US20120285659A1 - Heat exchanger, a food handler including the heat exchanger, and a manufacturing method of the heat exchanger - Google Patents

Heat exchanger, a food handler including the heat exchanger, and a manufacturing method of the heat exchanger Download PDF

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Publication number
US20120285659A1
US20120285659A1 US13/522,298 US201013522298A US2012285659A1 US 20120285659 A1 US20120285659 A1 US 20120285659A1 US 201013522298 A US201013522298 A US 201013522298A US 2012285659 A1 US2012285659 A1 US 2012285659A1
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United States
Prior art keywords
heat exchanger
flow channel
manufacturing
flow
flowing fluid
Prior art date
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Abandoned
Application number
US13/522,298
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English (en)
Inventor
Sang Gu Sim
Chan Jung Park
Sung Jin Kim
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.)
Coway Co Ltd
Original Assignee
Woongjin Coway Co Ltd
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 Woongjin Coway Co Ltd filed Critical Woongjin Coway Co Ltd
Assigned to WOONGJIN COWAY CO., LTD. reassignment WOONGJIN COWAY CO., LTD. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: KIM, SUNG JIN, PARK, CHAN JUNG, SIM, SANG GU
Publication of US20120285659A1 publication Critical patent/US20120285659A1/en
Abandoned legal-status Critical Current

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Classifications

    • 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
    • F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/16—Heat-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 being arranged in parallel spaced relation
    • F28D7/1684—Heat-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 being arranged in parallel spaced relation the conduits having a non-circular cross-section
    • 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
    • F28D21/00—Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
    • F28D21/0001—Recuperative heat exchangers
    • F28D21/0003—Recuperative heat exchangers the heat being recuperated from exhaust gases
    • 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
    • F28F1/40—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only inside the tubular element
    • F28F1/405—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only inside the tubular element and being formed of wires
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F3/00—Plate-like or laminated elements; Assemblies of plate-like or laminated elements
    • F28F3/02—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations
    • F28F3/04—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations the means being integral with the element
    • F28F3/048—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations the means being integral with the element in the form of ribs integral with the element or local variations in thickness of the element, e.g. grooves, microchannels
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F7/00—Elements not covered by group F28F1/00, F28F3/00 or F28F5/00
    • F28F7/02—Blocks traversed by passages for heat-exchange media
    • 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
    • F28D21/00—Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
    • F28D2021/0019—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
    • F28D2021/0042—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for foodstuffs
    • 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
    • F28D21/00—Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
    • F28D21/0001—Recuperative heat exchangers
    • F28D21/0012—Recuperative heat exchangers the heat being recuperated from waste water or from condensates
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F2255/00—Heat exchanger elements made of materials having special features or resulting from particular manufacturing processes
    • F28F2255/16—Heat exchanger elements made of materials having special features or resulting from particular manufacturing processes extruded
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/56—Heat recovery units
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T29/00—Metal working
    • Y10T29/49—Method of mechanical manufacture
    • Y10T29/4935—Heat exchanger or boiler making

Definitions

  • Exemplary embodiments of the present invention relate to a heat exchanger, a food handler including the heat exchanger, and a method of manufacturing the heat exchanger; and, particularly, to a heat exchanger in which a plurality of flow channels are formed therein by an extruding and cutting process and heat transfer occurs between the flow channels to simplify a working process, and a food handler including the heat exchanger, and a method of manufacturing the heat exchanger.
  • a heat exchanger is used to transfer heat from a fluid having high temperature to a fluid having low temperature via a heat transfer wall.
  • the most common structure of a heat exchanger includes a metal tube serving as the heat transfer wall.
  • heat exchangers such as a water injection type, a double-pipe type, a finned multi-tube type, and a shell and tube type.
  • the double-pipe heat exchanger consists of an inner tube and an outer tube, in which heat transfer occurs between a fluid in the inner tube and a fluid existing in a U-shaped portion which is positioned between the inner tube and the outer tube.
  • the double-pipe heat exchanger has a simple construction, but its ability to transfer heat is limited.
  • the shell and tube heat exchanger consists of a large shell with a bundle of tubes inside it.
  • the design of the heat exchanger may include a parallel-flow arrangement in which hot and cold fluids move in the same direction, a counter-flow arrangement in which hot and cold fluids move in the opposite direction, and a cross-flow arrangement in which fluids move in cross flow.
  • Heat transfer mediums widely used in the industries include water, vapor, air, combusted gas, oil, mercury, sodium, potassium, and Dowtherm which is a mixture of biphenyl and diphenyl oxide.
  • a plate fin heat exchanger 10 includes hollow circular tubes 12 and plate fins 14 in which the circular tubes 12 are inserted and fixed.
  • a hot fluid flows in the circuit tubes 12 (see reference numeral 18 ), and the plate fins 14 closely fixed to the circuit tubes 12 are stacked at regular intervals along an axial direction of the circular tubes 12 .
  • the heat of high temperature in the circular tubes 12 is dispersed to the plate fins 14 through a thermal diffusion process.
  • cooling air 16 having low temperature flowing to the plate fins 14 cools the plate fins 14 , thereby continuously performing the heat transfer function.
  • the plate fin heat exchanger 10 heat transfer efficiency is determined depending upon the fitting degree of the circular tube 12 to the plate fin 14 .
  • the circular tubes may be deformed at the time of fitting or using according to the thickness of the plate fin 14 , thereby deteriorating the quality.
  • the cross area of a flow passage of the circular tube 12 is generally small, the pressure load of the hot fluid flowing in the circular tube is significant, so that a high-pressure pump or a high-pressure blower fan is required.
  • a method of a heat exchanger with increased number of circular tubes 12 in order to decrease a pressure load has been proposed. The method has a drawback of increasing processing costs and ultimately manufacturing costs.
  • the present invention has been made to solve the above-described problems, and an object of the present invention is to provide a heat exchanger in which a body including a plurality of flow channels which are formed therein by extruding and cutting a metal shaped member, and a cover member attached to the body, are combined, thereby simplifying the working process and lowering manufacturing costs, and a food handler including the heat exchanger, and a method of manufacturing the heat exchanger.
  • a heat exchanger in which a heat transfer between a plurality of flowing fluids occurs, including a plurality of flow channels extending in a different direction so that the plurality of flowing fluids flows in a different direction.
  • the flow channel may have a first flow channel, serving as a passage for a first flowing fluid, and a second flow channel serving as a passage for a second flowing fluid, and the heat transfer may occur between the first flowing fluid and the second flowing fluid in the cross direction in the heat exchanger.
  • the first flow channel and the second flow channel may be alternatively disposed in the body.
  • the heat exchanger further includes a pair of cover members which is fastened to both ends of the body in the first direction.
  • the first flow channel may serve as a passage of the first flowing fluid, which passes through the cover member, in the first direction.
  • the first and second flow channels may be formed in the body in the first direction by an extruding process.
  • the first or second flow channel may be provided with a heat exchange fin with a predetermined shape protruding from the flow channel.
  • the heat exchange fin may be oppositely disposed in a staggered manner on an inner surface of either the first or second flow channel which is provided with the heat exchange fin.
  • the second flow channel may be formed to communicate with a lateral surface of the body by a cutting process.
  • the cover member can prevent the second flowing fluid, which flows through the second flow channel from the lateral surface of the body, from being discharged from the body in the first direction.
  • a method of manufacturing the heat exchanger set forth in the above-described invention including: extruding a body so that some of the plurality of flow channels in any one direction are formed to have a different height; cutting a lateral surface of the body in a direction different from the direction of the flow channel by a depth until a distal end of the flow channel having the different height is exposed outward; and attaching a cover member to both ends of the flow channel having the exposed distal end.
  • a food handler including the heat exchanger set forth in the above-described invention, wherein heat transfer occurs between exhaust gas generated from a drying oven of the food handler and cold air supplied from an exterior flow in the heat exchanger.
  • a food handler including the heat exchanger manufactured by the method.
  • the present invention is characterized in that as the flowing fluids having thermal energy of the different temperatures flow in the flow channels formed in the body in the cross or perpendicular direction, the heat transfer can occur effectively. Further, the heat exchanger can be rapidly manufactured with a simple method employing the above-described simultaneous extruding process, the process of cutting the upper and lower ends of the body, and the process of attaching the cover member to the front and rear surfaces of the body when the body is formed, thereby improving its productivity and thus reducing the cost of manufacturing.
  • FIG. 1 is a perspective view illustrating a configuration of a heat exchanger of the related art.
  • FIG. 2 is a perspective view illustrating a configuration of a heat exchanger according to one embodiment of the present invention.
  • FIG. 3 is a perspective view illustrating a state in which a body, which is a constitutional element of the heat exchanger according to the present invention, is formed by an extruding process.
  • FIG. 4 is a perspective view illustrating a state in which second flow channels formed in the body by a cutting process of a lateral surface of the body is exposed from the lateral surface of the body.
  • FIG. 5 is an exploded perspective view illustrating a state in which a pair of cover members is engaged with front and rear surfaces of the body.
  • FIG. 6 is a front view when seen from direction A in FIG. 4 .
  • FIG. 7 is a plan view when seen from direction B in FIG. 4 .
  • FIG. 8 is a cross-sectional view taken along the line C-C in FIG. 4 .
  • FIG. 9 is a cross-sectional view taken along the line D-D in FIG. 4 .
  • the configuration of a heat exchanger 100 will be described with reference to FIGS. 2 to 5 .
  • the heat exchanger 100 includes a body 110 having a plurality of flow channels 120 formed therein, and a pair of cover members 130 fastened to both ends of the front and rear surfaces of the body 110 .
  • Fastening grooves 112 formed in corner portions of the front and rear surfaces of the body 110 are provided to correspond to fastening holes 131 formed in corner portions of the cover member 130 , so that the fastening grooves 112 are engaged with the fastening holes 131 by separate fastening members (not illustrated).
  • the body 110 is made of single piece which can be made by an extruding process, and has the same cross section at any point in a longitudinal direction thereof.
  • the body is provided as a product of a desired shape by the extruding process within a short time.
  • the plurality of flow channels 120 have first flow channels 122 serving as a passage for a first flowing fluid passing through the cover member 130 , and second flow channels 124 serving as a second flowing fluid and selectively communicating with a lateral surface of the body 110 .
  • a moving direction of the first flowing fluid passing the front and rear surfaces of the body is referred to as a first direction 102
  • a moving direction of the second flowing fluid passing upper and lower ends of the lateral surface of the body is referred to as a second direction 104 .
  • the first direction is set as an X-axis on a rectangular coordinate system
  • the second direction is set as a Y-axis.
  • the first and second directions are set to be perpendicular to each other for convenience, but the direction setting is not limited thereto.
  • the first flowing fluid flows in the rear surface of the body 110 in the first direction 102 , and flows out from the front surface of the body 110 via the first flow channels 122 .
  • the flow of the first flowing fluid is not interrupted by the cover member 130 in the above process.
  • the second flowing fluid flows in the upper end of the lateral surface of the body 110 in the second direction 104 , and flows out from the lower end of the lateral surface of the body 110 via the second flow channels 124 .
  • the communication of the upper and lower ends of the lateral side of the body 110 and the second flow channels 124 is achieved by a process of cutting the upper and lower ends of the lateral side of the body 110 .
  • the body 110 is provided on both sides thereof with a constant stepped portion which is formed by the above cutting process.
  • the stepped portion means a height difference between a machined surface 116 which is subjected to the cutting process, and a non-machined reference surface 118 .
  • the second flow channels 124 are exposed to both sides of the body 110 due to the stepped portion.
  • the cover member 130 prevents the second flowing fluid from being discharged from the front surface of the body 110 . This is achieved by forming a configuration in which the cover member 130 closes the portion of the second flow channels 124 which communicate with the front and rear surfaces of the body 110 .
  • the cover member 130 is provided with through-holes 134 through which the first flowing fluid entering the body 110 in the first direction 102 flows. These through-holes 134 are formed by a process of piercing a metal plate using a press machine. A shield portion 132 formed between the through-holes 134 prevents the second flowing fluid from being leaked from the front and rear surfaces of the body 110 . Since a sealing member (not illustrated) is attached to the inner surface of the cover member 130 , it is possible to prevent the flowing fluid from being leaked in the case in which the cover member 130 is brought in close contact with the body 110 .
  • the first flow channels 122 and the second flow channels 124 are alternatively and continuously disposed in the body 110 , as illustrated in FIG. 6 . That is, since the second flow channels 124 are disposed on both adjacent sides of the first flow channels 122 , the heat transfer can smoothly occur between the first flowing fluid flowing in the first flow channels 122 and the second flowing fluid flowing in the second flow channels 124 .
  • a plurality of heat exchange fins 114 of a predetermined shape are formed between the flow channels 120 to enhance the heat exchange performance between the first and second flowing fluids.
  • the heat exchanger 100 can be applied to all apparatuses in which the heat exchange or distribution should be performed, and more particularly, to a heat exchanger for a food handler.
  • a heat exchanger for a food handler hot and humid exhaust gas generated from a drying oven in which food garbage is ground and dried, and cold air supplied from the exterior, flow in the flowing channels 120 of the heat exchanger 100 in a cross direction to exchange the heat.
  • the second flowing fluid entering the second flow channels 124 in the second direction 104 flows in a streamlined way due to the presence of the heat exchange fins 114 , so that the second flowing fluid comes in contact with the surface of the second flow channels 124 .
  • This increases mobility of the heat through heat conduction between the flowing channels 120 .
  • the heat exchanger fins 114 are formed in a staggered pattern on both sidewalls of the second flow channels 124 in the second direction 104 .
  • the flow channels 120 formed in the body 110 by the extruding process have different length in the second direction 104 . That is, referring to FIG. 8 , the second flow channels 124 are formed rather longer than the first flow channels 122 in the second direction 104 , so that the upper and lower ends of the second flow channels 124 are formed closer to the side of the body 110 than the first flow channels 122 .
  • FIG. 9 illustrates the cross section of the body 110 which is subjected to the cutting process. The cutting process is carried out until the upper and lower portions of the second flow channels 124 are exposed outward, and the upper and lower portions of the first flow channels 122 are not exposed.
  • the second flowing fluid entered through the upper end of the body 110 is discharged from the lower end of the body 110 through the second flow channels 124 .
  • the second flowing fluid flows in the second flow channels 124 in the streamlined way with a zigzag pattern due to the protruding shape of the heat exchange fins 114 (see reference numeral 125 ).
  • the extruding process is carried out by extruding a molten shaping material into a mould having the shape corresponding to the body 110 of the present invention using a pump.
  • the extruding process is classified into a positive extrusion method in which an extruding direction of the shaping material is the same as a direction of pressure applied from the exterior, and a negative extrusion method in which the extruding direction of the shaping material is opposite to the direction of pressure applied from the exterior.
  • the plurality of flow channels 120 is evenly formed in the body 110 through the above-described simultaneous extruding process.
  • FIG. 3 illustrates the body 110 formed by the extruding process, in which the flow channels 120 are formed to have the uniform shape in the first direction 102 (X-axis).
  • FIG. 4 illustrates the state in which the upper and lower sides of the body 110 are subjected to the cutting process. Through the process, the second flowing fluid enters the second flow channels 124 via the upper surface of the body 110 .
  • the cover members 130 are attached to the front and rear surfaces of the body 110 .
  • the cover member 130 prevents the second flowing fluid from being discharged from the body 110 in the first direction 102 . This is achieved by forming the configuration in which the cover member 130 closes the portion of the second flow channels 124 which communicate with the front and rear surfaces of the body 110 .
  • the present invention is characterized in that as the flowing fluids having thermal energy of the different temperatures flow in the flow channels formed in the body in the cross or perpendicular direction, the heat transfer can occur effectively. Further, the heat exchanger can be easily and rapidly manufactured with a simple method employing the above-described simultaneous extruding process once, the process of cutting the upper and lower ends of the body, and the process of attaching the cover member to the front and rear surfaces of the body when the body is formed, thereby improving its productivity and thus reducing the cost of manufacturing.

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Geometry (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
  • Processing Of Solid Wastes (AREA)
  • Cooling Or The Like Of Semiconductors Or Solid State Devices (AREA)
US13/522,298 2010-01-14 2010-09-29 Heat exchanger, a food handler including the heat exchanger, and a manufacturing method of the heat exchanger Abandoned US20120285659A1 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
KR10-2010-0003611 2010-01-14
KR1020100003611A KR101183292B1 (ko) 2010-01-14 2010-01-14 열교환기, 상기 열교환기를 포함하는 음식물 처리기 및 상기 열교환기의 제조 방법
PCT/KR2010/006649 WO2011087203A2 (ko) 2010-01-14 2010-09-29 열교환기, 상기 열교환기를 포함하는 음식물 처리기 및 상기 열교환기의 제조 방법

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US20120285659A1 true US20120285659A1 (en) 2012-11-15

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US (1) US20120285659A1 (ko)
EP (1) EP2525182A2 (ko)
JP (1) JP5882909B2 (ko)
KR (1) KR101183292B1 (ko)
CN (1) CN102713491A (ko)
WO (1) WO2011087203A2 (ko)

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US10900312B2 (en) 2015-04-28 2021-01-26 Thru Tubing Solutions, Inc. Plugging devices and deployment in subterranean wells
US10927639B2 (en) 2016-12-13 2021-02-23 Thru Tubing Solutions, Inc. Methods of completing a well and apparatus therefor
US11022248B2 (en) 2017-04-25 2021-06-01 Thru Tubing Solutions, Inc. Plugging undesired openings in fluid vessels
US11293578B2 (en) 2017-04-25 2022-04-05 Thru Tubing Solutions, Inc. Plugging undesired openings in fluid conduits
US11427751B2 (en) 2015-04-28 2022-08-30 Thru Tubing Solutions, Inc. Flow control in subterranean wells
US11851611B2 (en) 2015-04-28 2023-12-26 Thru Tubing Solutions, Inc. Flow control in subterranean wells

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WO2024173978A1 (en) * 2023-02-20 2024-08-29 A & K Building Co. Pty. Limited Heat exchanger for a shower

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WO2011087203A2 (ko) 2011-07-21
CN102713491A (zh) 2012-10-03
JP2013517448A (ja) 2013-05-16
JP5882909B2 (ja) 2016-03-09
EP2525182A2 (en) 2012-11-21
WO2011087203A3 (ko) 2011-09-09
KR20110083400A (ko) 2011-07-20
KR101183292B1 (ko) 2012-09-14

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