate member 28 with respect to the left-right direction.
  • a refrigerant passable tubular body 31 and a sack-like desiccant container 35 are disposed within the first header tank 3 such that the desiccant container 35 is located above the refrigerant passable tubular body 31 .
  • the refrigerant passable tubular body 31 is formed of a synthetic resin, and has a bottomed cylindrical tubular shape such that its upper end is opened, and its lower end is closed.
  • the desiccant container 35 is formed of a liquid permeable material, and a desiccant (not shown) is placed in the desiccant container 35 .
  • the refrigerant passable tubular body 31 is closely passed through the through hole 29 of the plate member 28 from the upper side thereof such that its upper end is located between the second heat exchange path P 2 and the third heat exchange path P 3 , and its lower end is located below the lower-end first heat exchange tubes 2 A of the fourth heat exchange path P 4 .
  • a lower end portion of the refrigerant passable tubular body 31 is closely fitted into the recess 25 of the inward projecting portion 24 of the lower end closing member 22 .
  • a fitting portion 31 a of the refrigerant passable tubular body 31 closely fitted into the recess 26 has a conical outer circumferential surface tapered such that its diameter decreases downward.
  • An upper portion 32 a of the circumferential wall 32 of the refrigerant passable tubular body 31 located above the plate member 28 has an outer diameter greater than the diameter of the through hole 29 .
  • a plurality of projections 33 projecting radially outward are integrally formed at predetermined intervals in the circumferential direction.
  • the lower end of the upper portion 32 a of the circumferential wall 32 is in contact with the upper surface of the plate member 28 , and the projections 33 are in contact with the lower surface of the plate member 28 , whereby movement of the refrigerant passable tubular body 31 in the vertical direction is prevented.
  • a plurality of outward projecting portions 34 which project radially outward, are integrally formed at predetermined intervals in the circumferential direction.
  • the desiccant container 35 is supported by the upper end of the circumferential wall 32 and the outward projecting portions 34 .
  • At least a portion (in the present embodiment, a lower portion) of the refrigerant passable tubular body 31 is located in the first region 26 , which communicates with the first heat exchange tubes 2 A of the fourth heat exchange path P 4 (a refrigerant super-cooling path adjacent to the lower-end refrigerant condensation path), and an upper end portion of the refrigerant passable tubular body 31 is located in a portion of the second region 27 , which communicates with the first heat exchange tubes 2 A of the third heat exchange path P 3 (the lower-end refrigerant condensation path).
  • the circumferential wall 32 of the refrigerant passable tubular body 31 has a plurality of vertically elongated first communication openings 36 and a plurality of vertically elongated second communication openings 37 , which are formed at predetermined intervals in the circumferential direction.
  • the first communication openings 36 are opened to the first region 26 of the interior of the first header tank 3 located below the plate member 28
  • the second communication openings 37 are opened to the second region 27 of the interior of the first header tank 3 located above the plate member 28 .
  • the first communication openings 36 are covered with a mesh filter 38 .
  • the first and second communication openings 36 , 37 account for the greater part of the circumferential wall 32 of the refrigerant passable tubular body 31 .
  • the mesh size of the mesh filter 38 covering the first communication openings 36 is such that 100 or more meshes are present over a length of 1 inch.
  • the filter 38 may be formed integrally with the circumferential wall 32 of the refrigerant passable tubular body 31 .
  • the filter 38 may be formed separately from the circumferential wall 32 of the refrigerant passable tubular body 31 , and fixed to the circumferential wall 32 .
  • the fitting portion 31 a of the refrigerant passable tubular body 31 which is closely fitted into the recess 25 of the inward projecting portion 24 of the lower end closing member 22 , and a portion of the refrigerant passable tubular body 31 extending upward from the fitting portion 31 a are solid, whereby a refrigerant entry prevention portion 39 for preventing entry of refrigerant from the first region 26 is formed at the lower end of the refrigerant passable tubular body 31 .
  • the refrigerant entry prevention portion 39 formed at the lower end of the refrigerant passable tubular body 31 , and a portion of the circumferential wall 32 located below the plate member 28 constitute an internal volume reduction portion 41 for reducing the internal volume of the first region 26 of the first header tank 3 .
  • the internal volume reduction portion 41 for reducing the internal volume of the first header tank 3 is provided in the first region 26 of the interior of the first header tank 3 , which communicates with the first heat exchange tubes 2 A of the fourth heat exchange path P 4 .
  • the refrigerant entry prevention portion 39 which is formed at the lower end of the refrigerant passable tubular body 31 and partially constitutes the internal volume reduction portion 41 , is not limited to a solid one, and the refrigerant entry prevention portion 39 may include a hollow space isolated from the first region 26 .
  • the condenser 1 is manufactured as follows. After all the components, excluding the refrigerant passable tubular body 31 , the desiccant container 35 , and the lid 23 , are brazed together, the refrigerant passable tubular body 31 and the desiccant container 35 are placed in the cylindrical tubular body 21 of the first header tank 3 from above, and the lid 23 is attached to the cylindrical tubular body 21 . Thus, the condenser 1 is completed. When the refrigerant passable tubular body 31 is inserted into the cylindrical tubular body 21 , the projections 33 of the refrigerant passable tubular body 31 deform, and then regain their original shapes after having passed through the through hole 29 of the plate member 28 .
  • the condenser 1 constitutes a refrigeration cycle in cooperation with a compressor, an expansion valve (pressure reducer), and an evaporator; and the refrigeration cycle is mounted on a vehicle as a car air conditioner.
  • gas phase refrigerant of high temperature and high pressure compressed by the compressor flows into the upper header section 11 of the third header tank 5 via the refrigerant inlet member 16 and the refrigerant inlet 14 .
  • the gas phase refrigerant is partially condensed while flowing leftward within the second heat exchange tubes 2 B of the first heat exchange path P 1 , and then flows into the second header tank 4 .
  • the refrigerant having flowed into the second header tank 4 is partially condensed while flowing rightward within the second heat exchange tubes 2 B of the second heat exchange path P 2 , and then flows into the intermediate header section 12 of the third header tank 5 .
  • the refrigerant having flowed into the intermediate header section 12 of the third header tank 5 is partially condensed while flowing leftward within the first heat exchange tubes 2 A of the third heat exchange path P 3 , and then flows into the first header tank 3 .
  • the refrigerant having flowed into the first header tank 3 is gas-liquid mixed phase refrigerant.
  • a portion of the gas-liquid mixed phase refrigerant; i.e., liquid-predominant mixed phase refrigerant, accumulates in a lower region within the first header tank 3 because of gravitational force, and enters the first heat exchange tubes 2 A of the fourth heat exchange path P 4 .
  • the liquid-predominant mixed phase refrigerant having entered the first heat exchange tubes 2 A of the fourth heat exchange path P 4 is super-cooled while flowing rightward within the first heat exchange tubes 2 A. After that, the super-cooled refrigerant enters the lower header section 13 of the third header tank 5 , and flows out via the refrigerant outlet 15 and the refrigerant outlet member 17 . The refrigerant is then fed to the evaporator via the expansion valve.
  • the gas phase component of the gas-liquid mixed phase refrigerant having flowed into the first header tank 3 accumulates in an upper region within the first header tank 3 .
  • the refrigerant passable tubular body 31 partially forms the internal volume reduction portion 41 provided in the first region 26 of the interior of the first header tank 3 located below the plate member 28 . Therefore, when the refrigerant is charged into the above-described car air conditioner, the liquid-phase refrigerant easily accumulates in the first region 26 of the interior of the first header tank 3 up to a level equal to or higher than the upper-end first heat exchange tube 2 A of the fourth heat exchange path P 4 , which is a refrigerant super-cooling path and which is located adjacent to and on the lower side of the third heat exchange path P 3 , which is a refrigerant condensation path.
  • the interiors of the first heat exchange tubes 2 A of the fourth heat exchange path P 4 can be quickly filled with the liquid-phase refrigerant.
  • the amount of refrigerant charged into the refrigeration cycle can be increased, in an early stage, to a proper level at which the degree of super-cooling becomes constant.
  • the width of a stabilized range in which the degree of super-cooling becomes constant i.e., a range of the refrigerant charging amount which renders the degree of super-cooling constant, becomes wider, a super-cooling characteristic which is more stable against variation of load and leakage of refrigerant can be obtained.
  • point A represents a point at which the super-cooling of refrigerant flowing out of the condenser 1 was started
  • point B represents a point at which the interiors of the first heat exchange tubes 2 A of the fourth heat exchange path P 4 of the condenser 1 were filled with liquid-phase refrigerant
  • point C represents a point at which the interior of the first header tank 3 of the condenser 1 was filled with liquid-phase refrigerant.
  • the width of a stabilized range in which the degree of super-cooling becomes constant i.e., a range of the refrigerant charging amount which renders the degree of super-cooling constant, becomes wider, a super-cooling characteristic which is more stable against variation of load and leakage of refrigerant can be obtained.
  • FIG. 7 shows a modification of the refrigerant passable tubular body.
  • a fitting portion 50 a closely fitted into the recess 25 of the lower end closing member 22 of the first header tank 3 has a conical outer circumferential surface tapered such that its diameter decreases downward.
  • the fitting portion 50 a of the refrigerant passable tubular body 50 and a portion of the circumferential wall 32 of the refrigerant passable tubular body 50 , the portion extending upward from the fitting portion 50 a form a hollow portion 51 which has a closed lower end and is opened upward.
  • a portion of the circumferential wall 32 of the refrigerant passable tubular body 50 serves as the internal volume reduction portion 41 , which reduces the internal volume of the first header tank 3 and which is provided in the first region 26 , which communicates with the first heat exchange tubes 2 A of the fourth heat exchange path P 4 .
  • the structure of the remaining portion of the refrigerant passable tubular body 50 is the same as that of the above-described refrigerant passable tubular body 31 , and the refrigerant passable tubular body 50 is placed in the first header tank 3 in the same manner as the refrigerant passable tubular body 31 .
  • portions and members of the refrigerant passable tubular body 50 identical with those of the above-described refrigerant passable tubular body 31 are denoted by the same reference numerals.

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Geometry (AREA)
  • Air-Conditioning For Vehicles (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
  • Details Of Heat-Exchange And Heat-Transfer (AREA)
US13/291,440 2010-11-08 2011-11-08 Condenser Abandoned US20120111547A1 (en)

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JP2010249466A JP5651431B2 (ja) 2010-11-08 2010-11-08 コンデンサ

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US20130340451A1 (en) * 2012-06-21 2013-12-26 Trane International Inc. System and Method of Charge Management
US20140014296A1 (en) * 2012-07-13 2014-01-16 Keihin Thermal Technology Corporation Condenser
EP3062042A1 (de) * 2015-02-27 2016-08-31 MAHLE International GmbH Fluidsammler
US20180017297A1 (en) * 2016-07-12 2018-01-18 Keihin Thermal Technology Corporation Condenser
US20190092135A1 (en) * 2016-04-08 2019-03-28 Denso Corporation Heat exchanger
US10436527B2 (en) 2014-10-16 2019-10-08 Daikin Industries, Ltd. Refrigerant diverter
US20200109902A1 (en) * 2017-03-27 2020-04-09 Daikin Industries, Ltd. Heat exchanger and air conditioner
US10989453B2 (en) * 2019-02-27 2021-04-27 Auras Technology Co., Ltd. Heat exchanger with improved heat removing efficiency
US20220041033A1 (en) * 2020-08-05 2022-02-10 Denso International America, Inc. Hermetically sealed cap for heat exchanger modulator

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JP5651431B2 (ja) * 2010-11-08 2015-01-14 株式会社ケーヒン・サーマル・テクノロジー コンデンサ
DE102013204294A1 (de) * 2013-03-12 2014-10-02 Behr Gmbh & Co. Kg Kondensatorbaugruppe für Kältemittel
JP6572040B2 (ja) * 2014-08-08 2019-09-04 株式会社ケーヒン・サーマル・テクノロジー コンデンサ
EP3112778B1 (en) * 2015-06-29 2018-01-17 MAHLE International GmbH Condenser
DE102015114562A1 (de) * 2015-09-01 2017-03-02 Halla Visteon Climate Control Corp. Wärmeübertrager mit Sammlerrohr
WO2021177122A1 (ja) * 2020-03-03 2021-09-10 株式会社デンソーエアクール 受液器一体凝縮器

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US20030110793A1 (en) * 2001-12-19 2003-06-19 Kwangheon Oh Refrigeration cycle and method for determining capacity of receiver thereof
US20050126210A1 (en) * 2003-12-12 2005-06-16 Knecht John W. Service cartridge for a receiver in a condenser system
JP2005315501A (ja) * 2004-04-28 2005-11-10 Nikkei Nekko Kk 受液器付き熱交換器
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US20130340451A1 (en) * 2012-06-21 2013-12-26 Trane International Inc. System and Method of Charge Management
US9267717B2 (en) * 2012-06-21 2016-02-23 Trane International Inc. System and method of charge management
US20140014296A1 (en) * 2012-07-13 2014-01-16 Keihin Thermal Technology Corporation Condenser
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US9285173B2 (en) * 2012-07-13 2016-03-15 Keihin Thermal Technology Corporation Condenser
US10436527B2 (en) 2014-10-16 2019-10-08 Daikin Industries, Ltd. Refrigerant diverter
EP3062042A1 (de) * 2015-02-27 2016-08-31 MAHLE International GmbH Fluidsammler
US20190092135A1 (en) * 2016-04-08 2019-03-28 Denso Corporation Heat exchanger
US10845124B2 (en) * 2016-04-08 2020-11-24 Denso Corporation Heat exchanger
US10094601B2 (en) * 2016-07-12 2018-10-09 Keihin Thermal Technology Corporation Condenser
US20180017297A1 (en) * 2016-07-12 2018-01-18 Keihin Thermal Technology Corporation Condenser
US20200109902A1 (en) * 2017-03-27 2020-04-09 Daikin Industries, Ltd. Heat exchanger and air conditioner
US11181328B2 (en) * 2017-03-27 2021-11-23 Daikin Industries, Ltd. Heat exchanger and air conditioner
US10989453B2 (en) * 2019-02-27 2021-04-27 Auras Technology Co., Ltd. Heat exchanger with improved heat removing efficiency
US20220041033A1 (en) * 2020-08-05 2022-02-10 Denso International America, Inc. Hermetically sealed cap for heat exchanger modulator
US11712942B2 (en) * 2020-08-05 2023-08-01 Denso International America, Inc. Hermetically sealed cap for heat exchanger modulator

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US20150184908A1 (en) 2015-07-02
DE102011085837A1 (de) 2012-05-10
CN102706045A (zh) 2012-10-03
JP5651431B2 (ja) 2015-01-14
CN102706045B (zh) 2016-04-27
JP2012102900A (ja) 2012-05-31
US9587862B2 (en) 2017-03-07
CN202361708U (zh) 2012-08-01

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