WO2011087203A2 - 열교환기, 상기 열교환기를 포함하는 음식물 처리기 및 상기 열교환기의 제조 방법 - Google Patents
열교환기, 상기 열교환기를 포함하는 음식물 처리기 및 상기 열교환기의 제조 방법 Download PDFInfo
- Publication number
- WO2011087203A2 WO2011087203A2 PCT/KR2010/006649 KR2010006649W WO2011087203A2 WO 2011087203 A2 WO2011087203 A2 WO 2011087203A2 KR 2010006649 W KR2010006649 W KR 2010006649W WO 2011087203 A2 WO2011087203 A2 WO 2011087203A2
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- WIPO (PCT)
- Prior art keywords
- heat exchanger
- flow
- flow channel
- main body
- fluid
- Prior art date
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Classifications
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- 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
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- 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
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- 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
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- 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
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- 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
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- 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
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- 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
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- 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
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- 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
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- 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
- the present invention relates to a heat exchanger, a food processor including the heat exchanger, and a method of manufacturing the heat exchanger, and more particularly, a plurality of flow channels are formed therein through an extrusion and cutting process to facilitate mutual heat exchange. It relates to a heat exchanger, a food processor including the heat exchanger, and a manufacturing method of the heat exchanger, the operation process of which is simplified.
- a heat exchanger may be defined as a device that transfers heat from a high temperature fluid to a low temperature fluid through a heat transfer wall.
- the most commonly used structure of the heat exchanger is a metal tube as the heat transfer wall, and various examples thereof include a main type, a double tube type, a multi-pin type tube type, and a tube type.
- the double tube heat exchanger has an inner tube and an outer tube, and heat exchange is performed between the fluid inside the inner tube and the fluid in the annular portion between the inner tube and the outer tube. Double tube heat exchangers are simple in construction but require less processing.
- the large-capacity one of the heat exchangers is a bushing type in which several small tubes are placed in a large appearance. Flowing in the same direction in the flow of high fluid and low fluid is cocurrent type, and flowing in the opposite direction is called counterflow type and crossflow type is called crossflow type. Water is usually used for heat transfer media used in industry. Water vapor, air, flue gas, petroleum, mercury, sodium, potassium, and dowtherm, which are a mixture of biphenylether and biphenyl, may be applied.
- the fin heat exchanger 10 includes a hollow circular tube 12 and a plate fin 14 into which the circular tube 12 is inserted and fixed.
- the high-temperature fluid flows into the circular tube 12 (see reference numeral 18), and the plate pins 14 closely fixed to the circular tube 12 are spaced along the axial direction of the circular tube 12 at a predetermined interval. Lamination is formed.
- the heat of the high temperature inside the circular tube 12 is subjected to a process of dispersing through the heat diffusion process to the plate fin 14, in this state toward the plate fin 14
- the cooling air 16 of the low temperature which flows to the cooling plate 16 can be continued heat exchange action.
- the heat exchange efficiency of the fin heat exchanger 10 is determined according to the degree of indentation on the plate fin 14 of the circular tube 12, and deformation or the like occurs in the case of indentation or use according to the thickness of the plate fin 14. This can result in degradation of quality.
- the flow path cross-sectional area of the circular tube 12 is generally small, so that the pressure load of the hot fluid flowing therein is large, thereby requiring a high pressure pump or a high pressure blowing fan.
- a method for overcoming the above problems a method of increasing the number of circular tubes 12 to reduce the pressure load may be derived. In the case of the above method, the disadvantage is that the process cost increases and the manufacturing cost is high. Will be.
- the present invention in order to solve the above problems, by combining the body formed with a plurality of flow channel through the extrusion and cutting process for the metal molding member and the cover member attached to the body to simplify the work process and reduce the manufacturing cost It is an object of the present invention to provide a heat exchanger, a food processor including the heat exchanger, and a manufacturing method of the heat exchanger.
- a heat exchanger is thermally moved between a plurality of flow fluids, and a plurality of penetrating in different directions so that the plurality of flow fluids flow in different directions. It characterized in that it comprises a flow channel.
- the flow channel includes a first flow channel serving as a passage of the first flow fluid and a second flow channel serving as a passage of the second flow fluid, wherein the first flow fluid and the second flow fluid comprise the heat exchanger. It may be desirable for the thermal exchange to be performed in a direction crossing the interior of the.
- first flow channel and the second flow channel are alternately arranged in the body.
- the heat exchanger includes a pair of cover members fastened to both ends of the body in a first direction, and the first flow channel is in the first direction of the first flow fluid entering and exiting through the cover member. It may be desirable to perform the function as a passage.
- the first and second flow channels formed along the first direction in the main body may be formed through extrusion processing.
- a heat exchange fin having a predetermined shape protrudes from the first or second flow channel.
- the heat exchange fins may be alternately arranged on the inner surface facing each other in the one of the first or the second flow channel in which the heat exchange fins are installed.
- the second flow channel be communicable through cutting to the side of the body.
- the cover member may prevent the second flow fluid flowing through the second flow channel from the side of the main body from being discharged from the main body in the first direction.
- a method of manufacturing a heat exchanger the extrusion process step of forming the main body such that the flow channel in any one direction of the plurality of flow channels are formed at different heights, A cutting step of cutting the side surface of the main body in a direction different from the one direction to a depth at which the end of a predetermined flow channel of the flow channels formed at different heights is exposed to the outside, and the end having the exposed end And attaching a cover member to cover the one side side of the predetermined flow channel.
- the exhaust gas generated in the drying furnace of the food processor and the external cooling air heat exchange. do in the heat exchanger, the exhaust gas generated in the drying furnace of the food processor and the external cooling air heat exchange. do.
- the food processor according to another aspect of the present invention provided to achieve the above object includes a heat exchanger manufactured according to the above production method.
- the heat exchanger of the present invention described above, the food processor including the heat exchanger and the method of manufacturing the heat exchanger are a process in which a flow fluid having heat energy of different temperatures flows in the direction in which the flow channels formed in the body cross or cross each other. It is characterized in that the heat exchange through the effective.
- high productivity in that the heat exchanger can be manufactured in a simple manner in a short time through a single extrusion process, a cutting process for the upper and lower ends of the main body, and a process of attaching the cover member to the front and rear surfaces of the main body in the process of forming the main body. And economics are derived.
- FIG. 1 is a perspective view showing a structure of a conventional general heat exchanger
- FIG. 2 is a perspective view showing the structure of a heat exchanger according to an embodiment of the present invention.
- FIG. 3 is a perspective view showing a state in which a main body which is a component of a heat exchanger of the present invention is formed through an extrusion process
- Figure 4 is a perspective view showing a state in which the second flow channel formed in the body through the cutting on the side of the main body exposed to the side of the main body,
- FIG. 5 is an exploded perspective view illustrating a state in which the cover member is coupled to the front and rear surfaces of the main body
- FIG. 6 is a front view as viewed from the direction A of FIG. 4, FIG.
- FIG. 9 is a cross-sectional view taken along the line D-D of FIG. 4.
- FIG. 1 is a perspective view showing the structure of a conventional heat exchanger
- Figure 2 is a perspective view showing the structure of a heat exchanger according to an embodiment of the present invention
- Figure 3 is a body of the heat exchanger of the present invention is an extrusion process
- 4 is a perspective view showing a state formed through
- Figure 4 is a perspective view showing a state in which the second flow channel formed in the body exposed to the side of the main body through the cutting process for the side of the main body
- Figure 5 is a cover member on the front and rear surfaces of the main body Is an exploded perspective view of the state in which the combination is
- Figure 6 is a front view as seen from the direction A of Figure 4
- Figure 7 is a plan view as seen from the direction B of Figure 4
- Figure 8 is a cross-sectional view along the line CC of Figure 4
- Figure 9 Is a cross-sectional view taken along the line DD of FIG. 4.
- the heat exchange apparatus 100 includes a main body 110 in which a plurality of flow channels 120 are formed therein and a cover member 130 fastened to both ends of front and rear surfaces of the main body 110.
- the fastening groove 112 formed at the front and rear edge portions of the main body 110 and the fastening hole 131 formed at the corner portions of the cover member 130 are configured to correspond to each other, so that a separate fastening member (not shown) is used. Mutual coupling is achieved.
- the main body 110 is a single member that can be produced through an extrusion process, so that the cross section at any point can be formed identically, thereby securing a product having a desired shape in a short time through the extrusion process.
- the plurality of flow channels 120 are selectively communicated with side surfaces of the first flow channel 122 and the main body 110 which serve as a passage of the first flow fluid entering and exiting through the cover member 130. It consists of a flow channel (124). 2, the direction in which the first fluid flows through the front and rear surfaces of the main body 110 is moved in the first direction 102 and the direction in which the second fluid flows through the upper and lower sides of the main body 110 moves in the second direction.
- Direction 104 may be defined. In the Cartesian coordinate system, the first direction may be set to the X direction and the second direction to the Y direction.
- the direction setting for the first and second directions is merely set to be orthogonal for convenience, and is not necessarily limited to being set to the orthogonal direction.
- the first flow fluid flows into the rear surface of the main body 110 along the first direction 102 and is discharged to the front surface of the main body 110 through the first flow channel 122.
- the cover member 130 does not interfere with the flow of the first fluid.
- the second fluid flows into the upper end of the side of the main body 110 along the second direction 104 and is discharged to the lower end of the side of the main body 110 through the second flow channel 124.
- the communication between the upper and lower ends of the main body 110 and the second flow channel 124 is performed through the cutting process for the upper and lower ends of the main body 110.
- a constant step is formed on both sides of the main body 110 through the cutting process.
- the step means a height difference between the cutting surface 116 and the unprocessed reference surface 118.
- the second flow channel 124 is exposed to both sides of the main body 110 due to the step. do.
- the cover member 130 prevents the second flow fluid from being discharged to the front portion of the main body 110, which covers a portion where the second flow channel 124 communicates with the front and rear surfaces of the main body 110. It becomes possible, forming a structure in which) closes.
- the cover member 130 is formed with a through hole 134 to allow the movement of the first flow fluid flowing into the main body 110 along the first direction 102.
- the through hole 134 may be formed by performing a piercing process on a metal plate using a press machine.
- the blocking unit 132 disposed between the through holes 134 prevents the second flow fluid from leaking through the front and rear surfaces of the main body 110.
- a sealing member (not shown) is attached to the inner surface of the cover member 130, it is possible to prevent the leakage of the flow fluid when the cover member 130 and the main body 110 is in close contact.
- first flow channel 122 and the second flow channel 124 may be continuously arranged alternately in the main body 110 as shown in FIG. 6. That is, the second flow channel 124 is disposed on both sides adjacent to the first flow channel 122 so that the first flow fluid flowing in the first flow channel 122 and the second flow flowing in the second flow channel 124 are provided. Thermal exchange between fluids can occur smoothly.
- a heat exchange fin 114 having a predetermined shape is formed between the flow channels 120 to enhance the heat exchange performance between the first and second fluids.
- the heat exchanger 100 may be applied to a hatching device in which thermal exchange or distribution is to be made, but may be particularly used for heat exchange of a food processor system.
- the high temperature and high humidity exhaust gas generated in the drying furnace in which the food is crushed and dried and the cooling air supplied from the outside flow in a direction crossing each other in the flow channel 120 of the heat exchanger 100. Can be.
- the flow process is streamlined due to the presence of the heat exchange fins 114.
- the process proceeds in close contact with the surface of the second flow channel 124, which increases the mobility of heat through heat conduction between the flow channels 120.
- the heat exchange fins 114 are alternately formed at both side walls along the second direction 104 in the respective second flow channels 124.
- the flow channels 120 formed in the main body 110 through the extrusion process are formed to have different lengths formed along the second direction 104. That is, referring to FIG. 8, the second flow channel 124 is formed longer than the first flow channel 122 with respect to the second direction 104, so that upper and lower ends of the second flow channel 124 are formed in the first direction. It is formed closer to the side of the body 110 than the flow channel 122.
- FIG. 9 illustrates a cross section in a state where cutting is performed on the main body 110, and the cutting process proceeds only to the extent that the upper and lower portions of the second flow channel 124 are exposed to the outside. The upper and lower parts are not exposed.
- the second flow fluid flowing through the upper end of the main body 110 passes through the second flow channel 124 and is discharged through the lower end of the main body 110.
- the second flow fluid flows in a zigzag streamline form in the second flow channel 124 (see reference numeral 125).
- an extrusion process of pushing the molten molding material into a molding mold conforming to the shape of the main body 110 of the present invention using a pump is performed.
- the extrusion process is largely classified into a forward extrusion method and a reverse extrusion method.
- the former is the case where the direction of the molding material to be extruded is the same as the direction of applying pressure from the outside, and the latter is the opposite direction.
- a plurality of flow channels 120 are uniformly formed in the body 110 through the single extrusion process.
- 3 illustrates a main body 110 formed through an extrusion process, in which a flow channel 120 having a uniform shape is formed along a first direction 102 (X-axis direction).
- the cover member 130 is attached to the front and rear surfaces of the main body 110.
- the cover member 130 prevents the second flow fluid from being discharged from the main body 110 along the first direction 102.
- the second flow channel 124 communicates with the front and rear surfaces of the main body 110. It becomes possible while forming a structure in which the cover member 130 closes the part.
- the present invention is characterized in that heat exchange is effectively performed through a process in which a flow fluid having thermal energy of different temperatures flows in a direction in which the flow channels formed in the body cross or cross each other.
- high productivity in that the heat exchanger can be manufactured in a simple manner in a short time through a single extrusion process, a cutting process for the upper and lower ends of the main body, and a process of attaching the cover member to the front and rear surfaces of the main body in the process of forming the main body.
- economics are derived.
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- 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)
- Cooling Or The Like Of Semiconductors Or Solid State Devices (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
Description
Claims (12)
- 복수의 유동유체 간에 열적 이동이 이루어지는 열교환기에 있어서,상기 복수의 유동유체가 서로 다른 방향으로 유동하도록 서로 다른 방향으로 관통하는 복수의 유동채널을 포함하는 것을 특징으로 하는 열교환기.
- 제 1 항에 있어서,상기 유동채널은 제 1 유동유체의 통로로서 기능하는 제 1 유동채널 및 제 2 유동유체의 통로로서 기능하는 제 2 유동채널을 포함하고,상기 제 1 유동유체 및 상기 제 2 유동유체는 상기 열교환기의 내부를 교차하는 방향으로 열적 교환이 행해지는 것을 특징으로 하는 열교환기.
- 제 2 항에 있어서,상기 제 1 유동채널과 상기 제 2 유동채널은 상기 본체 내에서 서로 교대로 배치되는 것을 특징으로 하는 열교환기.
- 제 2 항에 있어서,상기 열교환기는 상기 본체의 제 1 방향 상에서의 양측 끝단에 체결되는 한 쌍의 커버부재;를 포함하며,상기 제 1 유동채널은 상기 커버부재를 통해 출입하는 상기 제 1 유동유체의 상기 제 1 방향으로의 통로로서의 기능을 수행하는 것을 특징으로 하는 열교환기.
- 제 4 항에 있어서,상기 본체에 상기 제 1 방향을 따라 형성되는 상기 제 1 및 제 2 유동채널은 압출가공을 통하여 형성되는 것을 특징으로 하는 열교환기.
- 제 2 항에 있어서,상기 제 1 또는 제 2 유동채널에는 소정 형상의 열교환핀이 돌출 형성되는 것을 특징으로 하는 열교환기.
- 제 6 항에 있어서,상기 열교환핀은 상기 제 1 또는 제 2 유동채널 중 상기 열교환핀이 설치된 어느 하나의 유동채널 내에서 마주보는 내측면에 엇갈리게 배치되는 것을 특징으로 하는 열교환기.
- 제 4 항에 있어서,상기 제 2 유동채널은 상기 본체의 측면에 대한 절삭 가공을 통하여 연통 가능하게 되는 것을 특징으로 하는 열교환기.
- 제 4 항에 있어서,상기 커버부재는 상기 본체의 측면으로부터 상기 제 2 유동채널을 통해 유입되는 제 2 유동유체가 상기 제 1 방향을 따라 상기 본체로부터 배출되는 것을 방지하는 것을 특징으로 하는 열교환기.
- 제 1 항 내지 제 9 항 중 어느 한 항에 따른 열교환기를 제조하는 방법에 있어서,상기 복수의 유동채널 중 어느 일 방향의 유동채널이 상이한 높이로 형성되도록 상기 본체를 성형하는 압출 공정 단계;상기 상이한 높이로 형성된 유동채널 중 소정의 유동채널의 말단이 외부로 노출되는 깊이로 상기 일 방향과 상이한 방향의 상기 본체의 측면을 절삭하는 절삭 가공 단계; 및상기 외부로 노출된 말단을 구비한 상기 소정의 유동채널의 상기 일 방향측 측면을 커버하는 커버부재를 부착하는 단계;를 포함하는 것을 특징으로 하는 열교환기의 제조 방법.
- 제 1 항 내지 제 9 항 중 어느 한 항에 따른 열교환기를 포함하는 음식물 처리기에서,상기 열교환기에서는 상기 음식물 처리기의 건조로에서 발생한 배기가스와 외부의 냉각공기가 열교환하는 것을 특징으로 하는 음식물 처리기.
- 제 10 항에 따라 제조된 열교환기를 포함하는 음식물 처리기.
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2010800615858A CN102713491A (zh) | 2010-01-14 | 2010-09-29 | 热交换器、包括其的食物处理机及该热交换器的制造方法 |
JP2012548872A JP5882909B2 (ja) | 2010-01-14 | 2010-09-29 | 熱交換器、熱交換器を含む生ごみ処理機、及び熱交換器の製造方法 |
EP10843269A EP2525182A2 (en) | 2010-01-14 | 2010-09-29 | Heat exchanger, a food handler including the heat exchanger, and a manufacturing method of the heat exchanger |
US13/522,298 US20120285659A1 (en) | 2010-01-14 | 2010-09-29 | Heat exchanger, a food handler including the heat exchanger, and a manufacturing method of the heat exchanger |
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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 |
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WO2011087203A2 true WO2011087203A2 (ko) | 2011-07-21 |
WO2011087203A3 WO2011087203A3 (ko) | 2011-09-09 |
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EP (1) | EP2525182A2 (ko) |
JP (1) | JP5882909B2 (ko) |
KR (1) | KR101183292B1 (ko) |
CN (1) | CN102713491A (ko) |
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Families Citing this family (14)
Publication number | Priority date | Publication date | Assignee | Title |
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US9279626B2 (en) * | 2012-01-23 | 2016-03-08 | Honeywell International Inc. | Plate-fin heat exchanger with a porous blocker bar |
US9615604B2 (en) | 2014-02-06 | 2017-04-11 | David Russick | Food waste dehydrator |
US11851611B2 (en) | 2015-04-28 | 2023-12-26 | Thru Tubing Solutions, Inc. | Flow control in subterranean wells |
US10655427B2 (en) | 2015-04-28 | 2020-05-19 | Thru Tubing Solutions, Inc. | Flow control in subterranean wells |
US9816341B2 (en) | 2015-04-28 | 2017-11-14 | Thru Tubing Solutions, Inc. | Plugging devices and deployment in subterranean wells |
US10233719B2 (en) | 2015-04-28 | 2019-03-19 | Thru Tubing Solutions, Inc. | Flow control in subterranean wells |
US10513653B2 (en) | 2015-04-28 | 2019-12-24 | Thru Tubing Solutions, Inc. | Flow control in subterranean wells |
US10641069B2 (en) | 2015-04-28 | 2020-05-05 | Thru Tubing Solutions, Inc. | Flow control in subterranean wells |
US10753174B2 (en) | 2015-07-21 | 2020-08-25 | Thru Tubing Solutions, Inc. | Plugging device deployment |
US9920589B2 (en) | 2016-04-06 | 2018-03-20 | Thru Tubing Solutions, Inc. | Methods of completing a well and apparatus therefor |
CA3046487C (en) | 2016-12-13 | 2021-04-20 | Thru Tubing Solutions, Inc. | Methods of completing a well and apparatus therefor |
US11293578B2 (en) | 2017-04-25 | 2022-04-05 | Thru Tubing Solutions, Inc. | Plugging undesired openings in fluid conduits |
US11022248B2 (en) | 2017-04-25 | 2021-06-01 | Thru Tubing Solutions, Inc. | Plugging undesired openings in fluid vessels |
US11255610B2 (en) * | 2020-01-22 | 2022-02-22 | Cooler Master Co., Ltd. | Pulse loop heat exchanger and manufacturing method of the same |
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DE2707290C3 (de) * | 1977-02-19 | 1979-09-20 | Kernforschungsanlage Juelich Gmbh, 5170 Juelich | Rekuperativer Wärmeübertrager aus keramischem Material |
JPS60141541A (ja) * | 1983-12-29 | 1985-07-26 | Nippon Soken Inc | ブロツク型熱交換エレメントの製造方法 |
JPH0429252Y2 (ko) * | 1986-01-28 | 1992-07-15 | ||
JP2535842B2 (ja) * | 1986-09-18 | 1996-09-18 | 石川島播磨重工業株式会社 | セラミックス熱交換器 |
JPH08616Y2 (ja) * | 1990-07-05 | 1996-01-10 | 忠男 戸塚 | 熱交換器 |
JPH04340088A (ja) * | 1991-02-04 | 1992-11-26 | Kazumi Seisakusho:Kk | プレートフィン式熱交換器 |
JPH09184693A (ja) * | 1995-12-28 | 1997-07-15 | Ebara Corp | 熱交換エレメント |
JP4473996B2 (ja) | 1999-12-27 | 2010-06-02 | 住友精密工業株式会社 | 高温用プレートフィン型熱交換器 |
JP3805665B2 (ja) | 2001-11-06 | 2006-08-02 | 株式会社豊田中央研究所 | 熱交換器 |
KR20030067877A (ko) * | 2002-02-08 | 2003-08-19 | 벤트-악시아 그룹 리미티드 | 열교환기 |
DE10302948A1 (de) * | 2003-01-24 | 2004-08-05 | Behr Gmbh & Co. Kg | Wärmeübertrager, insbesondere Abgaskühler für Kraftfahrzeuge |
JP2004344850A (ja) * | 2003-05-26 | 2004-12-09 | Seiki Kogyo Kk | 生ゴミ処理装置 |
JP2005241049A (ja) * | 2004-02-24 | 2005-09-08 | Calsonic Kansei Corp | 熱交換器 |
DE102004011354A1 (de) * | 2004-03-05 | 2005-09-22 | Behr Gmbh & Co. Kg | Vorrichtung zum Austausch von Wärme und Verfahren zur Herstellung einer solchen Vorrichtung |
JP2005131631A (ja) * | 2004-06-11 | 2005-05-26 | Koichi Nakamura | 生分解性廃棄物のリサイクル装置 |
JP2006090642A (ja) * | 2004-09-24 | 2006-04-06 | Daikin Ind Ltd | 細径多管式熱交換器の細径伝熱管ユニット |
KR20080004703U (ko) * | 2007-04-13 | 2008-10-16 | 전범수 | 환기덕트용 전열교환기 소자 |
JP2009172546A (ja) * | 2008-01-28 | 2009-08-06 | Hoshino Kankyo Kenkyusho:Kk | 有機廃棄物の処理装置 |
-
2010
- 2010-01-14 KR KR1020100003611A patent/KR101183292B1/ko active IP Right Grant
- 2010-09-29 EP EP10843269A patent/EP2525182A2/en not_active Withdrawn
- 2010-09-29 WO PCT/KR2010/006649 patent/WO2011087203A2/ko active Application Filing
- 2010-09-29 CN CN2010800615858A patent/CN102713491A/zh active Pending
- 2010-09-29 JP JP2012548872A patent/JP5882909B2/ja active Active
- 2010-09-29 US US13/522,298 patent/US20120285659A1/en not_active Abandoned
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Publication number | Publication date |
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US20120285659A1 (en) | 2012-11-15 |
CN102713491A (zh) | 2012-10-03 |
WO2011087203A3 (ko) | 2011-09-09 |
KR20110083400A (ko) | 2011-07-20 |
EP2525182A2 (en) | 2012-11-21 |
JP2013517448A (ja) | 2013-05-16 |
JP5882909B2 (ja) | 2016-03-09 |
KR101183292B1 (ko) | 2012-09-14 |
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