WO2014077318A1 - Échangeur de chaleur - Google Patents

Échangeur de chaleur Download PDF

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Publication number
WO2014077318A1
WO2014077318A1 PCT/JP2013/080788 JP2013080788W WO2014077318A1 WO 2014077318 A1 WO2014077318 A1 WO 2014077318A1 JP 2013080788 W JP2013080788 W JP 2013080788W WO 2014077318 A1 WO2014077318 A1 WO 2014077318A1
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WO
WIPO (PCT)
Prior art keywords
line
heat exchange
heat exchanger
exchange fluid
heat
Prior art date
Application number
PCT/JP2013/080788
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English (en)
Japanese (ja)
Inventor
直毅 鹿園
洋介 長谷川
Original Assignee
国立大学法人東京大学
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Application filed by 国立大学法人東京大学 filed Critical 国立大学法人東京大学
Priority to JP2014547031A priority Critical patent/JP6206976B2/ja
Publication of WO2014077318A1 publication Critical patent/WO2014077318A1/fr

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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
    • F28D1/00—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators
    • F28D1/02—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid
    • F28D1/04—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits
    • F28D1/053—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits the conduits being straight
    • F28D1/0535—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits the conduits being straight the conduits having a non-circular cross-section
    • F28D1/05366—Assemblies of conduits connected to common headers, e.g. core type radiators
    • F28D1/05391—Assemblies of conduits connected to common headers, e.g. core type radiators with multiple rows of conduits or with multi-channel conduits combined with a particular flow pattern, e.g. multi-row multi-stage radiators
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F1/00—Tubular elements; Assemblies of tubular elements
    • F28F1/10—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
    • F28F1/12—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element
    • F28F1/126—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element consisting of zig-zag shaped fins
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F2215/00—Fins

Definitions

  • the present invention relates to a heat exchanger, and more specifically, a smooth curved surface is used on the surface of a heat transfer member, and a top line in which a cross section is corrugated and a wave top is continuous and a bottom line in which a wave bottom is continuous are V-shaped.
  • the present invention relates to a heat exchanger in which a plurality of corrugations are formed so as to exchange heat by flowing a first heat exchange fluid in a vertical direction in a V shape with respect to the plurality of corrugations.
  • an angle formed by a line connecting the top of the wave and a line connecting the bottom of the wave to the heat exchange tube or fin with respect to the main flow of air is 10 to 60 degrees.
  • a method in which corrugated irregularities are formed that are symmetrically folded by folding lines at predetermined intervals along the main flow of air see, for example, Patent Documents 1 to 3.
  • separation of air flow and local acceleration are suppressed, and an effective secondary flow is generated in the air flow to improve heat transfer efficiency, and overall heat exchange efficiency is improved. .
  • the waves in the corrugated irregularities formed on the heat exchanging tubes and fins are formed so as to have a constant amplitude at a constant wavelength, and with respect to the flow of heat exchanging fluid such as air.
  • the shape has the optimal flow resistance of the heat transfer promotion or heat exchange fluid.
  • the heat exchanger according to the present invention proposes a heat exchanger in which corrugated irregularities are formed in heat exchange members such as heat exchange tubes and fins, in which heat transfer promotion is higher and flow resistance is lower.
  • the main purpose proposes a heat exchanger in which corrugated irregularities are formed in heat exchange members such as heat exchange tubes and fins, in which heat transfer promotion is higher and flow resistance is lower.
  • the heat exchanger of the present invention employs the following means in order to achieve the main object described above.
  • the heat exchanger of the present invention is A plurality of undulations are formed so that the top surface of the heat transfer member has a smooth curved surface and has a V-shaped cross-section with a wave-like top line and a wave-bottom continuous bottom line.
  • a first average angle as an average of an angle formed between a V-shaped inclined portion of the top line and the main flow of the first heat exchange fluid is intermediate between the top and the bottom.
  • the intermediate portion to be positioned is formed to be smaller than a second average angle as an average of an angle formed by the V-shaped inclined portion in the continuous intermediate portion line and the main flow of the first heat exchange fluid. , It is characterized by that.
  • the plurality of corrugated irregularities are formed into a corrugated cross section using a smooth curved surface, and further, a top line in which the top of the wave continues and a bottom line in which the bottom of the wave continues.
  • the first average angle as the average of the angle between the V-shaped inclined portion of the top line and the main flow of the first heat exchange fluid is the top and bottom
  • An intermediate portion that is an intermediate portion is formed so as to be smaller than a second average angle as an average of an angle formed by a V-shaped inclined portion in a continuous intermediate portion line and a main flow of the first heat exchange fluid.
  • the top line where the wave top is continuous and the bottom line where the wave bottom is continuous using a smooth curved surface are V-shaped.
  • the first average angle as the average of the angle formed between the V-shaped hatched portion in the top line and the main flow of the first heat exchange fluid is the V-shaped hatched portion in the intermediate line and the first heat.
  • the “intermediate portion between the top portion and the bottom portion” means a portion that is an intermediate position (average height position) in the height direction with respect to the top portion and the bottom portion.
  • the intermediate part line in which the intermediate part continues is V-shaped because the top line and the bottom line are V-shaped.
  • corrugated irregularities are formed so that the first average angle is smaller than the second average angle
  • the V-shaped bent portion of the top line and the end of the inclined portion When the V-shape is continuous
  • the distance between the adjacent bent portion is longer than the distance between the corresponding bent portion of the V-shaped intermediate line and the end portion of the hatched portion (adjacent bent portion when the V-shape continues).
  • the heat exchanger is a corrugated fin type heat exchanger
  • the heat transfer member is a corrugated fin
  • the corrugated irregularities are formed so that the top and bottom are symmetrical.
  • the corrugated fin shape of the present invention is applied to the corrugated fin of the corrugated fin heat exchanger.
  • “the corrugated irregularities are formed so that the top and bottom are symmetrical” means that the top and bottom of the wave on one side of the fin are the bottom and top of the wave on the other side of the fin. This means that the shape of the top of the wave on one side of the fin is the same as the shape of the top of the wave on the other side of the fin.
  • the heat transfer member is a plurality of flat tubes forming a flow path of a second heat exchange fluid that exchanges heat with the first heat exchange fluid, and the tube
  • the corrugated irregularities are formed on the flat outer surface of the film. That is, the corrugated shape of the present invention is applied to the outer surface of a tube of a heat exchanger having a plurality of tubes.
  • both the “first heat exchange fluid” and the “second heat exchange fluid” mean a heat exchange medium.
  • air or the like is used as the “first heat exchange fluid”.
  • Oil or water may be used as the “second heat exchange fluid”, or conversely, air or the like may be used as the “second heat exchange fluid”, and the “first heat exchange fluid” Oil or water may be used.
  • the plurality of corrugated irregularities have an amplitude in the waveform of the corrugated irregularities located on the upstream side of the first heat exchange fluid on the upstream side of the first heat exchange fluid. It can also be characterized by being formed so as to be larger than the amplitude in the waveform of the waveform corrugation located. That is, in the heat transfer member, the amplitude of the waveform unevenness formed on the inlet side of the first heat exchange fluid is larger than the amplitude of the waveform unevenness formed on the outlet side of the first heat exchange fluid. Corrugated irregularities are formed so as to be.
  • the “amplitude in the waveform” corresponds to the height of the top and the depth of the bottom of the waveform unevenness.
  • the top line and the bottom line of the plurality of corrugated irregularities are formed so that a V-shape is continuously repeated a plurality of times.
  • V-shape is repeated continuously over a plurality of times means that the V-shape is brought into contact with the side so that it becomes a W-shape by repeating the V-shape continuously over two times, for example.
  • the plural corrugated irregularities are formed on the top line.
  • the bent portion is formed so as to be positioned in the vicinity of the end portion of the heat transfer member. That is, the top line and the bottom line of the corrugated irregularities are formed so that the V-shape is continuously repeated a plurality of times, and the bent portion of the top line is positioned near the end of the heat transfer member. It is formed.
  • the end portion (end portion of the heat transfer member) of the corrugated unevenness formed so that the V shape is continuous is the lower portion of the V-shaped hatched portion.
  • the plurality of corrugated irregularities are formed such that the height of the top at the bent portion of the top line is higher than the height of the top at a portion different from the bent portion of the top line. It can also be characterized by that.
  • the secondary flow with respect to the main flow of the first heat exchange fluid is further formed by forming the top height at the bent portion of the top line to be higher than the height of the top portion at a portion different from the bent portion of the top line. It can be effectively generated to improve heat transfer promotion.
  • the height of the top at the bent portion of the top line is formed to be higher than the height of the top at the portion different from the bent portion of the top line”, in other words, “is different from the bent portion of the top line. It is formed so that the height of the top portion at the portion is lower than the height of the top portion at the bent portion of the top line.
  • FIG. 4 is an explanatory view showing a horizontal surface of the corrugated fin 40 together with cross sections of two flat tubes 30.
  • FIG. It is explanatory drawing which shows and demonstrates the waveform unevenness
  • FIG. 3 is a cross-sectional view taken along the line AA of the AA cross section of FIG. 2 as viewed from the direction of the arrow A in FIG.
  • FIG. 11 is a BB cross-sectional view of the BB cross section of FIG. 10 as viewed from the direction of the arrow B in the drawing.
  • FIG. 11 is a cross-sectional view taken along the line CC of FIG. 10 as viewed from the direction of the arrow C in the drawing.
  • It is DD sectional drawing which continued the DD cross section of FIG. 210 from the arrow direction of D in the figure.
  • It is an external view which shows the external appearance of the heat exchanger 120 as 2nd Example of this invention.
  • FIG. 1 is a block diagram showing an outline of the configuration of the corrugated fin heat exchanger 20 according to the first embodiment of the present invention
  • FIG. 2 shows the appearance of the corrugated fin 40 disposed between the flat tubes 30
  • FIG. 3 is an explanatory view showing a horizontal plane 42 of the corrugated fin 40 together with cross sections of the flat tubes 30 on both sides.
  • FIG. 4 is an explanatory view illustrating the corrugated unevenness formed on the corrugated fin 40 of the first embodiment in three dimensions
  • FIG. 5 shows the corrugated unevenness formed on the corrugated fin 40 of the first embodiment.
  • FIG. 6 is an explanatory view showing the comparative example in three dimensions with auxiliary lines, FIG.
  • FIG. 6 is an explanatory view schematically showing the corrugated irregularities of the first embodiment together with auxiliary lines
  • FIG. 7 is a cross-sectional view taken along line AA in FIG.
  • FIG. 3 is a cross-sectional view taken along the line AA as viewed from the direction of the arrow A in the figure.
  • the corrugated fin-type heat exchanger 20 of the first embodiment is a heat exchanger used in a refrigeration cycle such as various air conditioners and refrigeration apparatuses, or heat from exhaust gas from an internal combustion engine or off-gas from a fuel cell. It is used as a heat exchanger used in an energy conversion device such as a heat recovery device that recovers energy. As shown in FIG.
  • a plurality of flat tubes 30 forming a flow path of the second heat exchange fluid), three partition walls 28a, 28b, 28c for diverting the second heat exchange fluid as a whole, Between the flat tube 30 and the three partition walls 28a, 28b, 28c, and between the flat tube 30 and the side walls 29a, 29b.
  • a plurality of corrugated fins 40 that promote heat transfer by heat exchange in the flow path of the heat exchange medium (first heat exchange fluid), and a second heat exchange fluid that is disposed above the heat exchange section composed of these.
  • the flat tube 30 and the partition walls 28a, 28b, 28c, the side walls 29a, 29b, the corrugated fins 40, the upper header 22, and the lower header 26 of the corrugated fin heat exchanger 20 of the first embodiment are the second heat exchange fluid.
  • a metal material that has corrosion resistance and high thermal conductivity with respect to the first heat exchange fluid such as aluminum, copper, stainless steel, and the first heat when air is used as the first heat exchange fluid.
  • exhaust gas from an internal combustion engine or exhaust gas from a fuel cell is used as a replacement fluid, it is made of stainless steel or the like.
  • the corrugated fin type heat exchanger 20 is a heat exchanger used in an air conditioner, and includes a flat tube 30, partition walls 28a, 28b, 28c, side walls 29a, 29b, corrugated fins 40, and an upper header. 22, each member of the lower header 26 is made of aluminum.
  • the size of the flat tube 30 is 5 mm to 10 mm, and the distance between the horizontal surfaces 42 of the corrugated fins 40 (the height of the vertical surface 48) is 1 mm to 2 mm.
  • a specific example is one in which hydrofluorocarbon is used as the second heat exchange fluid and air is used as the first heat exchange fluid.
  • Partition walls 25a and 25b are formed on the inner side of the upper header 22 so that the partition walls 28a and 28c extend at positions that align with the partition walls 28a and 28c, and the lower header 26 is aligned with the partition wall 28b.
  • a partition wall 27 is formed so that the partition wall 28b extends at a position where the partition wall 28b extends. Therefore, the second heat exchange fluid (for example, hydrofluorocarbon) flows into the upper header 22 from the inlet 23 as indicated by the arrows in the figure, and vertically passes through the three flat tubes 30 on the right side of the partition wall 28a.
  • the second heat exchange fluid for example, hydrofluorocarbon
  • the upper header flows vertically downward from above, is supplied to the three flat tubes 30 between the partition walls 28a and 28b by the partition wall 27 in the lower header 26, and flows vertically upward from below the three flat tubes 30.
  • 22 flows into the space between the partition walls 25a and 25b, flows from the vertically upper side to the vertically lower side in the three flat tubes 30 of the partition walls 28b and 28c, reaches the space on the right side of the partition wall 28b, and is on the left side of the partition wall 28c.
  • the inside of the three flat tubes 30 flows vertically downward from vertically above and enters the space on the left side of the partition wall 25b of the upper header 22, After, and is discharged from the outlet 24.
  • the first heat exchange fluid is a plurality of flat tubes from the front surface to the back surface in FIG. 1, from diagonally lower left to diagonally upper right in FIG. 2, and from lower to upper in FIG. Flows through 30.
  • the horizontal planes 42 and the vertical planes 48 are alternately formed in a folded shape (bellows shape), and the vertical planes 48 are joined to the flat tube 30 by brazing or the like.
  • a plurality of corrugated irregularities are formed by a smooth curved surface.
  • the plurality of corrugations of the first embodiment are mainly composed of a top line 43 connecting the wave tops and a bottom line 44 connecting the wave bottoms and the first heat exchange fluid (air).
  • the bent portion 43a of the top line 43 is a corrugated so that the top line 43 and the bottom line 44 are continuously repeated in a V shape a plurality of times so that the angle formed with the straight flow is an acute angle.
  • the first average angle as the average of the angle formed by the V-shaped oblique line portion 43b in the top line 43 and the main flow of the first heat exchange fluid so as to be positioned near the end of the horizontal surface 42 of the fin 40
  • the amplitude of the wave on the inlet side of the first heat exchange fluid (air) is greater than the amplitude of the wave on the outlet side so that the shape of the recess and the shape of the recess on the same surface are integrated. It is formed to be large.
  • the corrugated irregularities formed in the corrugated fin 40 of the embodiment will be described in detail.
  • the top of the wave means the top of the convex part in the repetition of the convex part and the concave part of the wave
  • the bottom of the wave means the bottom of the concave part in the repetition of the convex part and the concave part of the wave.
  • the plurality of corrugated irregularities formed on the horizontal surface 42 of the corrugated fin 40 has a smooth curved surface and a top line 43 connecting the wave tops and a bottom line 44 connecting the wave bottoms to the first line.
  • the angle formed with the main flow of the heat exchange fluid (air) is an acute angle.
  • the angle between the top line 43 and the bottom line 44 and the main flow of the first heat exchange fluid (air) is preferably 10 degrees to 60 degrees, more preferably 15 degrees to 45 degrees, and more preferably 25 degrees. Thirty-five degrees is more ideal.
  • the corrugated irregularities are formed by a smooth curved surface, and the angle between the top line 43 and the bottom line 44 and the main flow of the first heat exchange fluid (air) is within a range of 10 degrees to 60 degrees.
  • the formation of the corrugated irregularities so as to form an angle generates a secondary flow of air effective for promoting heat transfer by suppressing separation and local acceleration with respect to the flow of the first heat exchange fluid.
  • FIG. 8 shows a secondary flow (arrow) of the fluid generated on the flat plate when a uniform flow of fluid is introduced into the wavy flat plate, and contour lines due to temperature.
  • the corrugated unevenness by the smooth curved surface suppresses the separation of fluid and local acceleration to generate a strong secondary flow, and also generates a large temperature gradient near the wall surface. . Thereby, heat transfer promotion can be made higher and flow resistance can be made smaller.
  • the plurality of corrugated irregularities formed on the horizontal plane 42 of the corrugated fin 40 are formed such that the top line 43 and the bottom line 44 are continuously repeated in a V shape a plurality of times.
  • a plurality of times means, for example, that a plurality of V characters are in lateral contact with each other so that a V shape is formed by continuously repeating a V character twice. It means that it is formed so as to have a shape obtained side by side, that is, a zigzag shape.
  • the plurality of corrugated irregularities formed on the horizontal surface 42 of the corrugated fin 40 has a first average angle as an average of an angle formed by the oblique line portion 43b in the top line 43 and the main flow of the first heat exchange fluid,
  • An intermediate portion having an average height in the corrugated unevenness is made smaller than a second average angle as an average of an angle formed by a hatched portion 45b in a continuous intermediate portion line 45 and a main flow of the first heat exchange fluid.
  • the corrugated irregularities of the comparative example of FIG. 5A are the main heat exchange fluid (air) in both the bent portion 943a and the shaded portion 943b so that the top line 943 and the top line 944 are V-shaped.
  • the corrugated irregularities of the first embodiment shown in FIG. 4 and FIG. 5B are the average height of the corrugated irregularities with respect to the top line 943 of the corrugated irregularities of the comparative example, as shown by the auxiliary line in FIG.
  • the bent portion 943a is moved so as to extend vertically in the figure so as to avoid deformation of the intermediate portion line 945 where the intermediate portion is continuous, and is bent to a bent portion 43a, and the straight top line 943 is slightly S-curved.
  • the top line 43 is deformed so as to draw.
  • the corrugated bottom line 44 of the first embodiment is the same as the bottom line 944 of the comparative example.
  • the top line 43 of the corrugated unevenness is three-dimensionally shown, but the bottom line 44 is also formed in the same manner as the top line 43.
  • the intermediate line 45 is V-shaped because the top line 43 and the bottom line 44 are V-shaped, and the bent part 43a of the top line 43 and the bent part 44a of the bottom line 44 are illustrated from the position of the comparative example.
  • the position extends slightly in the up / down direction in the figure.
  • the first average angle ⁇ 1 as an average of the angle formed between the inclined portion 43b of the top line 43 and the main flow of the second heat exchange fluid is as shown in FIG.
  • the intermediate portion line 45 slightly extends in the vertical direction in the figure, but for ease of explanation, it is shown in FIG. 6 as not extending in the vertical direction in the figure.
  • the thick solid line is the top line 43
  • the thin solid line is the top line 943 of the comparative example before expansion
  • the thick broken line is the bottom line 44
  • the thin broken line is the bottom line 944 of the comparative example before expansion.
  • the thick dotted line is the intermediate part line 45.
  • L11 is the distance to the part 45a
  • L12 is the distance between the bent part 45a of the intermediate line 45 and the bent part 44a of the bottom line 44
  • the distance between the bent part 44a of the bottom line 44 and the bent part 45 of the intermediate line 45 is L13
  • the distance between the bent part 45a of the intermediate line 45 and the bent part 43a of the top line 43 is L14
  • the distance between the bent part 45a of the intermediate line 45 is L21
  • the distance between the bent part 45a of the intermediate part line 45 and the bent part 44a of the bottom part 44 is L22
  • the bent part 44a of the bottom part line 44 and the bent part 45 of the intermediate part line 45 are Distance L23, medium
  • the corrugated irregularities are bent from the bent portion 44a of the bottom line 44 to the intermediate portion line 45 in the inverted V-shaped bent portion. From the bent portion 43a of the top line 43 to the bent portion 45a of the top line 43, and from the bent portion 43a of the top line 43 to the bent portion 43a of the top line 43.
  • the intermediate line 45 has a relatively gentle downward slope to the bent part 45a, and the intermediate part 45 has a relatively steep downward slope from the bent part 45a of the intermediate line 45 to the bent part 44a of the bottom line 44.
  • a relatively steep upward slope is obtained from the bent portion 44a of the bottom line 44 to the bent portion 45a of the intermediate line 45, and the bent portion 45a of the intermediate line 45 is bent from the bent portion 45a.
  • the portion 43a has a relatively gentle slope
  • the bent portion 43a of the top line 43 to the bent portion 45a of the intermediate portion line 45 has a relatively steep downward slope
  • the bent portion 45a of the intermediate portion 45 has a bottom line 44.
  • a relatively gentle downward slope is obtained up to the bent portion 44a.
  • FIG. 9 is an explanatory diagram showing the result of simulating the relationship between the position of the corrugated surface of the comparative example, the contour line of the local heat flow velocity, and the contour line of the local shear stress.
  • the local heat flow rate is large in the region from the bottom line 44 to the top line 43 and small in the region from the top line 43 to the bottom line 44 when viewed from the direction of the flow of the first heat exchange fluid. It has become. Further, the part from the bent part 44a of the bottom line 44 to the bent part 43a of the top line 43 is larger than the part from the inclined part 44b of the bottom line 44 to the inclined part 43b of the top line 43.
  • the inflow side of 1 heat exchange fluid is larger than the outflow side.
  • the local shear stress is larger at the top line 43, and the bent portion 43a is larger than the inclined portion 43b.
  • the outflow side of the first heat exchange fluid is larger than the inflow side.
  • a region where the local heat flow rate is large indicates a region where heat transfer is highly promoted and greatly contributes to heat exchange, and a region where the local shear stress is large indicates a region where resistance to the flow of the first heat exchange fluid is large. Therefore, by emphasizing the shape of the region where the local heat flow rate is large and relaxing the shape of the region where the local shear stress is large, a heat exchanger with high heat transfer promotion and low flow resistance can be obtained. Since the portion from the bent portion 45a of the intermediate line 45 to the bent portion 43a of the top line 43 in the inverted V-shaped bent portion is a portion having a large local heat flow rate, this portion should be a relatively steep climb slope. Therefore, the heat transfer promotion can be increased.
  • the average angle (first average angle) formed between the inclined portion 43b of the top line 43 and the second heat exchange fluid is the same as that of the top line 943 of the comparative example.
  • the average angle (second average angle) formed with the first heat exchange fluid is small, and from the bent portion 45a of the intermediate line 45 to the bent portion 43a of the top line 43 in the V-shaped bent portion. Since the portion has a relatively gentle slope, the first heat exchange fluid can easily get over the top line 43. For this reason, the flow resistance with respect to the flow of the first heat exchange fluid is reduced.
  • the plurality of corrugated irregularities formed on the horizontal plane 42 of the corrugated fin 40 are concave portions (on the bottom line 44) on the same plane as the projections on one surface of the horizontal plane 42 (the bent portion 43 a and the inclined portion 43 b on the top line 43).
  • the bent portion 44a and the inclined portion 44b) are formed so as to be integrated with each other. That is, the shape of the bent portion 43a and the inclined portion 43b of the top line 43 on one surface of the horizontal plane 42 and the shape of the bent portion 44a and the inclined portion 44b of the bottom line 44 on the same surface are the same when the front and back sides are integrated, that is, the front and back are interchanged. It is formed as follows.
  • heat exchange with the first heat exchange fluid flowing on one surface side of the horizontal surface 42 of the corrugated fin 40 and heat exchange with the first heat exchange fluid flowing on the other surface side of the horizontal surface 42 are performed. This can be done in the same manner, and a heat exchanger with higher heat transfer and lower flow resistance can be obtained.
  • the plurality of corrugated irregularities formed on the horizontal plane 42 of the corrugated fin 40 are formed such that the bent portion 43 a of the top line 43 is positioned near the end of the horizontal plane 42 of the corrugated fin 40. That is, a plurality of corrugations are formed so that more bent portions 43a of the top line 43 are formed.
  • the bending part 43a of the top line 43 which is a site
  • the plurality of corrugated irregularities formed on the horizontal surface 42 of the corrugated fin 40 are formed such that the amplitude of the wave on the inlet side of the first heat exchange fluid (for example, air) is larger than the amplitude of the wave on the outlet side.
  • the height of the bent portion 43a of the top wire 43 is such that the bent portion 43a closest to the outlet from the height Hin of the bent portion 43a closest to the inlet of the first heat exchange fluid (for example, air). The height is gradually lowered so as to become the height Hout.
  • the depth of the bent portion 44a of the bottom line 44 is determined by the depth Hout of the bent portion 44a closest to the outlet from the depth Hin of the bent portion 44a closest to the inlet of the first heat exchange fluid (for example, air). It becomes gradually shallower.
  • the first heat exchange fluid for example, air
  • the top line 43 on the outlet side of the first heat exchange fluid having a large local shear stress is used.
  • the plurality of corrugated irregularities formed on the horizontal surface 42 of the corrugated fin 40 are exchanged with the top line 43 and the bottom line 44 by the first heat exchange with a smooth curved surface.
  • the first average angle as the average of the angle formed between the portion 43b and the main flow of the first heat exchange fluid is the hatched portion 45b in the intermediate portion line 45 where the intermediate portion having the average height in the corrugated irregularities is continuous.
  • first heat exchange fluid By forming the first heat exchange fluid so as to be smaller than the second average angle as an average of the angles formed with the main flow of the first heat exchange fluid, separation or locality is caused with respect to the flow of the first heat exchange fluid.
  • a secondary flow of air can be generated, heat transfer is promoted by emphasizing a portion where the local heat flow rate is large, and the flow of the first heat exchange fluid is reduced by reducing the shear stress at the portion where the local shear stress is large.
  • the flow resistance with respect to can be reduced. As a result, a heat exchanger with higher heat transfer promotion and lower flow resistance can be obtained.
  • the plurality of corrugated irregularities formed on the horizontal plane 42 of the corrugated fin 40 are formed with a convex shape on one surface of the horizontal plane 42 and a concave shape on the same surface. Is formed so as to be integrated with the front and back, heat exchange with the first heat exchange fluid flowing on one surface side of the horizontal surface 42 of the corrugated fin 40 and first heat flowing on the other surface side of the horizontal surface 42 Heat exchange with the replacement fluid can be performed in the same manner. As a result, a heat exchanger with higher heat transfer acceleration and lower flow resistance can be obtained.
  • the plurality of corrugated irregularities formed on the horizontal surface 42 of the corrugated fin 40 are arranged so that the bent portion 43 a of the top line 43 is near the end of the horizontal surface 42 of the corrugated fin 40.
  • the bending part 43a of the top line 43 which is a site
  • the wave amplitude on the inlet side of the first heat exchange fluid (for example, air) is changed between the plurality of waveform irregularities formed on the horizontal surface 42 of the corrugated fin 40.
  • the flow resistance to the flow of the first heat exchange fluid can be reduced.
  • the plurality of corrugated irregularities formed on the horizontal surface 42 of the corrugated fin 40 are formed so that the shape of the convex portion on one surface of the horizontal surface 42 and the shape of the concave portion on the same surface are integrated.
  • the shape of the convex portion on one surface of the horizontal surface 42 may be different from the shape of the concave portion on the same surface.
  • the plurality of corrugations are formed so that the height of the bent portion 43a is higher than the height of the shaded portion 43b with respect to the top line 43, but the depth of the bent portion 44a is the height of the shaded portion 44b with respect to the bottom line 44.
  • the bottom line 44 is formed so that the bent part 44a is deeper than the hatched part 44b, whereas the top line 43 is formed with the bent part 43a.
  • the height may be the same as the height of the hatched portion 43b.
  • a plurality of corrugated irregularities formed on the horizontal surface 42 of the corrugated fin 40 are arranged such that the bent portion 43a of the top line 43 is positioned near the end of the horizontal surface 42 of the corrugated fin 40.
  • the bent portion 43 a of the top line 43 may be formed so as not to be positioned in the vicinity of the end of the horizontal surface 42 of the corrugated fin 40.
  • the plurality of corrugated irregularities formed on the horizontal surface 42 of the corrugated fins 40 are such that the amplitude of the wave on the inlet side of the first heat exchange fluid is larger than the amplitude of the wave on the outlet side.
  • it may be formed such that the amplitude of the wave on the inlet side and the amplitude of the wave on the outlet side of the first heat exchange fluid are the same.
  • the plurality of corrugated irregularities formed on the horizontal surface 42 of the corrugated fin 40 are repeated so that the top line 43 and the bottom line 44 are continuously V-shaped multiple times.
  • the top line 43 and the bottom line 44 may be formed so as to be continuously W-shaped twice in a V shape, or the top line 43 and the bottom line 44 are single. It may be formed so as to have a V shape.
  • a plurality of corrugated irregularities formed on the horizontal surface 42 of the corrugated fin 40 are formed so that the oblique line portion 43b in the top line 43 and the oblique line portion 44b in the bottom line 44 have an S-shaped curve.
  • the hatched portion 43b in the top line 43 and the hatched portion 44b in the bottom line 44 it is not necessary for the hatched portion 43b in the top line 43 and the hatched portion 44b in the bottom line 44 to form an S-curve, and the shape or recess that is convex with respect to the flow of the first heat exchange fluid.
  • the shape may be a straight line or a straight line.
  • a plurality of corrugated irregularities formed on the horizontal surface 42 of the corrugated fin 40 are formed by a smooth curved surface, and a top line 43 connecting the wave tops and a bottom line connecting the wave bottoms.
  • the top line 43 and the bottom line 44 are continuously repeated in a V shape a plurality of times so that the angle ⁇ formed between the main flow of the first heat exchange fluid and the angle 44 is an acute angle.
  • the first average angle as the average of the angle formed between the V-shaped oblique line portion 43b in the top line 43 and the main flow of the first heat exchange fluid is an intermediate portion where the average height in the corrugated unevenness is
  • the intermediate portion 45 is formed so as to be smaller than the second average angle as an average of the angle formed by the V-shaped oblique portion 45b in the continuous intermediate line 45 and the main flow of the first heat exchange fluid
  • the height of the bent part in the top line is the top part. It may alternatively be formed to be higher than the height of the hatched portion of the V-shape in.
  • FIG. 10 three-dimensionally shows the waveform irregularities of the modification. Compared with the corrugated unevenness of the first embodiment of FIG.
  • FIG. 11 is an AA cross section along the top line 53 of the corrugated unevenness of FIG. 10, and also shows the height from the center position that is the average height of the corrugated unevenness of the top line 53.
  • the bent portion 53a of the V-shaped top line 53 is formed such that the height Hua from the center position is higher than the height Hub from the center position of the hatched portion 53b.
  • the bent portion 53a of the top line 53 has a slightly raised shape in the bent portion 43a of the top line 43 of the first embodiment, and the oblique portion 53b of the top line 53 has a shape of the top line 43 of the first embodiment.
  • the reason why the hatched portion 43b is slightly crushed is to emphasize the shape of the portion where the local heat flow rate is large and relax the shape of the portion where the local shear stress is large, as described with reference to FIG. That is, by increasing the height of the bent top portion 53a of the top line 53 where the local heat flow rate is large, the heat transfer acceleration is increased, and the height of the inclined portion 53b of the top line 53 having a large local shear stress is decreased. As a result, the flow resistance can be reduced.
  • the shape of the bottom line 54 is not shown in order to explain the shape of the top line 53, but the waveform irregularities of the modified example are the shape of the top line 53 and the shape of the bottom line 54. Is an integrated front and back. Accordingly, the depth of the bent portion 54a in the bottom line 54 is the same as that in which the height of the bent portion 53a in the top line 53 is higher than the height of the V-shaped hatched portion 53b in the top line 53.
  • the top line 53 is formed so as to be deeper than the depth of the V-shaped oblique line part 53b.
  • FIG. 12 is a cross-sectional view of the corrugated irregularities of the modified example corresponding to the CC cross section of FIG.
  • the corrugated unevenness of the modified example is such that the height Hua of the bent portion 53 a of the top line 53 is higher than the height Hub of the inclined portion 53 b of the top line 53.
  • the height Hua of the bent portion 53a of the top line 53 and the depth Hda of the bent portion 54a of the bottom line 54 are set so that the depth Hda of the bent portion 54a is deeper than the depth Hdb of the inclined portion 53b of the bottom line 54.
  • the height Hub of the inclined portion 53b of the top line 53 and the depth Hdb of the inclined portion 53b of the bottom line 54 are formed so as to match.
  • heat exchange with the first heat exchange fluid flowing on one surface side of the horizontal surface 42 of the corrugated fin 40 and heat exchange with the first heat exchange fluid flowing on the other surface side of the horizontal surface 42 are performed. This can be done in the same manner, and a heat exchanger with higher heat transfer and lower flow resistance can be obtained.
  • the bent portion 53a of the top line 53 may be formed in the vicinity of the end of the horizontal surface 42 of the corrugated fin 40, or on the inlet side of the first heat exchange fluid. It is good also as what forms so that the amplitude of a wave may become larger than the amplitude of the wave of an exit side, and forms so that the top line 53 and the bottom line 54 may become W shape continuously in a V shape only twice.
  • the top line 53 and the bottom line 54 may be formed into a single V-shape, or the shape of the concave portion on the same surface as the shape of the convex portion on one surface of the horizontal surface 42. It is good also as what forms so that it may become different.
  • FIG. 14 is an external view showing the external appearance of the heat exchanger 120 as the second embodiment of the present invention
  • FIG. 15 shows the flat surface of the heat exchange tube 130 used in the heat exchanger 120 of the second embodiment.
  • the heat exchanger 120 of the second embodiment includes a plurality of heat exchange tubes 130 that are formed as flat hollow tubes and arranged in parallel, and ends of the plurality of heat exchange tubes 130.
  • a pair of headers 140 and 150 are attached so as to cover and flow heat exchange fluid into and out of the plurality of heat exchange tubes 30.
  • the heat exchanging tube 130 is formed into a flat tube having a thickness of 0.5 mm by using a plate having a thickness of 0.1 mm made of a material having thermal conductivity, such as a stainless material, by pressing or bending. Has been.
  • a plurality of corrugated irregularities are formed by a smooth curved surface.
  • the plurality of corrugated irregularities of the second embodiment are connected to the top line 143 that connects the tops of the waves and the bottom of the waves, similarly to the plurality of corrugated irregularities formed on the horizontal surface 42 of the corrugated fin 40 of the first embodiment.
  • the top wire 143 and the top wire 143 so that the angle ⁇ between the bottom wire 144 and the main flow of the first heat exchange fluid (eg, air) is an acute angle (about 30 degrees in the second embodiment).
  • the first average angle is an average of the angles formed by the V-shaped oblique line portion 145b in the intermediate line 145 and the main flow of the first heat exchange fluid in the intermediate part line 145 where the intermediate part is the average height of the corrugated irregularities.
  • the top to be smaller than the second average angle It is formed so that the amplitude of the wave on the inlet side of the first heat exchange fluid (air) is larger than the amplitude of the wave on the outlet side so that the bent portion 143a of 143 is positioned in the vicinity of the end of the flat surface. ing.
  • the plurality of corrugations of the second embodiment are smooth curved surfaces, and the angle ⁇ between the top line 143 and the bottom line 144 and the main flow of the first heat exchange fluid (air) is an acute angle range.
  • the oblique line 143b of the top line 143 and the main flow of the first heat exchange fluid are formed so that the top line 143 and the bottom line 144 are continuously repeated in a V shape over a plurality of times.
  • the average angle (first average angle) is formed to be smaller than the average angle (second average angle) formed by the hatched portion 145b of the intermediate portion line 145 and the main flow of the first heat exchange fluid.
  • the plurality of corrugations of the second embodiment are formed such that the bent portion 143a of the top line 143 is located near the end of the flat surface, the plurality of corrugations of the second embodiment Is the wave amplitude on the inlet side of the first heat exchange fluid (air) Reason is formed to be larger than the wave amplitude is the same as the waveform irregularity of the first embodiment.
  • a plurality of corrugated irregularities formed on the flat outer wall surface side of the heat exchanging tube 130 are connected to the top of the wave by a smooth curved surface.
  • the top line 143 and the bottom line 144 are such that the angle ⁇ between the line 143 and the bottom line 144 connecting the bottoms of the waves and the main flow of the first heat exchange fluid (air) is an acute angle.
  • the angle formed by the oblique portion 143b of the top line 143 and the main flow of the first heat exchanging fluid so as to continuously repeat a plurality of times in a V shape (first average angle).
  • the intermediate portion 145 By forming the intermediate portion 145 so as to be smaller than the average angle (second average angle) between the oblique line portion 145b of the intermediate line 145 and the main flow of the first heat exchange fluid, peeling or local acceleration is achieved.
  • Second average angle between the oblique line portion 145b of the intermediate line 145 and the main flow of the first heat exchange fluid.
  • the plurality of corrugated irregularities formed on the outer wall surface side of the flat surface of the heat exchanging tube 130 are the end portions where the bent portions 143a of the top line 143 are flat surfaces.
  • the plurality of corrugated irregularities formed on the outer wall surface side of the flat surface of the heat exchanging tube 130 are replaced with the inlet of the first heat exchanging fluid (for example, air).
  • the first heat exchanging fluid for example, air
  • a plurality of corrugated irregularities formed on the outer flat wall surface side of the heat exchanging tube 130 are arranged such that the bent portion 143a of the top line 143 is located near the end of the flat surface.
  • the bent portion 143a of the top line 143 may be formed so as not to be positioned near the end portion of the flat surface.
  • a plurality of corrugations formed on the flat outer wall surface side of the heat exchanging tube 130 has a wave amplitude on the inlet side of the first heat exchanging fluid.
  • it may be formed such that the amplitude of the wave on the inlet side and the amplitude of the wave on the outlet side of the first heat exchange fluid are the same.
  • a plurality of corrugated irregularities formed on the outer wall surface side of the flat surface of the heat exchange tube 130 are formed a plurality of times so that the top line 143 and the bottom line 144 are V-shaped.
  • the top line 143 and the bottom line 144 may be formed so as to be continuously W-shaped twice in a V shape, or the top line 143 and the bottom line 144 may be formed continuously.
  • the bottom line 144 may be formed in a single V shape.
  • a plurality of corrugated irregularities formed on the flat outer wall surface side of the heat exchanging tube 130 are formed by a smooth curved surface with a top line 143 connecting the wave tops and
  • the top wire 143 and the bottom wire 144 are V-shaped multiple times so that the angle ⁇ formed by the bottom wire 144 connecting the bottom and the main flow of the first heat exchange fluid is an acute angle.
  • the average angle (first average angle) formed between the hatched portion 143b of the top line 143 and the main flow of the first heat exchange fluid is the hatched portion 145b of the intermediate line 145 so as to be continuously repeated.
  • the main flow of the first heat exchange fluid is formed so as to be smaller than the average angle (second average angle), but the height of the bent portion in the top line is further the top line.
  • the present invention can be used in the heat exchanger manufacturing industry and the like.

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

Abstract

De multiples concavités et convexités en forme de vagues, qui sont formées dans des ailettes ondulées, sont formées à partir d'une surface incurvée lisse de sorte que l'angle formé par des lignes de crête (43) et des lignes de creux (44) et l'écoulement principal d'un premier fluide d'échange de chaleur soit un angle aigu, et les lignes de crête (43) et les lignes de creux (44) sont répétées de façon continue à de multiples reprises sous une forme en V, et la moyenne de l'angle formé par une région inclinée (43b) des lignes de crête (43) et l'écoulement principal du premier fluide d'échange de chaleur est inférieur à la moyenne de l'angle formé par une région inclinée (45b) d'une ligne intermédiaire (45) et l'écoulement principal du premier fluide d'échange de chaleur. Ainsi, une séparation et une augmentation localisée de la vitesse peuvent être supprimées et un écoulement de fluide secondaire peut être généré, une région présentant une vitesse d'écoulement thermique locale importante peut être renforcée et le transfert de chaleur peut être favorisé, la contrainte de cisaillement au niveau d'une région présentant une contrainte de cisaillement locale importante peut être réduite et une résistance à l'écoulement peut être réduite.
PCT/JP2013/080788 2012-11-15 2013-11-14 Échangeur de chaleur WO2014077318A1 (fr)

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JP2012-251291 2012-11-15
JP2012251291 2012-11-15

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JP2016020776A (ja) * 2014-07-15 2016-02-04 国立大学法人 東京大学 熱交換器
WO2016043341A1 (fr) * 2014-09-19 2016-03-24 株式会社ティラド Ailettes ondulées pour échangeur de chaleur
WO2016043340A1 (fr) * 2014-09-19 2016-03-24 株式会社ティラド Ailettes ondulées d'échangeur thermique
JPWO2017115436A1 (ja) * 2015-12-28 2018-10-18 国立大学法人 東京大学 熱交換器

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JPH01219497A (ja) * 1988-02-29 1989-09-01 Hitachi Ltd 傾斜波形フイン付き熱交換器
JP2002107074A (ja) * 2000-09-29 2002-04-10 Sanyo Electric Co Ltd プレート型熱交換器及びそれを用いたヒートポンプ給湯機
JP4815612B2 (ja) * 2005-07-29 2011-11-16 国立大学法人 東京大学 熱交換器およびこれを用いた空気調和装置並びに空気性状変換器
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JP2016020776A (ja) * 2014-07-15 2016-02-04 国立大学法人 東京大学 熱交換器
WO2016043341A1 (fr) * 2014-09-19 2016-03-24 株式会社ティラド Ailettes ondulées pour échangeur de chaleur
WO2016043340A1 (fr) * 2014-09-19 2016-03-24 株式会社ティラド Ailettes ondulées d'échangeur thermique
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JPWO2016043340A1 (ja) * 2014-09-19 2017-07-13 株式会社ティラド 熱交換器用コルゲートフィン
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