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WO2019073807A1 - Metal base plate material for use in heat exchange plate - Google Patents

Metal base plate material for use in heat exchange plate Download PDF

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Publication number
WO2019073807A1
WO2019073807A1 PCT/JP2018/035935 JP2018035935W WO2019073807A1 WO 2019073807 A1 WO2019073807 A1 WO 2019073807A1 JP 2018035935 W JP2018035935 W JP 2018035935W WO 2019073807 A1 WO2019073807 A1 WO 2019073807A1
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WO
WIPO (PCT)
Prior art keywords
protrusions
region
longitudinal direction
condensate
area
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.)
Ceased
Application number
PCT/JP2018/035935
Other languages
French (fr)
Japanese (ja)
Inventor
圭太郎 田村
義男 逸見
和久 福谷
明夫 岡本
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.)
Kobe Steel Ltd
Original Assignee
Kobe Steel 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 Kobe Steel Ltd filed Critical Kobe Steel Ltd
Priority to EP18866789.3A priority Critical patent/EP3696487A4/en
Priority to RU2020115479A priority patent/RU2747945C1/en
Priority to KR1020207013118A priority patent/KR102407924B1/en
Priority to CN201880061319.1A priority patent/CN111108338B/en
Priority to US16/651,810 priority patent/US20200248975A1/en
Publication of WO2019073807A1 publication Critical patent/WO2019073807A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F3/00Plate-like or laminated elements; Assemblies of plate-like or laminated elements
    • F28F3/02Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations
    • F28F3/04Elements 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
    • F28F3/042Elements 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 local deformations of the element
    • F28F3/046Elements 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 local deformations of the element the deformations being linear, e.g. corrugations
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F3/00Plate-like or laminated elements; Assemblies of plate-like or laminated elements
    • F28F3/02Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations
    • F28F3/04Elements 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
    • 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
    • F28D9/00Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • 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
    • F28D9/00Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D9/0062Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by spaced plates with inserted elements
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F13/00Arrangements for modifying heat-transfer, e.g. increasing, decreasing
    • F28F13/04Arrangements for modifying heat-transfer, e.g. increasing, decreasing by preventing the formation of continuous films of condensate on heat-exchange surfaces, e.g. by promoting droplet formation
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F17/00Removing ice or water from heat-exchange apparatus
    • F28F17/005Means for draining condensates from heat exchangers, e.g. from evaporators
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F21/00Constructions of heat-exchange apparatus characterised by the selection of particular materials
    • F28F21/08Constructions of heat-exchange apparatus characterised by the selection of particular materials of metal
    • F28F21/081Heat exchange elements made from metals or metal alloys
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F3/00Plate-like or laminated elements; Assemblies of plate-like or laminated elements
    • F28F3/02Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations
    • F28F3/04Elements 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
    • F28F3/048Elements 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
    • 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
    • F28D2021/0061Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for phase-change applications
    • F28D2021/0063Condensers

Definitions

  • the present invention relates to a metal base plate used for a heat exchange plate.
  • Plate type heat exchangers which make use of the condensation heat transfer of the working medium.
  • the heat exchange plate contained in the plate type heat exchanger is usually formed into a complex shape such as a herringbone shape for the purpose of improving heat exchange efficiency and mechanical durability.
  • Such a heat exchange plate is generally manufactured by pressing a metal original plate material.
  • Patent Document 1 In order to further improve the heat exchange efficiency of the heat exchange plate, a method has been proposed in which a plurality of fine projections are provided on the surface of a metal original plate material before pressing (Patent Document 1).
  • Patent Document 1 In the base plate material of Patent Document 1, two types of protrusions are formed symmetrically on the surface of a metal flat material before pressing at an angle to form a V shape, and a gap between these two types of protrusions It is said that the stirring action on the vapor of the working medium promotes condensation of the working medium, and the condensate of the working medium can be efficiently discharged.
  • the two types of protrusions provided on the surface of the original plate material of Patent Document 1 have a symmetrical V shape having a gap between the protrusions, so the condensate flowing down the surface of the original plate has two types of protrusions It is concentrated between the ridges by the guidance of the ridges, and decelerates when passing through the gap between the downstream ends of the ridges. For this reason, in order to disperse
  • the present invention has been made based on the above circumstances, and provides a metal base plate used for a heat exchange plate capable of appropriately dispersing the condensate of the working medium and efficiently discharging the condensate.
  • the purpose is
  • the invention made in order to solve the above-mentioned subject is metal former board material used for a heat exchange plate built in a plate type heat exchanger, and at least one surface is a plurality of beltlike 1st fields and a plurality of A plurality of strip-shaped second regions arranged in parallel and alternately, the plurality of strip-like first regions being arranged substantially parallel and at substantially equal intervals such that the crossing angle with the longitudinal direction is 10 degrees or more and 25 degrees or less
  • the strip-like second region has a plurality of ridges and a plurality of second ridges aligned substantially parallel and at substantially equal intervals at an angle facing the plurality of first ridges in the short direction; When the first area and the second area are spaced at substantially equal intervals via the gap area, and one of the first area and the second area in the longitudinal direction is the downstream direction, the plurality of first areas and the second area are separated.
  • the downstream first end of the ridge and the downstream second end of the plurality of second ridges are in the longitudinal direction They
  • the metal original plate material has a gap area between the first area and the second area, and the end portions of the two types of ridges are disposed to be shifted in the longitudinal direction of the first area and the second area. Therefore, the concentration of the condensate between the ends of the two types of ridges can be suppressed, and the condensate can be properly dispersed.
  • the metal base plate material has two types of ridges inclined in opposite directions with respect to the longitudinal direction so that the crossing angle with the longitudinal direction of the first region and the second region is 10 degrees or more and 25 degrees or less. Since it arrange
  • the average distance between the plurality of first protrusions is 0.1 mm or more and 1.0 mm or less
  • the average distance between the plurality of second protrusions is 0.1 mm or more and 1.0 mm or less
  • the first region The average distance between the second regions may be 0.2 mm or more and 4.0 mm or less.
  • the amount of longitudinal displacement between the first end and the second end may be 0.1 mm or more and 5.8 mm or less.
  • the metallic base plate can appropriately disperse the condensate because the amount of longitudinal displacement between the first end and the second end is appropriately adjusted.
  • the angle of intersection of the second ridge with the longitudinal direction of the second region is preferably equal to the angle of intersection of the first ridge. This is because the balance of the flow rate of the condensate in the first area and the second area can be effectively balanced.
  • the metal base plate used for the heat exchange plate of the present invention can properly disperse the condensate of the working medium and can efficiently discharge the condensate.
  • FIG. 2 is a schematic perspective cross-sectional view partially showing an AA cross section in the vicinity of the surface of the metal base plate material of FIG. 1;
  • the metal original plate material 1 of FIG. 1 is a metal original plate material used for a heat exchange plate incorporated in a plate type heat exchanger.
  • the material of the metal base plate 1 is not particularly limited, and titanium, for example, is used.
  • the metal original plate material 1 is a flat plate material which is a raw material for manufacturing a heat exchange plate, and when incorporated in a plate type heat exchanger, is formed into a heat exchange plate by press processing.
  • the metal base plate 1 is not particularly limited, but a rectangular plate having a long side of 1200 mm, a short side of 800 mm, and an average thickness of 0.5 mm to 1.0 mm is used.
  • a plurality of band-like first regions 2 and a plurality of band-like second regions 3 are provided in parallel and alternately on the surface of the metal base plate 1.
  • the surface provided with the first region 2 and the second region 3 may be at least one surface of the metal base plate 1, and even if it is only one side of the metal base plate 1, the surface of the metal base plate 1 It may be both sides.
  • the first area 2 is a band-like area provided on the surface of the metal base plate 1 and a plurality of first areas 2 are provided substantially in parallel. Each of the first regions 2 has a plurality of first ridges 21 aligned substantially in parallel and at substantially equal intervals such that the angle of intersection with the longitudinal direction is ⁇ 1.
  • average width Z1 of the cross direction of the 1st field 2 1 mm is preferred, 2 mm is more preferred, and 3 mm is still more preferred.
  • an upper limit of average width Z1 20 mm is preferred, 18 mm is more preferred, and 16 mm is more preferred. If the average width Z1 is less than the above lower limit, the stirring action on the vapor of the working medium may not be sufficiently obtained, and condensation of the working medium may not be promoted. Conversely, when the average width Z1 exceeds the upper limit, the condensate may stay in the first region 2 and the condensate may not be discharged efficiently.
  • average width shows the value which averaged the width
  • first protrusion 21 In the first region 2, a plurality of first protrusions 21 are provided substantially in parallel and at substantially equal intervals.
  • the first protrusion 21 is an elongated rod-like protrusion in a plan view, and both ends thereof have lengths reaching both side portions of the band-shaped first region 2.
  • the shape of the 1st protrusion 21 is substantially rectangular, two long sides should just be formed substantially parallel in planar view, and the 1st protrusion 21 is for example It may be curvilinear.
  • the method of forming the ridges on the surface of the metal base plate 1 is not particularly limited, but, for example, a method of transferring unevenness during rolling is adopted.
  • intersection angle ⁇ 1 between the first protrusion 21 and the longitudinal direction of the first region 2 is set to an acute angle in order to suppress the deceleration of the flowing down condensate.
  • the lower limit of the intersection angle ⁇ 1 is preferably 10 degrees, more preferably 12 degrees, and even more preferably 13 degrees.
  • the upper limit of the intersection angle ⁇ 1 is preferably 25 degrees, more preferably 22 degrees, and still more preferably 20 degrees. If the crossing angle ⁇ 1 is less than the above lower limit, the condensate may not be properly induced along the side of the first protrusion 21. Conversely, when the crossing angle ⁇ 1 exceeds the upper limit, the condensate may stay in the first region 2 and may not be discharged efficiently.
  • cross angle refers to an acute angle out of two corners formed when two straight lines intersect.
  • the upper limit of the average width a1 is preferably 1.0 mm, more preferably 0.8 mm, and still more preferably 0.6 mm. If the average width a1 is less than the above lower limit, the strength of the first protrusion 21 may be insufficient. In contrast, when the average width a1 exceeds the upper limit, the condensate may flow down the upper surface of the first ridge 21 and the condensate may not be appropriately induced along the side of the first ridge 21.
  • the lower limit of the average distance b1 between the two first protrusions 21 is preferably 0.1 mm, more preferably 0.2 mm, and still more preferably 0.3 mm.
  • the upper limit of the average distance b1 is preferably 1.0 mm, more preferably 0.9 mm, and still more preferably 0.8 mm. If the average distance b1 is less than the above lower limit, the condensate may overflow to the upper surface of the first ridge 21 and the condensate may not be properly induced along the side of the first ridge 21. Conversely, when the average distance b1 exceeds the upper limit, the condensate may stay between the first protrusions 21 and may not be discharged efficiently.
  • "average distance” is the average of the distance in the short side direction of a protrusion, and shows the value which averaged five arbitrary distances between two protrusions.
  • the upper limit of the average height h is preferably 0.10 mm, more preferably 0.09 mm, and still more preferably 0.08 mm. If the average height h is less than the above lower limit, the stirring action on the vapor of the working medium may not be sufficiently obtained, and condensation of the working medium may not be promoted. Conversely, if the average height h exceeds the above upper limit, there is a possibility that the processing cost may increase.
  • the second area 3 is a band-like area provided on the surface of the metal base plate 1, and a plurality of second areas 3 are provided substantially in parallel.
  • Each second region 3 includes a plurality of second protrusions 31 aligned substantially in parallel and at substantially equal intervals at an angle ⁇ 2 opposed to the plurality of first protrusions 21 in the short direction.
  • the lower limit of the average width Z2 in the short direction of the second region 3 is preferably 1 mm, more preferably 2 mm, and still more preferably 3 mm.
  • an upper limit of average width Z2 20 mm is preferred, 18 mm is more preferred, and 16 mm is still more preferred. If the average width Z2 is less than the above lower limit, the action of stirring the vapor of the working medium may not be sufficiently obtained, and condensation of the working medium may not be promoted. Conversely, when the average width Z2 exceeds the upper limit, the condensate may stay in the second region 3 and the condensate may not be discharged efficiently.
  • a plurality of second protrusions 31 are provided substantially in parallel and at substantially equal intervals. Similar to the first protrusion 21, the second protrusion 31 is an elongated rod-like protrusion in plan view, and both ends thereof have lengths reaching both sides of the strip-shaped second region 3.
  • the shape of the 2nd protrusion 31 is substantially the same rectangle as the shape of the 1st protrusion 21, the 2nd protrusion 31 is planar view in the same manner as the 1st protrusion 21. The two long sides may be formed substantially in parallel.
  • the second ridge 31 has the same shape as the first ridge 21 in plan view, and the height of the second ridge 31 with respect to the surface of the metal base plate 1 Is preferably equal to the height h of the first protrusion 21 with respect to the surface of the metal base plate 1 as shown in FIG.
  • the second ridges 31 are disposed at an angle facing the first ridges 21 in the short side direction, when one of the first region 2 and the second region 3 in the longitudinal direction is the downstream direction, The first end 21a on the downstream side of the first protrusion 21 and the second end 31a on the downstream side of the plurality of second protrusions 31 are close to each other with the gap region 4 interposed therebetween.
  • An intersection angle ⁇ 2 between the second ridges 31 and the longitudinal direction of the second region 3 is set to an acute angle in order to suppress the deceleration of the flowing down condensate.
  • the lower limit of the intersection angle ⁇ 2 is preferably 10 degrees, more preferably 12 degrees, and still more preferably 13 degrees.
  • the upper limit of the intersection angle ⁇ 2 is preferably 25 degrees, more preferably 22 degrees, and still more preferably 20 degrees. If the crossing angle ⁇ 2 is less than the above lower limit, the condensate may not be properly induced along the side of the second protrusion 31. Conversely, when the crossing angle ⁇ 2 exceeds the upper limit, the condensate may stay in the second region 3 and may not be discharged efficiently. From the viewpoint of balance of the flow rate of the condensate, it is preferable that the absolute values of the intersection angle ⁇ 1 and the intersection angle ⁇ 2 be equal.
  • the upper limit of the average width a2 is preferably 1.0 mm, more preferably 0.8 mm, and still more preferably 0.6 mm. If the average width a2 is less than the above lower limit, the strength of the second protrusion 31 may be insufficient. Conversely, when the average width a2 exceeds the upper limit, the condensate may flow down the upper surface of the second ridge 31 and the condensate may not be properly induced along the side of the second ridge 31.
  • the average width a1 and the average width a2 are preferably equal from the viewpoint of the balance of the flow rate of the condensate.
  • the lower limit of the average distance b2 between the two second protrusions 31 is preferably 0.1 mm, more preferably 0.2 mm, and still more preferably 0.3 mm.
  • an upper limit of average distance b2 1.0 mm is preferred, 0.9 mm is more preferred, and 0.8 mm is still more preferred. If the average distance b2 is less than the above lower limit, the condensate may overflow on the upper surface of the second ridge 31 and the condensate may not be properly induced along the side of the second ridge 31. Conversely, if the average distance b2 exceeds the upper limit, the condensate may stay between the second protrusions 31 and may not be discharged efficiently.
  • the average distance b1 and the average distance b2 are preferably equal from the viewpoint of the balance of the flow rate of the condensate.
  • downstream first end portions 21 a of the plurality of first protrusions 21 and a plurality of second protrusions are offset from each other in the longitudinal direction.
  • the amount of deviation in the longitudinal direction between the first end 21a and the second end 31a the amount of deviation W1 when the first end 21a is on the downstream side of the second end 31a, and the first end 21a
  • the amount of deviation W2 in the upstream side of the second end 31a is present.
  • the shift amount W1 and the shift amount W2 are preferably equal from the viewpoint of the balance of the flow-down amount of the condensate, but are not particularly limited, and the shift amount W1 and the shift amount W2 may be different.
  • the downstream end of the ridge refers to the downstream end of the upstream long side of the ridge.
  • the lower limit of the longitudinal displacement amount W1 between the first end 21a and the second end 31a is preferably 0.1 mm, more preferably 0.6 mm, and still more preferably 1.0 mm.
  • an upper limit of average distance b2 5.8 mm is preferred, 4.5 mm is more preferred, and 3.5 mm is still more preferred. If the deviation amount W1 is less than the above lower limit, concentration of the condensate between the first end 21a and the second end 31a is not suppressed, and the condensate may not be properly dispersed. Conversely, if the displacement amount W1 exceeds the upper limit, there is a possibility that the condensate may not be properly induced along the first and second protrusions 21 and 31.
  • the lower limit and the upper limit of the deviation amount W2 are the same as W1.
  • the first area 2 and the second area 3 are spaced at substantially equal intervals via the gap area 4.
  • the gap region 4 is a band-like region parallel to the longitudinal direction of the first region 2 and the second region 3, and the first region 2 and the second region 3 are disposed in parallel across the gap region 4. . No unevenness such as a ridge is formed in the clearance area 4 and most of the condensate flows down the clearance area 4 while meandering.
  • the upper limit of the average distance X is preferably 4.0 mm, more preferably 3.5 mm, and still more preferably 3.0 mm. If the average distance X is less than the above lower limit, the condensate may not be discharged efficiently. Conversely, if the average distance X exceeds the upper limit, the condensate may not be properly induced along the first and second protrusions 21 and 31.
  • the metal original plate material 1 has a gap area 4 between the first area 2 and the second area 3, and the ends of the two types of ridges are shifted in the longitudinal direction of the first area 2 and the second area 3. Since it arranges, it is possible to suppress the concentration of the condensate between the ends of the two types of ridges and to disperse the condensate appropriately. Further, since the metal base plate 1 is provided with two types of ridges so that the crossing angle with the longitudinal direction of the first area 2 and the second area 3 is 10 degrees or more and 25 degrees or less, It is possible to discharge the condensate efficiently by suppressing the deceleration of the condensate.
  • the average distance b 1 between the first protrusions 21, the average distance b 2 between the second protrusions 31, and the average distance X between the first region 2 and the second region 3 are properly adjusted. As a result, the condensate can be discharged efficiently.
  • the metal original plate material 1 can appropriately disperse the condensate.
  • the metal original plate material used for the heat exchange plate of the present invention is not limited to the above embodiment.
  • the clearance area 4 has the 1st end 21a and the 2nd end It may be provided between the portions 31 a, and may not be provided between the upstream end of the first protrusion 21 and the upstream end of the second protrusion 31.
  • the heat passing rate is the inflow temperature of cold water to the back surface of the metal base plate, the outflow temperature of cold water from the back surface of the metal base plate, the heat transfer area of the metal base plate, the inflow temperature of the working medium and the cold water
  • the difference was calculated using the difference of the inflow temperature of
  • the surface of the metal base plate to be brought into contact with the working medium was as follows. No. 1 to No.
  • the metal base plate 2 of No. 2 is the metal base plate 1 of the above-described embodiment.
  • the metal base plate of No. 4 is a flat plate material having no ridges on the surface.
  • the third metal base plate has the same shape as the first protrusion and the second protrusion.
  • Metal original plate material of 2 Height h of the ridge: 0.05 mm, width a of the ridge in the lateral direction a: 0.125 mm, distance between the ridges b: 0.6 mm, the ridge and the longitudinal direction of the region where the ridge is provided Crossing angle ⁇ : 15 degrees, distance X between the areas in which the ridges are provided X: 0.49 mm, width Z in the width direction of the area in which the ridges are provided Z: 2.44 mm, longitudinal deviation between the ends of the ridges Amount W: 1.4 mm [No.
  • the heat transfer rate of the metal original plate material of No. 1 is 3592 W / m 2 ⁇ K, no.
  • the heat transfer rate of the metal base plate of No. 2 is 3436 W / m 2 ⁇ K, no.
  • the heat transfer rate of the metal base plate of No. 3 is 2518 W / m 2 ⁇ K, no.
  • the heat transfer rate of the metal original plate material of No. 4 is 2305 W / m 2 ⁇ K. 1 to No. It was confirmed that the metal original board material of 2 showed a high heat transfer rate.
  • No. 1 to No. It can be said that the heat passing rate of the metal original plate material is improved when the ridges are provided in an appropriate arrangement on the surface of the metal original plate material as in the metal original plate material of 2.
  • the metal base plate used for the heat exchange plate of the present invention can properly disperse the condensate of the working medium and can efficiently discharge the condensate.

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
  • Laminated Bodies (AREA)

Abstract

A metal base plate material for use in a heat exchange plate built into a plate-type heat exchanger, wherein the surface of the base plate material is provided with a plurality of strip-shaped first regions and a plurality of strip-shaped second regions, which are provided alternately and in parallel, the strips-shaped first regions have a plurality of first protrusions arranged substantially parallel to each other and at substantially equal intervals such that an angle of intersection with the longitudinal direction is between 10 and 25 degrees, the strip-shaped second regions have a plurality of second protrusions arranged substantially parallel to each other and at substantially equal intervals, at an angle allowing the plurality of second protrusions to face the plurality of first protrusions in the transverse direction, the first regions and the second regions are separated from each other at substantially equal intervals with a gap region therebetween, and when one direction in the longitudinal direction of the first regions and the second regions is defined as the downstream direction a first end on the downstream side of the plurality of first protrusions and a second end on the downstream side of the plurality of second protrusions are offset from each other in the longitudinal direction.

Description

熱交換プレートに用いられる金属製元板材Metal original plate material used for heat exchange plate

 本発明は、熱交換プレートに用いられる金属製元板材に関する。 The present invention relates to a metal base plate used for a heat exchange plate.

 作動媒体の凝縮熱伝達を利用するプレート式熱交換器が知られている。このプレート式熱交換器に内蔵される熱交換プレートは、熱交換効率や機械的耐久性の向上を目的として、通常、ヘリンボーン形状等の複雑な形状に成形される。このような熱交換プレートは、一般的に、金属製元板材をプレス加工することにより製造される。 Plate type heat exchangers are known which make use of the condensation heat transfer of the working medium. The heat exchange plate contained in the plate type heat exchanger is usually formed into a complex shape such as a herringbone shape for the purpose of improving heat exchange efficiency and mechanical durability. Such a heat exchange plate is generally manufactured by pressing a metal original plate material.

 熱交換プレートの熱交換効率をさらに向上させるために、プレス加工前の金属製元板材の表面に微細な複数の突条を設ける手法が提案されている(特許文献1)。特許文献1の元板材は、プレス加工前の金属製の平板材の表面に2種類の突条をV字形状となる角度で対称的に形成し、かつこれらの2種類の突条間に隙間を設けることで、作動媒体の蒸気に対する撹拌作用で作動媒体の凝縮を促進し、かつ作動媒体の凝縮液を効率よく排出できるとしている。 In order to further improve the heat exchange efficiency of the heat exchange plate, a method has been proposed in which a plurality of fine projections are provided on the surface of a metal original plate material before pressing (Patent Document 1). In the base plate material of Patent Document 1, two types of protrusions are formed symmetrically on the surface of a metal flat material before pressing at an angle to form a V shape, and a gap between these two types of protrusions It is said that the stirring action on the vapor of the working medium promotes condensation of the working medium, and the condensate of the working medium can be efficiently discharged.

 特許文献1の元板材の表面に設けられる2種類の突条は、突条間に隙間を有する対称的なV字形状であるため、元板材の表面を流下する凝縮液は、2種類の突条の誘導により突条間に集中し、突条の下流側の端部間の隙間を通過する際に減速する。このため、凝縮液を板材表面に適切に分散させ、凝縮液をさらに効率よく排出させるためには新たな工夫が必要である。 The two types of protrusions provided on the surface of the original plate material of Patent Document 1 have a symmetrical V shape having a gap between the protrusions, so the condensate flowing down the surface of the original plate has two types of protrusions It is concentrated between the ridges by the guidance of the ridges, and decelerates when passing through the gap between the downstream ends of the ridges. For this reason, in order to disperse | distribute a condensate appropriately on the plate | board material surface, and to discharge | emit a condensate more efficiently, a new idea is required.

特開2015-161449号公報JP, 2015-161449, A

 本発明は、上述のような事情に基づいてなされたものであり、作動媒体の凝縮液を適切に分散し、かつ凝縮液を効率よく排出できる熱交換プレートに用いられる金属製元板材を提供することを目的とする。 The present invention has been made based on the above circumstances, and provides a metal base plate used for a heat exchange plate capable of appropriately dispersing the condensate of the working medium and efficiently discharging the condensate. The purpose is

 上記課題を解決するためになされた発明は、プレート式熱交換器に内蔵される熱交換プレートに用いられる金属製元板材であって、少なくとも一方の表面が、複数の帯状の第1領域と複数の帯状の第2領域とを並列かつ交互に備え、帯状の上記第1領域が、長手方向との交角が10度以上25度以下となるように略平行かつ略等間隔に並ぶ複数の第1突条を有し、帯状の上記第2領域が、短手方向に上記複数の第1突条と対向する角度で略平行かつ略等間隔に並ぶ複数の第2突条を有し、上記第1領域と上記第2領域とが、隙間領域を介して略等間隔に離隔されており、上記第1領域及び上記第2領域の長手方向の一方を下流方向とした場合、上記複数の第1突条の下流側の第1端部と上記複数の第2突条の下流側の第2端部とが長手方向に互いにずれている。 The invention made in order to solve the above-mentioned subject is metal former board material used for a heat exchange plate built in a plate type heat exchanger, and at least one surface is a plurality of beltlike 1st fields and a plurality of A plurality of strip-shaped second regions arranged in parallel and alternately, the plurality of strip-like first regions being arranged substantially parallel and at substantially equal intervals such that the crossing angle with the longitudinal direction is 10 degrees or more and 25 degrees or less The strip-like second region has a plurality of ridges and a plurality of second ridges aligned substantially parallel and at substantially equal intervals at an angle facing the plurality of first ridges in the short direction; When the first area and the second area are spaced at substantially equal intervals via the gap area, and one of the first area and the second area in the longitudinal direction is the downstream direction, the plurality of first areas and the second area are separated. The downstream first end of the ridge and the downstream second end of the plurality of second ridges are in the longitudinal direction They are offset from each other.

 当該金属製元板材は、第1領域と第2領域との間に隙間領域を備え、2種類の突条の端部を第1領域及び第2領域の長手方向にずらして配設しているので、2種類の突条の端部間への凝縮液の集中を抑制し、凝縮液を適切に分散できる。また、当該金属製元板材は、第1領域及び第2領域の長手方向との交角が10度以上25度以下となるように、上記長手方向に関して互いに反対方向に傾斜する2種類の突条を配設しているので、流下する凝縮液の減速を抑制することにより凝縮液を効率よく排出できる。 The metal original plate material has a gap area between the first area and the second area, and the end portions of the two types of ridges are disposed to be shifted in the longitudinal direction of the first area and the second area. Therefore, the concentration of the condensate between the ends of the two types of ridges can be suppressed, and the condensate can be properly dispersed. In addition, the metal base plate material has two types of ridges inclined in opposite directions with respect to the longitudinal direction so that the crossing angle with the longitudinal direction of the first region and the second region is 10 degrees or more and 25 degrees or less. Since it arrange | positions, a condensate can be discharged | emitted efficiently by suppressing the deceleration of the condensate which flows down.

 上記複数の第1突条間の平均距離が0.1mm以上1.0mm以下であり、上記複数の第2突条間の平均距離が0.1mm以上1.0mm以下であり、上記第1領域及び上記第2領域間の平均距離が0.2mm以上4.0mm以下であるとよい。これにより、当該金属製元板材は、第1突条間の平均距離、第2突条間の平均距離並びに第1領域及び第2領域間の平均距離が適切に調整されるので、凝縮液を効率よく排出できる。 The average distance between the plurality of first protrusions is 0.1 mm or more and 1.0 mm or less, the average distance between the plurality of second protrusions is 0.1 mm or more and 1.0 mm or less, and the first region The average distance between the second regions may be 0.2 mm or more and 4.0 mm or less. As a result, since the average distance between the first protrusions, the average distance between the second protrusions, and the average distance between the first region and the second region are appropriately adjusted, the metal base plate material concerned can It can be discharged efficiently.

 上記第1端部及び上記第2端部間の長手方向のずれ量が、0.1mm以上5.8mm以下であるとよい。これにより、当該金属製元板材は、第1端部及び第2端部間の長手方向のずれ量が適切に調整されるので、凝縮液を適切に分散できる。 The amount of longitudinal displacement between the first end and the second end may be 0.1 mm or more and 5.8 mm or less. As a result, the metallic base plate can appropriately disperse the condensate because the amount of longitudinal displacement between the first end and the second end is appropriately adjusted.

 上記第2突条の、上記第2領域の長手方向との交角が、上記第1突条の交角とその絶対値が等しいのが好ましい。第1領域及び第2領域における凝縮液の流下量のバランスが効果的にとられるからである。 The angle of intersection of the second ridge with the longitudinal direction of the second region is preferably equal to the angle of intersection of the first ridge. This is because the balance of the flow rate of the condensate in the first area and the second area can be effectively balanced.

 本発明の熱交換プレートに用いられる金属製元板材は、作動媒体の凝縮液を適切に分散し、かつ凝縮液を効率よく排出できる。 The metal base plate used for the heat exchange plate of the present invention can properly disperse the condensate of the working medium and can efficiently discharge the condensate.

本発明の一実施形態の金属製元板材の表面を部分的に示す模式的平面図である。It is a schematic plan view which shows partially the surface of the metal base material board | plate of one Embodiment of this invention. 図1の金属製元板材の表面付近のA-A断面を部分的に示す模式的斜視断面図である。FIG. 2 is a schematic perspective cross-sectional view partially showing an AA cross section in the vicinity of the surface of the metal base plate material of FIG. 1;

 以下、本発明に係る熱交換プレートに用いられる金属製元板材の実施形態について図を参照しつつ詳説する。 Hereinafter, an embodiment of a metal original plate material used for a heat exchange plate according to the present invention will be described in detail with reference to the drawings.

[金属製元板材]
 図1の金属製元板材1は、プレート式熱交換器に内蔵される熱交換プレートに用いられる金属製元板材である。金属製元板材1の材質としては、特に限定されないが、例えばチタンが用いられる。金属製元板材1は、熱交換プレートを製造するための素材となる平板材であり、プレート式熱交換器に内蔵される際には、プレス加工により熱交換プレートに成形される。金属製元板材1としては、特に限定されないが、長辺が1200mm、短辺が800mm、平均厚みが0.5mm以上1.0mm以下の矩形板が用いられる。
[Metal original plate material]
The metal original plate material 1 of FIG. 1 is a metal original plate material used for a heat exchange plate incorporated in a plate type heat exchanger. The material of the metal base plate 1 is not particularly limited, and titanium, for example, is used. The metal original plate material 1 is a flat plate material which is a raw material for manufacturing a heat exchange plate, and when incorporated in a plate type heat exchanger, is formed into a heat exchange plate by press processing. The metal base plate 1 is not particularly limited, but a rectangular plate having a long side of 1200 mm, a short side of 800 mm, and an average thickness of 0.5 mm to 1.0 mm is used.

 金属製元板材1の表面には、複数の帯状の第1領域2と複数の帯状の第2領域3とが並列かつ交互に設けられている。なお、第1領域2及び第2領域3を備える表面は、金属製元板材1の少なくとも一方の表面であればよく、金属製元板材1の片面のみであっても、金属製元板材1の両面であってもよい。 A plurality of band-like first regions 2 and a plurality of band-like second regions 3 are provided in parallel and alternately on the surface of the metal base plate 1. The surface provided with the first region 2 and the second region 3 may be at least one surface of the metal base plate 1, and even if it is only one side of the metal base plate 1, the surface of the metal base plate 1 It may be both sides.

<第1領域>
 第1領域2は、金属製元板材1の表面に設けられる帯状の領域であり、複数の第1領域2が略平行に設けられている。各第1領域2は、長手方向との交角がθ1となるように略平行かつ略等間隔に並ぶ複数の第1突条21を有している。
<First area>
The first area 2 is a band-like area provided on the surface of the metal base plate 1 and a plurality of first areas 2 are provided substantially in parallel. Each of the first regions 2 has a plurality of first ridges 21 aligned substantially in parallel and at substantially equal intervals such that the angle of intersection with the longitudinal direction is θ1.

 第1領域2の短手方向の平均幅Z1の下限としては、1mmが好ましく、2mmがより好ましく、3mmがさらに好ましい。一方、平均幅Z1の上限としては、20mmが好ましく、18mmがより好ましく、16mmがさらに好ましい。平均幅Z1が上記下限に満たないと、作動媒体の蒸気に対する撹拌作用が十分に得られず、作動媒体の凝縮が促進されないおそれがある。逆に、平均幅Z1が上記上限を超えると、凝縮液が第1領域2に滞留し、凝縮液が効率よく排出されないおそれがある。なお、「平均幅」とは、1つの対象における任意の5点の幅を平均した値を示す。 As a minimum of average width Z1 of the cross direction of the 1st field 2, 1 mm is preferred, 2 mm is more preferred, and 3 mm is still more preferred. On the other hand, as an upper limit of average width Z1, 20 mm is preferred, 18 mm is more preferred, and 16 mm is more preferred. If the average width Z1 is less than the above lower limit, the stirring action on the vapor of the working medium may not be sufficiently obtained, and condensation of the working medium may not be promoted. Conversely, when the average width Z1 exceeds the upper limit, the condensate may stay in the first region 2 and the condensate may not be discharged efficiently. In addition, "average width" shows the value which averaged the width | variety of arbitrary five points in one object.

(第1突条)
 第1領域2には、複数の第1突条21が略平行かつ略等間隔に設けられている。第1突条21は、平面視で細長い棒状の突条であり、その両端が帯状の第1領域2の両側部に届く長さを有している。なお、図1では、第1突条21の形状が略矩形となっているが、第1突条21は、平面視で2つの長辺が略平行に形成されていればよく、両端は例えば曲線形状であってもよい。また、金属製元板材1の表面に突条を形成する方法としては、特に限定されないが、例えば圧延時に凹凸を転写する方法等が採用される。
(1st protrusion)
In the first region 2, a plurality of first protrusions 21 are provided substantially in parallel and at substantially equal intervals. The first protrusion 21 is an elongated rod-like protrusion in a plan view, and both ends thereof have lengths reaching both side portions of the band-shaped first region 2. In addition, in FIG. 1, although the shape of the 1st protrusion 21 is substantially rectangular, two long sides should just be formed substantially parallel in planar view, and the 1st protrusion 21 is for example It may be curvilinear. The method of forming the ridges on the surface of the metal base plate 1 is not particularly limited, but, for example, a method of transferring unevenness during rolling is adopted.

 第1突条21と第1領域2の長手方向との交角θ1は、流下する凝縮液の減速を抑制するために鋭角に設定されている。交角θ1の下限としては、10度が好ましく、12度がより好ましく、13度がさらに好ましい。一方、交角θ1の上限としては、25度が好ましく、22度がより好ましく、20度がさらに好ましい。交角θ1が上記下限に満たないと、第1突条21の側辺に沿って凝縮液が適切に誘導されないおそれがある。逆に、交角θ1が上記上限を超えると、凝縮液が第1領域2に滞留し、効率よく排出されないおそれがある。なお、「交角」とは、2直線が交差する際に形成する2つの角の内、鋭角のものを示す。 An intersection angle θ1 between the first protrusion 21 and the longitudinal direction of the first region 2 is set to an acute angle in order to suppress the deceleration of the flowing down condensate. The lower limit of the intersection angle θ1 is preferably 10 degrees, more preferably 12 degrees, and even more preferably 13 degrees. On the other hand, the upper limit of the intersection angle θ1 is preferably 25 degrees, more preferably 22 degrees, and still more preferably 20 degrees. If the crossing angle θ1 is less than the above lower limit, the condensate may not be properly induced along the side of the first protrusion 21. Conversely, when the crossing angle θ1 exceeds the upper limit, the condensate may stay in the first region 2 and may not be discharged efficiently. The term "cross angle" refers to an acute angle out of two corners formed when two straight lines intersect.

 第1突条21の短手方向の平均幅a1の下限としては、0.10mmが好ましく、0.11mmがより好ましく、0.12mmがさらに好ましい。一方平均幅a1の上限としては、1.0mmが好ましく、0.8mmがより好ましく、0.6mmがさらに好ましい。平均幅a1が上記下限に満たないと、第1突条21の強度が不十分となるおそれがある。逆に、平均幅a1が上記上限を超えると、凝縮液が第1突条21の上面を流下し、第1突条21の側辺に沿って凝縮液が適切に誘導されないおそれがある。 As a minimum of average width a1 of a transverse direction of the 1st projected rim 21, 0.10 mm is preferred, 0.11 mm is more preferred, and 0.12 mm is still more preferred. On the other hand, the upper limit of the average width a1 is preferably 1.0 mm, more preferably 0.8 mm, and still more preferably 0.6 mm. If the average width a1 is less than the above lower limit, the strength of the first protrusion 21 may be insufficient. In contrast, when the average width a1 exceeds the upper limit, the condensate may flow down the upper surface of the first ridge 21 and the condensate may not be appropriately induced along the side of the first ridge 21.

 2つの第1突条21間の平均距離b1の下限としては、0.1mmが好ましく、0.2mmがより好ましく、0.3mmがさらに好ましい。一方、平均距離b1の上限としては、1.0mmが好ましく、0.9mmがより好ましく、0.8mmがさらに好ましい。平均距離b1が上記下限に満たないと、凝縮液が第1突条21の上面へ溢れてしまい、第1突条21の側辺に沿って凝縮液が適切に誘導されないおそれがある。逆に、平均距離b1が上記上限を超えると、凝縮液が第1突条21間に滞留し、効率よく排出されないおそれがある。なお、「平均距離」とは、突条の短手方向における距離の平均であり、2つの突条間の任意の5つの距離を平均した値を示す。 The lower limit of the average distance b1 between the two first protrusions 21 is preferably 0.1 mm, more preferably 0.2 mm, and still more preferably 0.3 mm. On the other hand, the upper limit of the average distance b1 is preferably 1.0 mm, more preferably 0.9 mm, and still more preferably 0.8 mm. If the average distance b1 is less than the above lower limit, the condensate may overflow to the upper surface of the first ridge 21 and the condensate may not be properly induced along the side of the first ridge 21. Conversely, when the average distance b1 exceeds the upper limit, the condensate may stay between the first protrusions 21 and may not be discharged efficiently. In addition, "average distance" is the average of the distance in the short side direction of a protrusion, and shows the value which averaged five arbitrary distances between two protrusions.

 金属製元板材1の表面に対する第1突条21の平均高さhの下限としては、0.02mmが好ましく、0.03mmがより好ましく、0.04mmがさらに好ましい。一方、平均高さhの上限としては、0.10mmが好ましく、0.09mmがより好ましく、0.08mmがさらに好ましい。平均高さhが上記下限に満たないと、作動媒体の蒸気に対する撹拌作用が十分に得られず、作動媒体の凝縮が促進されないおそれがある。逆に、平均高さhが上記上限を超えると、加工コストが増大するおそれがある。 As a minimum of average height h of the 1st projected rim 21 to the surface of metal former board material 1, 0.02 mm is preferred, 0.03 mm is more preferred, and 0.04 mm is still more preferred. On the other hand, the upper limit of the average height h is preferably 0.10 mm, more preferably 0.09 mm, and still more preferably 0.08 mm. If the average height h is less than the above lower limit, the stirring action on the vapor of the working medium may not be sufficiently obtained, and condensation of the working medium may not be promoted. Conversely, if the average height h exceeds the above upper limit, there is a possibility that the processing cost may increase.

<第2領域>
 第2領域3は、第1領域2と同様に、金属製元板材1の表面に設けられる帯状の領域であり、複数の第2領域3が略平行に設けられている。各第2領域3は、短手方向に複数の第1突条21と対向する角度θ2で略平行かつ略等間隔に並ぶ複数の第2突条31を有している。
<Second area>
Similar to the first area 2, the second area 3 is a band-like area provided on the surface of the metal base plate 1, and a plurality of second areas 3 are provided substantially in parallel. Each second region 3 includes a plurality of second protrusions 31 aligned substantially in parallel and at substantially equal intervals at an angle θ2 opposed to the plurality of first protrusions 21 in the short direction.

 第2領域3の短手方向の平均幅Z2の下限としては、1mmが好ましく、2mmがより好ましく、3mmがさらに好ましい。一方、平均幅Z2の上限としては、20mmが好ましく、18mmがより好ましく、16mmがさらに好ましい。平均幅Z2が上記下限に満たないと、作動媒体の蒸気に対する撹拌作用が十分に得られず、作動媒体の凝縮が促進されないおそれがある。逆に、平均幅Z2が上記上限を超えると、凝縮液が第2領域3に滞留し、凝縮液が効率よく排出されないおそれがある。 The lower limit of the average width Z2 in the short direction of the second region 3 is preferably 1 mm, more preferably 2 mm, and still more preferably 3 mm. On the other hand, as an upper limit of average width Z2, 20 mm is preferred, 18 mm is more preferred, and 16 mm is still more preferred. If the average width Z2 is less than the above lower limit, the action of stirring the vapor of the working medium may not be sufficiently obtained, and condensation of the working medium may not be promoted. Conversely, when the average width Z2 exceeds the upper limit, the condensate may stay in the second region 3 and the condensate may not be discharged efficiently.

(第2突条)
 第2領域3には、複数の第2突条31が略平行かつ略等間隔に設けられている。第2突条31は、第1突条21と同様に、平面視で細長い棒状の突条であり、その両端が帯状の第2領域3の両側部に届く長さを有している。なお、図1では、第2突条31の形状が第1突条21の形状と同じ略矩形となっているが、第2突条31は、第1突条21と同様に、平面視で2つの長辺が略平行に形成されていればよい。また、凝縮液の流下量のバランスの観点から、第2突条31は、平面視で第1突条21と同じ形状であり、金属製元板材1の表面に対する第2突条31の高さは、図2に示すように、金属製元板材1の表面に対する第1突条21の高さhと等しいと好ましい。
(Second protrusion)
In the second region 3, a plurality of second protrusions 31 are provided substantially in parallel and at substantially equal intervals. Similar to the first protrusion 21, the second protrusion 31 is an elongated rod-like protrusion in plan view, and both ends thereof have lengths reaching both sides of the strip-shaped second region 3. In addition, in FIG. 1, although the shape of the 2nd protrusion 31 is substantially the same rectangle as the shape of the 1st protrusion 21, the 2nd protrusion 31 is planar view in the same manner as the 1st protrusion 21. The two long sides may be formed substantially in parallel. Further, from the viewpoint of balance of the amount of flow of the condensate, the second ridge 31 has the same shape as the first ridge 21 in plan view, and the height of the second ridge 31 with respect to the surface of the metal base plate 1 Is preferably equal to the height h of the first protrusion 21 with respect to the surface of the metal base plate 1 as shown in FIG.

 第2突条31は、短手方向に第1突条21と対向する角度で配設されているため、第1領域2及び第2領域3の長手方向の一方を下流方向とした場合、複数の第1突条21の下流側の第1端部21aと複数の第2突条31の下流側の第2端部31aとが隙間領域4を挟んで互いに近接している。 Since the second ridges 31 are disposed at an angle facing the first ridges 21 in the short side direction, when one of the first region 2 and the second region 3 in the longitudinal direction is the downstream direction, The first end 21a on the downstream side of the first protrusion 21 and the second end 31a on the downstream side of the plurality of second protrusions 31 are close to each other with the gap region 4 interposed therebetween.

 第2突条31と第2領域3の長手方向との交角θ2は、流下する凝縮液の減速を抑制するために鋭角に設定されている。交角θ2の下限としては、10度が好ましく、12度がより好ましく、13度がさらに好ましい。一方、交角θ2の上限としては、25度が好ましく、22度がより好ましく、20度がさらに好ましい。交角θ2が上記下限に満たないと、第2突条31の側辺に沿って凝縮液が適切に誘導されないおそれがある。逆に、交角θ2が上記上限を超えると、凝縮液が第2領域3に滞留し、効率よく排出されないおそれがある。なお、凝縮液の流下量のバランスの観点から、交角θ1及び交角θ2の絶対値は等しいと好ましい。 An intersection angle θ2 between the second ridges 31 and the longitudinal direction of the second region 3 is set to an acute angle in order to suppress the deceleration of the flowing down condensate. The lower limit of the intersection angle θ2 is preferably 10 degrees, more preferably 12 degrees, and still more preferably 13 degrees. On the other hand, the upper limit of the intersection angle θ2 is preferably 25 degrees, more preferably 22 degrees, and still more preferably 20 degrees. If the crossing angle θ2 is less than the above lower limit, the condensate may not be properly induced along the side of the second protrusion 31. Conversely, when the crossing angle θ2 exceeds the upper limit, the condensate may stay in the second region 3 and may not be discharged efficiently. From the viewpoint of balance of the flow rate of the condensate, it is preferable that the absolute values of the intersection angle θ1 and the intersection angle θ2 be equal.

 第2突条31の短手方向の平均幅a2の下限としては、0.10mmが好ましく、0.11mmがより好ましく、0.12mmがさらに好ましい。一方平均幅a2の上限としては、1.0mmが好ましく、0.8mmがより好ましく、0.6mmがさらに好ましい。平均幅a2が上記下限に満たないと、第2突条31の強度が不十分となるおそれがある。逆に、平均幅a2が上記上限を超えると、凝縮液が第2突条31の上面を流下し、第2突条31の側辺に沿って凝縮液が適切に誘導されないおそれがある。なお、凝縮液の流下量のバランスの観点から、平均幅a1及び平均幅a2は等しいと好ましい。 As a minimum of average width a2 of a transverse direction of the 2nd projected rim 31, 0.10 mm is preferred, 0.11 mm is more preferred, and 0.12 mm is still more preferred. On the other hand, the upper limit of the average width a2 is preferably 1.0 mm, more preferably 0.8 mm, and still more preferably 0.6 mm. If the average width a2 is less than the above lower limit, the strength of the second protrusion 31 may be insufficient. Conversely, when the average width a2 exceeds the upper limit, the condensate may flow down the upper surface of the second ridge 31 and the condensate may not be properly induced along the side of the second ridge 31. The average width a1 and the average width a2 are preferably equal from the viewpoint of the balance of the flow rate of the condensate.

 2つの第2突条31間の平均距離b2の下限としては、0.1mmが好ましく、0.2mmがより好ましく、0.3mmがさらに好ましい。一方、平均距離b2の上限としては、1.0mmが好ましく、0.9mmがより好ましく、0.8mmがさらに好ましい。平均距離b2が上記下限に満たないと、凝縮液が第2突条31の上面へ溢れてしまい、第2突条31の側辺に沿って凝縮液が適切に誘導されないおそれがある。逆に、平均距離b2が上記上限を超えると、凝縮液が第2突条31間に滞留し、効率よく排出されないおそれがある。なお、凝縮液の流下量のバランスの観点から、平均距離b1及び平均距離b2は等しいと好ましい。 The lower limit of the average distance b2 between the two second protrusions 31 is preferably 0.1 mm, more preferably 0.2 mm, and still more preferably 0.3 mm. On the other hand, as an upper limit of average distance b2, 1.0 mm is preferred, 0.9 mm is more preferred, and 0.8 mm is still more preferred. If the average distance b2 is less than the above lower limit, the condensate may overflow on the upper surface of the second ridge 31 and the condensate may not be properly induced along the side of the second ridge 31. Conversely, if the average distance b2 exceeds the upper limit, the condensate may stay between the second protrusions 31 and may not be discharged efficiently. The average distance b1 and the average distance b2 are preferably equal from the viewpoint of the balance of the flow rate of the condensate.

 第1領域2及び第2領域3の長手方向の一方を下流方向とした場合、図1に示すように、複数の第1突条21の下流側の第1端部21aと複数の第2突条31の下流側の第2端部31aとは、長手方向に互いにずれている。第1端部21a及び第2端部31a間の長手方向のずれ量としては、第1端部21aが第2端部31aより下流側である場合のずれ量W1と、第1端部21aが第2端部31aより上流側である場合のずれ量W2とが存在する。凝縮液の流下量のバランスの観点から、ずれ量W1及びずれ量W2は等しいと好ましいが、特に限定されず、ずれ量W1及びずれ量W2は異なっていてもよい。なお、突条の下流側の端部とは、突条の上流側の長辺における下流側の終端部を示す。 When one of the first region 2 and the second region 3 in the longitudinal direction is taken as the downstream direction, as shown in FIG. 1, downstream first end portions 21 a of the plurality of first protrusions 21 and a plurality of second protrusions The downstream second ends 31 a of the strips 31 are offset from each other in the longitudinal direction. As the amount of deviation in the longitudinal direction between the first end 21a and the second end 31a, the amount of deviation W1 when the first end 21a is on the downstream side of the second end 31a, and the first end 21a The amount of deviation W2 in the upstream side of the second end 31a is present. The shift amount W1 and the shift amount W2 are preferably equal from the viewpoint of the balance of the flow-down amount of the condensate, but are not particularly limited, and the shift amount W1 and the shift amount W2 may be different. The downstream end of the ridge refers to the downstream end of the upstream long side of the ridge.

 第1端部21a及び第2端部31a間の長手方向のずれ量W1の下限としては、0.1mmが好ましく、0.6mmがより好ましく、1.0mmがさらに好ましい。一方、平均距離b2の上限としては、5.8mmが好ましく、4.5mmがより好ましく、3.5mmがさらに好ましい。ずれ量W1が上記下限に満たないと、第1端部21a及び第2端部31a間への凝縮液の集中が抑制されず、凝縮液が適切に分散されないおそれがある。逆に、ずれ量W1が上記上限を超えると、第1突条21及び第2突条31に沿って凝縮液が適切に誘導されないおそれがある。なお、ずれ量W2の下限及び上限についてもW1と同様である。 The lower limit of the longitudinal displacement amount W1 between the first end 21a and the second end 31a is preferably 0.1 mm, more preferably 0.6 mm, and still more preferably 1.0 mm. On the other hand, as an upper limit of average distance b2, 5.8 mm is preferred, 4.5 mm is more preferred, and 3.5 mm is still more preferred. If the deviation amount W1 is less than the above lower limit, concentration of the condensate between the first end 21a and the second end 31a is not suppressed, and the condensate may not be properly dispersed. Conversely, if the displacement amount W1 exceeds the upper limit, there is a possibility that the condensate may not be properly induced along the first and second protrusions 21 and 31. The lower limit and the upper limit of the deviation amount W2 are the same as W1.

<隙間領域>
 第1領域2と第2領域3とは、隙間領域4を介して略等間隔に離隔されている。隙間領域4は、第1領域2及び第2領域3の長手方向と平行な帯状の領域であり、第1領域2及び第2領域3はこの隙間領域4を挟んで平行に配設されている。隙間領域4には、突条等の凹凸が形成されておらず、凝縮液の大部分は蛇行しながらこの隙間領域4を流下する。
<Near gap area>
The first area 2 and the second area 3 are spaced at substantially equal intervals via the gap area 4. The gap region 4 is a band-like region parallel to the longitudinal direction of the first region 2 and the second region 3, and the first region 2 and the second region 3 are disposed in parallel across the gap region 4. . No unevenness such as a ridge is formed in the clearance area 4 and most of the condensate flows down the clearance area 4 while meandering.

 第1領域2及び第2領域3間の平均距離Xの下限としては、0.2mmが好ましく、0.3mmがより好ましく、0.4mmがさらに好ましい。一方、平均距離Xの上限としては、4.0mmが好ましく、3.5mmがより好ましく、3.0mmがさらに好ましい。平均距離Xが上記下限に満たないと、凝縮液が効率よく排出されないおそれがある。逆に、平均距離Xが上記上限を超えると、第1突条21及び第2突条31に沿って凝縮液が適切に誘導されないおそれがある。 As a minimum of average distance X between the 1st field 2 and the 2nd field 3, 0.2 mm is preferred, 0.3 mm is more preferred, and 0.4 mm is still more preferred. On the other hand, the upper limit of the average distance X is preferably 4.0 mm, more preferably 3.5 mm, and still more preferably 3.0 mm. If the average distance X is less than the above lower limit, the condensate may not be discharged efficiently. Conversely, if the average distance X exceeds the upper limit, the condensate may not be properly induced along the first and second protrusions 21 and 31.

(利点)
 当該金属製元板材1は、第1領域2と第2領域3との間に隙間領域4を備え、2種類の突条の端部を第1領域2及び第2領域3の長手方向にずらして配設しているので、2種類の突条の端部間への凝縮液の集中を抑制し、凝縮液を適切に分散できる。また、当該金属製元板材1は、第1領域2及び第2領域3の長手方向との交角が10度以上25度以下となるように2種類の突条を配設しているので、流下する凝縮液の減速を抑制することにより凝縮液を効率よく排出できる。
(advantage)
The metal original plate material 1 has a gap area 4 between the first area 2 and the second area 3, and the ends of the two types of ridges are shifted in the longitudinal direction of the first area 2 and the second area 3. Since it arranges, it is possible to suppress the concentration of the condensate between the ends of the two types of ridges and to disperse the condensate appropriately. Further, since the metal base plate 1 is provided with two types of ridges so that the crossing angle with the longitudinal direction of the first area 2 and the second area 3 is 10 degrees or more and 25 degrees or less, It is possible to discharge the condensate efficiently by suppressing the deceleration of the condensate.

 また、当該金属製元板材1は、第1突条21間の平均距離b1、第2突条31間の平均距離b2並びに第1領域2及び第2領域3間の平均距離Xが適切に調整されるので、凝縮液を効率よく排出できる。 Further, in the metal original plate material 1, the average distance b 1 between the first protrusions 21, the average distance b 2 between the second protrusions 31, and the average distance X between the first region 2 and the second region 3 are properly adjusted. As a result, the condensate can be discharged efficiently.

 また、当該金属製元板材1は、第1端部21a及び第2端部31a間の長手方向のずれ量W1、W2が適切に調整されるので、凝縮液を適切に分散できる。 In addition, since the displacement amounts W1 and W2 in the longitudinal direction between the first end 21a and the second end 31a are appropriately adjusted, the metal original plate material 1 can appropriately disperse the condensate.

[その他の実施形態]
 本発明の熱交換プレートに用いられる金属製元板材は、上記実施形態に限定されない。
Other Embodiments
The metal original plate material used for the heat exchange plate of the present invention is not limited to the above embodiment.

 上記実施形態では、金属製元板材1が、第1領域2と第2領域3との間に隙間領域4を備えるものについて説明したが、隙間領域4は、第1端部21a及び第2端部31a間に設けられていればよく、第1突条21の上流側の端部と第2突条31の上流側の端部との間には設けられていなくてもよい。 Although the metal original board material 1 demonstrated the thing provided with the clearance area | region 4 between the 1st area | region 2 and the 2nd area | region 3 in the said embodiment, the clearance area 4 has the 1st end 21a and the 2nd end It may be provided between the portions 31 a, and may not be provided between the upstream end of the first protrusion 21 and the upstream end of the second protrusion 31.

 以下、実施例によって本発明をさらに詳細に説明するが、本発明はこれらの実施例に限定されるものではない。 Hereinafter, the present invention will be described in more detail by way of examples, but the present invention is not limited to these examples.

 凝縮熱伝達の性能試験として、No.1~No.4の金属製元板材を用いた熱通過率の評価を行った。金属製元板材の表面に接触させる作動媒体としてハイドロフルオロカーボン(R134a)を用い、作動媒体を凝縮させるために金属製元板材の裏面に接触させる冷媒として冷水を用いた。作動媒体は、ヒーターを用いて流入温度を30℃とし、圧力0.68MPaで金属製元板材の表面に流入させた。冷水は、流入温度を20℃とし、流量を3L/minとして金属製元板材の裏面に流入させた。また、金属製元板材の伝熱面積を17500mmとし、W深さを2mmとした。熱通過率は、金属製元板材の裏面への冷水の流入温度と、金属製元板材の裏面からの冷水の流出温度と、金属製元板材の伝熱面積と、作動媒体の流入温度及び冷水の流入温度の差とを用いて算出した。 As a performance test of condensation heat transfer, No. 1 to No. The heat transfer rate was evaluated using the metal original plate material of 4. Hydrofluorocarbon (R134a) was used as the working medium to be brought into contact with the surface of the metal base plate, and cold water was used as the refrigerant to be brought into contact with the back of the metal base plate to condense the working medium. The working medium was made to flow into the surface of the metal base plate material at a pressure of 0.68 MPa and a flow rate of 30 ° C. using a heater. Cold water was made to flow into the back surface of the metal base plate at an inflow temperature of 20 ° C. and a flow rate of 3 L / min. Further, the heat transfer area of the metal original plate and 17500Mm 2, and the W depth and 2 mm. The heat passing rate is the inflow temperature of cold water to the back surface of the metal base plate, the outflow temperature of cold water from the back surface of the metal base plate, the heat transfer area of the metal base plate, the inflow temperature of the working medium and the cold water The difference was calculated using the difference of the inflow temperature of

 作動媒体を接触させる金属製元板材の表面は、以下の通りとした。なお、No.1~No.2の金属製元板材は、上述の実施形態の金属製元板材1であり、No.3の金属製元板材は、上述の実施形態の金属製元板材1について、突条と突条が設けられる領域の長手方向との交角θ及び突条の端部間の長手方向のずれ量Wを実施形態の範囲外としたものである。また、No.4の金属製元板材は、表面に突条を有していない平板材である。なお、No.1~No.3の金属製元板材は、第1突条及び第2突条を同一形状としている。 The surface of the metal base plate to be brought into contact with the working medium was as follows. No. 1 to No. The metal base plate 2 of No. 2 is the metal base plate 1 of the above-described embodiment. In the metal base plate 3 of the third embodiment, with respect to the metal base plate 1 of the above-described embodiment, the crossing angle θ between the ridges and the longitudinal direction of the region where the ridges are provided and the longitudinal shift amount W between the ends of the ridges Out of the scope of the embodiment. Also, no. The metal base plate of No. 4 is a flat plate material having no ridges on the surface. No. 1 to No. The third metal base plate has the same shape as the first protrusion and the second protrusion.

[No.1の金属製元板材]
 突条の高さh:0.05mm、突条の短手方向の幅a:0.125mm、突条間の距離b:0.6mm、突条と突条が設けられる領域の長手方向との交角θ:15度、突条が設けられる領域間の距離X:0.98mm、突条が設けられる領域の短手方向の幅Z:4.88mm、突条の端部間の長手方向のずれ量W:1.4mm
[No.2の金属製元板材]
 突条の高さh:0.05mm、突条の短手方向の幅a:0.125mm、突条間の距離b:0.6mm、突条と突条が設けられる領域の長手方向との交角θ:15度、突条が設けられる領域間の距離X:0.49mm、突条が設けられる領域の短手方向の幅Z:2.44mm、突条の端部間の長手方向のずれ量W:1.4mm
[No.3の金属製元板材]
 突条の高さh:0.05mm、突条の短手方向の幅a:0.125mm、突条間の距離b:0.6mm、突条と突条が設けられる領域の長手方向との交角θ:45度、突条が設けられる領域間の距離X:4mm、突条が設けられる領域の短手方向の幅Z:20mm、突条の端部間の長手方向のずれ量W:0mm
[No. 1 metal former board material]
Height h of the ridge: 0.05 mm, width a of the ridge in the lateral direction a: 0.125 mm, distance between the ridges b: 0.6 mm, the ridge and the longitudinal direction of the region where the ridge is provided Crossing angle θ: 15 degrees, distance X between the areas where the ridges are provided X: 0.98 mm, width Z in the width direction of the areas where the ridges are provided Z: 4.88 mm, longitudinal deviation between the ends of the ridges Amount W: 1.4 mm
[No. Metal original plate material of 2]
Height h of the ridge: 0.05 mm, width a of the ridge in the lateral direction a: 0.125 mm, distance between the ridges b: 0.6 mm, the ridge and the longitudinal direction of the region where the ridge is provided Crossing angle θ: 15 degrees, distance X between the areas in which the ridges are provided X: 0.49 mm, width Z in the width direction of the area in which the ridges are provided Z: 2.44 mm, longitudinal deviation between the ends of the ridges Amount W: 1.4 mm
[No. 3 metal former board material]
Height h of the ridge: 0.05 mm, width a of the ridge in the lateral direction a: 0.125 mm, distance between the ridges b: 0.6 mm, the ridge and the longitudinal direction of the region where the ridge is provided Crossing angle θ: 45 degrees, distance X between the areas in which the ridges are provided X: 4 mm, width Z in the width direction of the area in which the ridges are provided Z: 20 mm, longitudinal displacement between the ends of the ridges W: 0 mm

 試験の結果、No.1の金属製元板材の熱通過率は3592W/m・K、No.2の金属製元板材の熱通過率は3436W/m・K、No.3の金属製元板材の熱通過率は2518W/m・K、No.4の金属製元板材の熱通過率は2305W/m・Kとなり、No.1~No.2の金属製元板材は、高い熱通過率を示すことが確認された。これにより、No.1~No.2の金属製元板材のように金属製元板材の表面に適切な配置で突条が設けられると、金属製元板材の熱通過率が向上するといえる。 As a result of the test, No. The heat transfer rate of the metal original plate material of No. 1 is 3592 W / m 2 · K, no. The heat transfer rate of the metal base plate of No. 2 is 3436 W / m 2 · K, no. The heat transfer rate of the metal base plate of No. 3 is 2518 W / m 2 · K, no. The heat transfer rate of the metal original plate material of No. 4 is 2305 W / m 2 · K. 1 to No. It was confirmed that the metal original board material of 2 showed a high heat transfer rate. Thereby, No. 1 to No. It can be said that the heat passing rate of the metal original plate material is improved when the ridges are provided in an appropriate arrangement on the surface of the metal original plate material as in the metal original plate material of 2.

 本発明の熱交換プレートに用いられる金属製元板材は、作動媒体の凝縮液を適切に分散し、かつ凝縮液を効率よく排出できる。 The metal base plate used for the heat exchange plate of the present invention can properly disperse the condensate of the working medium and can efficiently discharge the condensate.

 1 金属製元板材
 2 第1領域
 3 第2領域
 4 隙間領域
 21 第1突条
 21a 第1端部
 31 第2突条
 31a 第2端部
DESCRIPTION OF SYMBOLS 1 metal original board material 2 1st area | region 3 2nd area | region 4 clearance area 21 1st protrusion 21a 1st end part 31 2nd protrusion 31a 2nd end

Claims (4)

 プレート式熱交換器に内蔵される熱交換プレートに用いられる金属製元板材であって、
 少なくとも一方の表面が、
 複数の帯状の第1領域と複数の帯状の第2領域とを並列かつ交互に備え、
 帯状の上記第1領域が、
 長手方向との交角が10度以上25度以下となるように略平行かつ略等間隔に並ぶ複数の第1突条を有し、
 帯状の上記第2領域が、
 短手方向に上記複数の第1突条と対向する角度で略平行かつ略等間隔に並ぶ複数の第2突条を有し、
 上記第1領域と上記第2領域とが、隙間領域を介して略等間隔に離隔されており、
 上記第1領域及び上記第2領域の長手方向の一方を下流方向とした場合、上記複数の第1突条の下流側の第1端部と上記複数の第2突条の下流側の第2端部とが長手方向に互いにずれている金属製元板材。
A metal original plate material used for a heat exchange plate incorporated in a plate type heat exchanger,
At least one surface is
A plurality of strip-shaped first regions and a plurality of strip-shaped second regions arranged in parallel and alternately;
The band-shaped first region is
It has a plurality of first ridges arranged substantially parallel and at substantially equal intervals so that the crossing angle with the longitudinal direction is 10 degrees or more and 25 degrees or less,
The band-shaped second region is
It has a plurality of second protrusions arranged substantially parallel and at substantially equal intervals at an angle facing the plurality of first protrusions in the short direction,
The first area and the second area are spaced at substantially equal intervals via a gap area,
When one of the first region and the second region in the longitudinal direction is taken as the downstream direction, the downstream first ends of the plurality of first protrusions and the second of the plurality of second protrusions downstream of the plurality of second protrusions Metal original plate material which is mutually shifted in the longitudinal direction with the end.
 上記複数の第1突条間の平均距離が0.1mm以上1.0mm以下であり、
 上記複数の第2突条間の平均距離が0.1mm以上1.0mm以下であり、
 上記第1領域及び上記第2領域間の平均距離が0.2mm以上4.0mm以下である請求項1に記載の金属製元板材。
The average distance between the plurality of first protrusions is 0.1 mm or more and 1.0 mm or less,
The average distance between the plurality of second protrusions is 0.1 mm or more and 1.0 mm or less,
The metal original board material according to claim 1 whose average distance between said 1st field and said 2nd field is 0.2 mm or more and 4.0 mm or less.
 上記第1端部及び上記第2端部間の長手方向のずれ量が、0.1mm以上5.8mm以下である請求項1又は請求項2に記載の金属製元板材。 The metal original board material according to claim 1 or 2, wherein the shift amount in the longitudinal direction between the first end and the second end is 0.1 mm or more and 5.8 mm or less.  上記第2突条の、上記第2領域の長手方向との交角が、上記第1突条の交角とその絶対値が等しい請求項1に記載の金属製元板材。 The metal original plate material according to claim 1, wherein an angle of intersection of the second protrusion with the longitudinal direction of the second region is equal to an absolute value of an angle of intersection of the first protrusion.
PCT/JP2018/035935 2017-10-12 2018-09-27 Metal base plate material for use in heat exchange plate Ceased WO2019073807A1 (en)

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EP18866789.3A EP3696487A4 (en) 2017-10-12 2018-09-27 Metal base plate material for use in heat exchange plate
RU2020115479A RU2747945C1 (en) 2017-10-12 2018-09-27 Sheet material of metal base for heat exchange plate
KR1020207013118A KR102407924B1 (en) 2017-10-12 2018-09-27 Metal raw material used for heat exchange plate
CN201880061319.1A CN111108338B (en) 2017-10-12 2018-09-27 Metal base sheet for heat exchange plates
US16/651,810 US20200248975A1 (en) 2017-10-12 2018-09-27 Metal base plate material for heat exchange plate

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JP2017198590A JP6815965B2 (en) 2017-10-12 2017-10-12 Original metal plate used for heat exchange plates

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CN112179179A (en) * 2020-09-02 2021-01-05 东南大学 An energy-saving heat exchange plate for enhanced heat transfer and drag reduction for folded printed circuit board heat exchangers

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JP2019074226A (en) 2019-05-16
CN111108338A (en) 2020-05-05
RU2747945C1 (en) 2021-05-17
EP3696487A4 (en) 2021-06-16
CN111108338B (en) 2021-08-13
JP6815965B2 (en) 2021-01-20
KR20200062313A (en) 2020-06-03
US20200248975A1 (en) 2020-08-06
KR102407924B1 (en) 2022-06-13

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