WO1999066281A1 - Condenser for heat exchanger systems - Google Patents

Condenser for heat exchanger systems Download PDF

Info

Publication number
WO1999066281A1
WO1999066281A1 PCT/KR1998/000158 KR9800158W WO9966281A1 WO 1999066281 A1 WO1999066281 A1 WO 1999066281A1 KR 9800158 W KR9800158 W KR 9800158W WO 9966281 A1 WO9966281 A1 WO 9966281A1
Authority
WO
WIPO (PCT)
Prior art keywords
tube
liquid
refrigerant
condenser
condensing
Prior art date
Application number
PCT/KR1998/000158
Other languages
English (en)
French (fr)
Inventor
Chul Soo Lee
Original Assignee
Chul Soo Lee
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 Chul Soo Lee filed Critical Chul Soo Lee
Priority to AU79389/98A priority Critical patent/AU7938998A/en
Priority to PCT/KR1998/000158 priority patent/WO1999066281A1/en
Priority to DE69818696T priority patent/DE69818696T2/de
Priority to EP98929873A priority patent/EP1015835B1/de
Priority to JP2000555058A priority patent/JP3333500B2/ja
Priority to CN98808067.2A priority patent/CN1103434C/zh
Publication of WO1999066281A1 publication Critical patent/WO1999066281A1/en

Links

Classifications

    • 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
    • F28D7/00Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/0008Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one medium being in heat conductive contact with the conduits for the other medium
    • 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
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F1/00Tubular elements; Assemblies of tubular elements
    • F28F1/10Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
    • F28F1/12Tubular 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
    • F28F1/14Tubular 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 and extending longitudinally
    • F28F1/16Tubular 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 and extending longitudinally the means being integral with the element, e.g. formed by extrusion
    • 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
    • F28D2021/0068Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for refrigerant cycles
    • F28D2021/007Condensers

Definitions

  • the present invention relates, in general, to a condenser for heat exchanger systems and, more particularly, to a condenser capable of reducing a compressed refrigerant, having high temperature and high pressure, from a vapor phase to a liquid phase.
  • a heat exchanger system such as a refrigerator, freezer or refrigerated display case is widely used for preserving food and drink at cool temperatures (for example, 2-5°C) for a lengthy period of time.
  • Such a heat exchange system is operated by a refrigerating cycle.
  • Fig. 1 is a view illustrating a typical refrigerating cycle in a heat exchanger system.
  • the typical refrigerating cycle includes a compressor 1, condenser 2, capillary tube 3, evaporator 4 and accumulator 5.
  • the circulation of a refrigerant in the heat exchanger system is described below. That is, a refrigerant in the heat exchanger system is compressed by the compressor 1, thus having relatively high temperature and high pressure.
  • the compressed refrigerant is introduced into a condenser 2, having a long refrigerant tube, in order to reduce the refrigerant from a vapor phase to a liquid phase. Thereafter, the liquid refrigerant in the condenser 2 is introduced into a capillary tube 3.
  • the liquid refrigerant turns into a mixed refrigerant which consists of the vapor and liquid phases and has relatively low temperature and low pressure.
  • the above mixed refrigerant is quickly vaporized in an evaporator 4 while absorbing heat from the surroundings of the heat exchanger system.
  • the mixed refrigerant in the evaporator 4 is introduced into an accumulator 5 in order to be divided into the vapor and the liquid refrigerants.
  • Such an accumulator 5 comprises intake and discharging tubes and a housing. That is, the vapor refrigerant in the mixed refrigerant is only introduced into the compressor 1 passing through the discharging tube, while the liquid refrigerant in the mixed refrigerant is discharged into and kept in the housing.
  • the refrigerant is compressed by the compressor 1 and is introduced into the condenser 2. At this time, the compressed refrigerant has relatively low temperature while passing through the long refrigerant tube of the condenser 2. Thereafter, the refrigerant, having low temperature, passes through the capillary tube 3, thereby allowing the current speed of the refrigerant to be fast. The refrigerant is discharged from the capillary tube 3 to the evaporator 4. In such a case, since the high pressure of the refrigerant falls, the refrigerant is quickly vaporized in the evaporator 4 while absorbing heat from the surroundings of the heat exchanger system, thus forming cool air to be circulated in the heat exchanger system.
  • the condenser consists of a long refrigerant tube between the compressor and the capillary tube.
  • the above long refrigerant tube is bent in a desired shape by a bending process.
  • the high temperature of the refrigerant spontaneously falls while the refrigerant passes through the long refrigerant tube of the condenser 2.
  • the heat of the refrigerant may be forcibly radiated by a cooling fan mounted around the condenser 2 when necessary.
  • the performance of the condenser namely, the liquefaction of a vapor refrigerant, is based on the radiant heat efficiency of the vapor refrigerant.
  • the above condenser is problematic in that the radiant heat of the refrigerant passing through the condenser is unexpectedly reduced during the height of the warm-weather seasons.
  • the cooling fan is forcibly operated, thereby generating a noise and increasing power consumption.
  • an object of the present invention is to provide a condenser for heat exchanger systems , which has a radiating pipe filled with a condensing medium containing a liquid such as a brine, antifreezing solution or water having a relatively high density, thus increasing the radiant heat of the condenser and reducing the electric power consumption of the condenser, and prolonging the life span of the condenser.
  • the present invention provides a condenser for heat exchanger systems, comprising: a condensing tube connected to a refrigerant tube located between a compressor and a capillary tube in order to allow a refrigerant in a heat exchanger system to pass through the condensing tube; a liquid tube integrally formed on a side wall of the condensing tube by an extrusion process; and a radiating pipe having a long zigzag shape and including a plurality of radiating fins formed on its outer surface, and mounted to the liquid tube in such a manner that both ends of the liquid tube are connected to a liquid supplying inlet and a drain outlet of the radiating pipe, respectively, so a
  • At least two or more condensing tubes are horizontally and integrally formed on both side walls of the liquid tube by an extrusion process.
  • Fig. 1 is a view illustrating a typical refrigerating cycle in a heat exchanger system
  • Fig. 2 is a view illustrating a refrigerating cycle in a heat exchanger system in accordance with the present invention
  • Fig. 3 is a view illustrating the construction of a condenser for heat exchanger systems in accordance with the first embodiment of the present invention.
  • Fig. 4 is an expanded sectional view illustrating the condenser of Fig. 3;
  • Fig. 5 is an expanded sectional view illustrating the construction of a condenser for heat exchanger systems in accordance with the second embodiment of the present invention. Best Mode for Carrying Out the Invention
  • Fig. 2 is a view illustrating a refrigerating cycle in a heat exchanger system in accordance with the present invention.
  • Figs. 3 and 4 are views illustrating the construction of a condenser for heat exchanger systems in accordance with the first embodiment of the present invention.
  • the refrigerating cycle "A" includes a compressor 10, condenser 20, capillary tube 30, evaporator 40 and accumulator 50.
  • the circulation of a refrigerant in the heat exchanger system is described below. That is, the refrigerant in the heat exchanger system is compressed by the compressor 10, thus having relatively high temperature and high pressure.
  • the compressed refrigerant is introduced into the condenser 20, having a long refrigerant tube, in order to reduce the refrigerant from a vapor phase to a liquid phase. Thereafter, the liquid refrigerant in the condenser 20 is introduced into the capillary tube 30.
  • the liquid refrigerant turns into a mixed refrigerant which consists of the vapor and liquid phases and has low temperature and low pressure.
  • the above mixed refrigerant is quickly vaporized in the evaporator 40 while absorbing heat from the surroundings of the heat exchanger system.
  • the mixed refrigerant in the evaporator 40 is introduced into the accumulator 50 in order to be divided into the vapor and liquid refrigerants.
  • the condenser 20 includes a condensing tube 21 and liquid tube 22. That is, the condensing tube 21 communicates with a refrigerant tube 26 located between the compressor 10 and the capillary tube 30 as shown in Fig. 3.
  • the condensing tube 21 is linearly illustrated in Fig. 3, but it actually has a long spiral shape in order to improve the efficiency of the condenser 20.
  • the liquid tube 22 is integrally formed on a side wall 23 of the condensing tube 21 of the condenser 20.
  • a liquid tube 22 is connected to a radiating pipe 25, having a long zigzag shape, in such a manner that both en,ds of the liquid tube 22 are connected to a liquid supplying inlet 25b and a drain outlet 25c of the radiating pipe 25, respectively.
  • a plurality of radiating fins 25a are formed on the outer surface of the radiating pipe 25.
  • the liquid tube 22 is filled with a condensing medium such as a calcium chloride solution, sodium chloride or magnesium chloride solution containing a medium such as a brine, antifreezing solution or water having a relatively high density.
  • slits 23a are longitudinally formed at both top and bottom portions of the side wall
  • the length of the radiating pipe 25 has to be long. That is, another extending tube (not shown), having a condensed construction, is connected between the liquid supplying inlet 25b and the drain outlet 25c of the liquid tube 22 at its both ends.
  • a pump (not shown) is mounted to the radiating pipe 25 at a desired position.
  • a cooling fan (not shown), operated by a control means, may be mounted around the radiating pipe 25 in order to improve the radiant heat of the radiating pipe 25.
  • the manufacturing process of the condenser according to this invention is described below.
  • the liquid tube 22 is integrally formed on the condensing tube 21 by an extrusion process, thus allowing the configuration of the condensing and liquid tubes 21 and 22 to be formed into a peanut shape. Thereafter, the single body of the condensing and liquid tubes 21 and 22 is cut in a desired length. In this case, since the slits 23a are longitudinally formed both top and bottom portions of the side wall 23 formed between the condensing and liquid tubes 21 and 22, thus allowing the condensing and liquid tubes 21 and 22 to be widely distanced from each other when necessary.
  • both ends of the condensing tube 21 are respectively connected to the refrigerant tube 26 by a welding process, thus allowing the refrigerant to flow through the condensing tube 21.
  • both ends of the liquid tube 22 are connected to the liquid supplying inlet 25b and the drain outlet 25c of the radiating pipe 25, respectively, thus allowing the condensing medium to be circulated through the liquid tube 22 and the radiating pipe 25.
  • the circulation of a refrigerant in the heat exchanger system is described below. That is, the refrigerant in the heat exchanger system is compressed by the compressor 10, thus having relatively high temperature and high pressure.
  • the compressed refrigerant is introduced into the condenser 20 in order to reduce the refrigerant from a vapor phase to a liquid phase.
  • the liquid refrigerant in the condenser 20 is introduced into the capillary tube 30.
  • the liquid refrigerant turns into a mixed refrigerant which consists of the vapor and liquid phases and has low temperature and low pressure.
  • the above mixed refrigerant is quickly vaporized in the evaporator 40 while absorbing heat from the surroundings of the heat exchanger system.
  • the condensing medium having high density, passes from the radiating pipe 25 to the liquid tube 22.
  • the heat of the vapor refrigerant, having about 80 °C and passing through the condensing tube 21 is transmitted to the condensing medium which has a normal temperature and passes through the liquid tube 22.
  • the vapor refrigerant easily turns into the liquid refrigerant, while the condensing medium has relatively high temperature.
  • the circulation of the condensing medium, having high temperature is described below.
  • the condensing medium has relatively low temperature while spontaneously passing through the long radiating pipe 25. That is, the condensing medium, having relatively high temperature and passing the liquid supplying inlet 25b, is introduced into the upper portion of the radiating pipe 25. Thereafter, the high temperature of the condensing medium falls while the refrigerant passes from the upper portion to the lower portion of the radiating pipe 25.
  • the condensing medium, having a normal temperature is discharged into the drain outlet 25c of the radiating pipe 25.
  • the condensing medium having relatively high temperature and passing the liquid supplying inlet 25b, forcibly passes from the upper portion to the lower portion of the radiating pipe 25 by a pump (not shown) which is mounted to the radiating pipe 25 at a desired position.
  • the radiating pipe 25, having a condensed construction is exposed to the outside of the condenser 20, thus allowing the piping work of the ra,diating pipe 25 to be easily carried out.
  • a cooling fan (not shown), operated by a control means, may be mounted around the radiating pipe 25 in order to effectively increase the radiant heat of the radiating pipe 25.
  • Fig. 5 is a view illustrating the construction of a condenser for heat exchanger systems in accordance with the second embodiment of the present invention.
  • the condenser includes a liquid tube 22 and two condensing tubes 21a and 21b. That is, the condensing tubes 21a and 21b are horizontally and integrally formed on both side walls of the liquid tube 22 by an extrusion process.
  • the heat of vapor refrigerants, passing through the condensing tubes 21a and 21b is more quickly transmitted to the condensing medium passing through the liquid tube 22.
  • the radiant heat of the condenser is effectively and quickly carried out.
  • a condenser for heat exchanger systems of this invention is provided with a radiating pipe filled with a condensing medium containing a liquid such as a brine, antifreezing solution or water having a relatively high density, thus increasing the radiant heat of the condenser and reducing the electric power consumption of the condenser, and prolonging the life span of the condenser.
  • a condensing medium containing a liquid such as a brine, antifreezing solution or water having a relatively high density
  • the condensing medium having heat transmitted from a vapor refrigerant, has a normal temperature while passing through the long radiating pipe.
  • the condensing medium having relatively high temperature, is forcibly circulated through the radiating pipe by a pump.
  • a cooling fan may be mounted around the radiating pipe in order to effectively increase the radiant heat of the radiating pipe.
  • the radiating pipe having a condensed construction, is exposed to the outside of the condenser, thus allowing the piping work of the radiating pipe to be easily carried out.

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Geometry (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
PCT/KR1998/000158 1998-06-15 1998-06-15 Condenser for heat exchanger systems WO1999066281A1 (en)

Priority Applications (6)

Application Number Priority Date Filing Date Title
AU79389/98A AU7938998A (en) 1998-06-15 1998-06-15 Condenser for heat exchanger systems
PCT/KR1998/000158 WO1999066281A1 (en) 1998-06-15 1998-06-15 Condenser for heat exchanger systems
DE69818696T DE69818696T2 (de) 1998-06-15 1998-06-15 Kondensator für wärmeaustauschsysteme
EP98929873A EP1015835B1 (de) 1998-06-15 1998-06-15 Kondensator für wärmeaustauschsysteme
JP2000555058A JP3333500B2 (ja) 1998-06-15 1998-06-15 熱交換装置の凝縮機構造
CN98808067.2A CN1103434C (zh) 1998-06-15 1998-06-15 热交换设备中的冷凝器

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/KR1998/000158 WO1999066281A1 (en) 1998-06-15 1998-06-15 Condenser for heat exchanger systems

Publications (1)

Publication Number Publication Date
WO1999066281A1 true WO1999066281A1 (en) 1999-12-23

Family

ID=19531053

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/KR1998/000158 WO1999066281A1 (en) 1998-06-15 1998-06-15 Condenser for heat exchanger systems

Country Status (6)

Country Link
EP (1) EP1015835B1 (de)
JP (1) JP3333500B2 (de)
CN (1) CN1103434C (de)
AU (1) AU7938998A (de)
DE (1) DE69818696T2 (de)
WO (1) WO1999066281A1 (de)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003021474A (ja) * 2001-07-04 2003-01-24 Daikin Ind Ltd 熱交換器
WO2004033947A1 (de) * 2002-09-20 2004-04-22 Erbslöh Aluminium Gmbh Wärmetauscher und verfahren zur herstellung eines wärmetauschers sowie stranggepresstes verbundprofil zur verwendung in einem solchen verfahren
WO2004051168A3 (en) * 2002-12-03 2004-08-26 Milind V Rane Tube-tube heat exchangers
EP3760960A4 (de) * 2018-03-01 2021-04-14 Daikin Industries, Ltd. Wärmetauscher

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005291696A (ja) * 2004-03-11 2005-10-20 Tokyo Electric Power Co Inc:The 凝縮器、ヒートポンプ、熱利用装置
JP5130676B2 (ja) * 2006-08-15 2013-01-30 東京電力株式会社 蒸気発生システム
KR102622254B1 (ko) * 2021-12-28 2024-01-08 태성전기(주) 냉장고용 냉매관 제조장치

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0086470A1 (de) * 1982-02-15 1983-08-24 Wilhelm Dr.-Ing. Vox Dreirohrkondensator für Wärmepumpen, insbesondere Koaxialkondensator
DE3411567A1 (de) * 1984-03-29 1985-10-10 Küppersbusch AG, 4650 Gelsenkirchen Waermeuebertrager, insbesondere fuer einen kaeltemittelkreislauf

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0086470A1 (de) * 1982-02-15 1983-08-24 Wilhelm Dr.-Ing. Vox Dreirohrkondensator für Wärmepumpen, insbesondere Koaxialkondensator
DE3411567A1 (de) * 1984-03-29 1985-10-10 Küppersbusch AG, 4650 Gelsenkirchen Waermeuebertrager, insbesondere fuer einen kaeltemittelkreislauf

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003021474A (ja) * 2001-07-04 2003-01-24 Daikin Ind Ltd 熱交換器
JP4631224B2 (ja) * 2001-07-04 2011-02-16 ダイキン工業株式会社 熱交換器
WO2004033947A1 (de) * 2002-09-20 2004-04-22 Erbslöh Aluminium Gmbh Wärmetauscher und verfahren zur herstellung eines wärmetauschers sowie stranggepresstes verbundprofil zur verwendung in einem solchen verfahren
WO2004051168A3 (en) * 2002-12-03 2004-08-26 Milind V Rane Tube-tube heat exchangers
EP3760960A4 (de) * 2018-03-01 2021-04-14 Daikin Industries, Ltd. Wärmetauscher
US11874034B2 (en) 2018-03-01 2024-01-16 Daikin Industries, Ltd. Heat exchanger

Also Published As

Publication number Publication date
JP3333500B2 (ja) 2002-10-15
DE69818696T2 (de) 2004-08-05
CN1103434C (zh) 2003-03-19
JP2002518660A (ja) 2002-06-25
DE69818696D1 (de) 2003-11-06
EP1015835A1 (de) 2000-07-05
EP1015835B1 (de) 2003-10-01
AU7938998A (en) 2000-01-05
CN1266482A (zh) 2000-09-13

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