CN101208575A - Fin tube heat exchanger - Google Patents

Fin tube heat exchanger Download PDF

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Publication number
CN101208575A
CN101208575A CNA2006800229226A CN200680022922A CN101208575A CN 101208575 A CN101208575 A CN 101208575A CN A2006800229226 A CNA2006800229226 A CN A2006800229226A CN 200680022922 A CN200680022922 A CN 200680022922A CN 101208575 A CN101208575 A CN 101208575A
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CN
China
Prior art keywords
guide fins
heat exchanger
flow
fin tube
air
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Granted
Application number
CNA2006800229226A
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Chinese (zh)
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CN100554855C (en
Inventor
藤野宏和
金铉永
镰田俊光
笠井一成
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Daikin Industries Ltd
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Daikin Industries Ltd
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Publication of CN101208575A publication Critical patent/CN101208575A/en
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Publication of CN100554855C publication Critical patent/CN100554855C/en
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F1/00Tubular elements; Assemblies of tubular elements
    • F28F1/10Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
    • F28F1/12Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element
    • F28F1/24Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending transversely
    • F28F1/32Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending transversely the means having portions engaging further tubular elements
    • F28F1/325Fins with openings
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F1/00Tubular elements; Assemblies of tubular elements
    • F28F1/10Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
    • F28F1/12Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element
    • F28F1/24Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending transversely
    • F28F1/32Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending transversely the means having portions engaging further tubular elements
    • 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
    • F28D1/00Heat-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
    • F28D1/02Heat-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
    • F28D1/04Heat-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
    • F28D1/047Heat-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 bent, e.g. in a serpentine or zig-zag
    • 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
    • F28F13/06Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media
    • 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

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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)
  • Details Of Fluid Heaters (AREA)

Abstract

A fin tube heat exchanger where both a heat transmission promotion effect and water discharge ability by guiding fins are simultaneously achieved. The fin tube heat exchanger (1) has heat transmission fins (2) placed in an airflow, and also has heat transmission tubes (3) inserted in the heat transmission fins (2) and placed in the direction substantially orthogonal to the direction of the airflow. A set of guiding fins (21a, 21b) and a set of guiding fins (21c, 21d) are formed by cutting and bending on the surface of each heat transmission fin (2), and the sets are on both sides, respectively, of each heat transmission tube (3). Each set of the guiding fins (21a, 21b)(21c, 21d) are linearly aligned from the upstream side toward the downstream side of the direction of the airflow. Lines (L1, L2) imaginarily connecting the guiding fins (21a, 21b) and the guiding fins (21c, 21d), respectively, are inclined relative to the direction of the airflow so as to guide airflow near each heat transmission tube (3) to the rear side of the direction of the airflow.

Description

Fin tube heat exchanger
Technical field
The present invention relates to fin tube heat exchanger, particularly have the thermofin that is configured in the air-flow, and insert thermofin and be configured in and the flow direction of the air-flow fin tube heat exchanger of a plurality of heat-transfer pipes on the direction of quadrature roughly.
Background technology
In the past, in aircondition etc., be extensive use of and have the thermofin that is configured in the air stream, and insert thermofin and be configured in and the flow direction of the air stream fin tube heat exchanger of a plurality of heat-transfer pipes on the direction of quadrature (that is, intersect fin tube heat exchanger) roughly.
In this fin tube heat exchanger, as dead water region that forms with the part of minimizing in the flow direction downstream of the air stream of the heat-transfer pipe of thermofin and the boundary layer of upgrading thermofin is the heat transfer promotion method of purpose, sometimes adopt following technology: on the position of the heat-transfer pipe both sides on thermofin surface, erect the flow direction upstream side that forms towards air stream and expand the guide fins of opening (with reference to patent documentation 1) by cutting out.
Patent documentation 1: Japanese kokai publication sho 61-110889 communique
But, the fin tube heat exchanger that will adopt above-mentioned the sort of guide fins as with aircondition etc. be representative with the situation of air as the evaporimeter of the thermophores such as cold-producing medium of thermal source under, can produce following problem: guide fins is interior to make the flowing resistance increase because the discharge water that the heat exchange of air and thermophore produces is trapped in.And, under the situation of the fin tube heat exchanger that will adopt above-mentioned the sort of guide fins as the outdoor heat converter of the outdoor unit that constitutes aircondition, sometimes remove the frost that produces on the thermofin surface by the defrosting running, but can produce the problem that drainage reduces this moment.
Summary of the invention
Problem of the present invention is, in fin tube heat exchanger, realizes heat transfer facilitation effect and drainage based on guide fins simultaneously.
The fin tube heat exchanger of the 1st aspect has: thermofin, and it is configured in the air-flow; And a plurality of heat-transfer pipes, it inserts thermofin, and is configured in and the flow direction of air-flow roughly on the direction of quadrature.On thermofin,, erect and be formed with on the thermofin surface from the flow direction upstream side of air-flow a plurality of guide fins towards the straight arrangement in downstream by cutting out in the both sides of heat-transfer pipe.The straight line that a plurality of guide fins are coupled together imaginaryly is to tilt near the side directed mode behind the flow direction of the air-flow of heat-transfer pipe of the air-flow the heat-transfer pipe with respect to the flow direction of air-flow.
In this fin tube heat exchanger, guide fins is split into a plurality of from the flow direction upstream side of air-flow towards the downstream, and, a plurality of guide fins are to tilt near the side directed mode behind the flow direction of the air-flow of heat-transfer pipe of the air-flow the heat-transfer pipe with respect to the flow direction of air-flow, therefore, mainly can obtain following effect reliably: the guide fins of the flow direction front side by the air-flow that is configured in thermofin in a plurality of guide fins is upgraded the boundary layer, and can obtain following effect: the guide fins of the flow direction rear side of the air-flow by being configured in thermofin reduces the dead water region that the part at the flow direction rear side of the air-flow of heat-transfer pipe forms, simultaneously, can easily discharge the discharge water that produces on the thermofin surface from the gap between the guide fins.Thus, can not be subjected to influence, and obtain heat transfer facilitation effect based on guide fins at the discharge water of thermofin surface generation.
And, a plurality of guide fins are arranged towards the downstream as the crow flies from the flow direction upstream side of air-flow, thus, the guide fins of flow direction rear side that is configured in the air-flow of thermofin in a plurality of guide fins has the identical inclination of guide fins with the flow direction front side that is configured in air-flow, therefore, not only can reduce the dead water region that the part at the flow direction rear side of the air-flow of heat-transfer pipe forms, and can prevent to form new dead water region in the behind of guide fins.
As mentioned above, in fin tube heat exchanger of the present invention, can not be subjected to influence at the discharge water of thermofin surface generation, and acquisition is based on the heat transfer facilitation effect of guide fins, and, can prevent to form new dead water region, therefore can realize heat transfer facilitation effect and drainage simultaneously based on guide fins in the behind of guide fins.
The fin tube heat exchanger of the 2nd aspect forms, and in the fin tube heat exchanger aspect the 1st, the height of each guide fins increases gradually towards the flow direction downstream of air-flow.
In this fin tube heat exchanger, form the shape that height increases gradually towards the flow direction downstream of air-flow by the shape that makes each guide fins, thereby can produce vertical vortex in the behind of each guide fins, therefore, can further improve heat transfer facilitation effect based on guide fins.
The fin tube heat exchanger of the 3rd aspect forms, in the fin tube heat exchanger aspect the 1st or the 2nd, be formed with draining promotion portion on thermofin, this draining promotion portion is used to make and is stranded in below the water between the guide fins mutually adjacent on the straight line flows to.
In this fin tube heat exchanger, owing between guide fins, be formed with draining promotion portion, so can further improve the drainage of thermofin.
The fin tube heat exchanger of the 4th aspect forms, and in the fin tube heat exchanger aspect the 3rd, draining promotion portion is the slit that is formed between guide fins adjacent mutually on the straight line.
The fin tube heat exchanger of the 5th aspect forms, in the fin tube heat exchanger aspect the 3rd, draining promotion portion is an otch, and this notch shape is formed on the end of guide fins mutual adjacent on the straight line, promptly is formed on the part that becomes the bottom of guide fins.
The fin tube heat exchanger of the 6th aspect forms, and in the fin tube heat exchanger aspect the 3rd, draining promotion portion is the water guide rib that is formed between guide fins adjacent mutually on the straight line.
Description of drawings
Fig. 1 is the profile of the fin tube heat exchanger of the 1st embodiment of the present invention.
Fig. 2 is the profile along the A-A line of Fig. 1.
Fig. 3 is the profile along the B-B line of Fig. 1.
Fig. 4 is the figure of fin tube heat exchanger that the variation of the 1st embodiment is shown, and is the figure that the C part of Fig. 1 is shown.
Fig. 5 is the figure of fin tube heat exchanger that the variation of the 1st embodiment is shown, and is the figure that the C part of Fig. 1 is shown.
Fig. 6 is the figure of fin tube heat exchanger that the variation of the 1st embodiment is shown, and is the figure that the C part of Fig. 1 is shown.
Fig. 7 is the profile of the fin tube heat exchanger of the 2nd embodiment of the present invention.
Fig. 8 is the profile along the A-A line of Fig. 7.
Fig. 9 is the profile along the B-B line of Fig. 8.
Figure 10 is the figure of fin tube heat exchanger that the variation of the 2nd embodiment is shown, and is the figure that the C part of Fig. 7 is shown.
Figure 11 is the figure of fin tube heat exchanger that the variation of the 2nd embodiment is shown, and is the figure that the C part of Fig. 7 is shown.
Figure 12 is the figure of fin tube heat exchanger that the variation of the 2nd embodiment is shown, and is the figure that the C part of Fig. 7 is shown.
Symbol description
1,101: fin tube heat exchanger; 2,102: thermofin; 3: heat-transfer pipe; 21a~21d, 121a~121f: guide fins; 32,35,132,133,136,137: slit (draining promotion portion); 42,43,142,143,144,145: otch (draining promotion portion); 52,151,154: the water guide rib.
The specific embodiment
Below, the embodiment of fin tube heat exchanger of the present invention is described with reference to the accompanying drawings.
<the 1 embodiment 〉
Fig. 1~Fig. 3 illustrates the major part of the fin tube heat exchanger 1 of the 1st embodiment of the present invention.Here, Fig. 1 is the profile of fin tube heat exchanger 1.Fig. 2 is the profile along the A-A line of Fig. 1.Fig. 3 is the profile along the B-B line of Fig. 1.
(1) basic structure of fin tube heat exchanger
Fin tube heat exchanger 1 is so-called intersection finned tube (cross fin and tube) type heat exchanger, mainly has a plurality of tabular thermofins 2 and a plurality of heat-transfer pipe 3.Thermofin 2 makes its in-plane roughly under the state of the flow direction of air-flows such as air, alignment arrangements on the thickness of slab direction.On thermofin 2, with the flow direction of air-flow roughly on the direction of quadrature, devices spaced apart is formed with a plurality of through hole 2a.Peripheral part of through hole 2a becomes the collar (collar) portion 23 to one of the thickness of slab direction of thermofin 2 side-prominent ring-type.The opposing face butt of collar portion 23 and the face that is formed with collar portion 23 of adjacent thermofin 2 on the thickness of slab direction is guaranteed the interval H that is scheduled between the thickness of slab direction of each thermofin 2.Heat-transfer pipe 3 is the duct members that have thermophore such as cold-producing medium to flow in inside, is inserted in a plurality of thermofin 2 of alignment arrangements on the thickness of slab direction, and is roughly disposing on the direction of quadrature with the flow direction of air-flow.Particularly, heat-transfer pipe 3 connects the through hole 2a that forms on thermofin 2, and the expander operation during assembling by fin tube heat exchanger 1 is close to the inner surface of collar portion 23.
And the fin tube heat exchanger 1 of present embodiment is arranged to be roughly in the orientation of a plurality of heat-transfer pipes 3 under the state of above-below direction and is used.Therefore, air-flow flows through fin tube heat exchanger 1 in the mode of roughly crossing towards horizontal direction.In addition, in the following description, when using the such word in " upside ", " top " or " downside ", " below ", the orientation of expression heat-transfer pipe 3.
(2) detail shape of thermofin
Then, the detail shape to the fin tube heat exchanger 1 employed thermofin 2 of present embodiment describes.
On thermofin 2, in the both sides of each heat-transfer pipe 3 (promptly, the downside of each heat-transfer pipe 3 and upside), erect and form on thermofin 2 surface by cutting out from the flow direction upstream side of air-flow a plurality of (being 2 in the present embodiment) guide fins 21a, 21b and guide fins 21c, 21d towards the straight arrangement in downstream.The straight line L that this guide fins 21a, 21b or guide fins 21c, 21d are coupled together imaginaryly 1, L 2So that near the side directed mode behind the flow direction of the air-flow of heat-transfer pipe 3 of the air-flow the heat-transfer pipe 3 is tilted with respect to the flow direction of air-flow.Here, straight line L 1, L 2The angle of attack (meeting the え angle) α with respect to the flow direction of air-flow 1, α 2Be set in 10 °~30 ° the scope.
And each guide fins 21a~21d forms its height to be increased gradually towards the flow direction downstream of air-flow.In the present embodiment, each guide fins 21a~21d be roughly trapezoidal shape or general triangular shape (with reference to Fig. 3, Fig. 3 is the figure that guide fins 21c, 21d are shown, and guide fins 21a, 21b also have same shape), its maximum height h forms lower than the height H of collar portion 23.And, be configured in from heat-transfer pipe 3 side far away across guide fins 21a~21d cutting out slit pore 22a~22d of being formed on when erecting guide fins 21a~21d on the thermofin 2.
(3) feature of fin tube heat exchanger
In above-mentioned such fin tube heat exchanger that constitutes 1, each guide fins that forms in the both sides of each heat-transfer pipe 3 is split into from the flow direction upstream side of air-flow a plurality of (being 2 in the present embodiment) guide fins 21a towards the downstream, 21b and guide fins 21c, 21d, and, guide fins 21a, 21b and guide fins 21c, 21d is to tilt near the side directed mode behind the flow direction of the air-flow of heat-transfer pipe 3 of the air-flow the heat-transfer pipe 3 with respect to the flow direction of air-flow, therefore, mainly can obtain following effect reliably: the guide fins 21a of the flow direction front side by the air-flow that is configured in thermofin 2 among guide fins 21a~21d, 21c upgrades the boundary layer, and can obtain following effect: the guide fins 21b of the flow direction rear side of the air-flow by being configured in thermofin 2,21d, reduce the dead water region that the part at the flow direction rear side of the air-flow of heat-transfer pipe 3 forms, simultaneously, can be easily from guide fins 21a, between the 21b and guide fins 21c, the discharge water that produces on thermofin 2 surfaces is discharged in gap between the 21d.Thus, can not be subjected to influence, and obtain heat transfer facilitation effect based on guide fins 21a~21d at the discharge water of thermofin 2 surface generations.
And, be arranged in straight line L by making guide fins 21a, 21b and guide fins 21c, 21d as the crow flies towards the downstream from the flow direction upstream side of air-flow 1With straight line L 2On, thereby guide fins 21b, the 21d of the flow direction rear side of the air-flow that is configured in thermofin 2 among guide fins 21a~21d have the identical inclination of guide fins 21a, 21c with the flow direction front side that is configured in air-flow, therefore, not only can reduce the dead water region that the part at the flow direction rear side of the air-flow of heat-transfer pipe 3 forms, and can prevent to form new dead water region in the behind of guide fins 21b, 21d.
As mentioned above, in the fin tube heat exchanger 1 of present embodiment, can not be subjected to influence at the discharge water of thermofin 2 surface generations, and acquisition is based on the heat transfer facilitation effect of guide fins 21a~21d, and, can prevent to form new dead water region, therefore can realize heat transfer facilitation effect and drainage simultaneously based on guide fins in the behind of guide fins 21b, 21d.
And, in this fin tube heat exchanger 1, form flow direction downstream by the shape that makes each guide fins 21a~21d towards air-flow, the shape of Zeng Jiaing highly gradually, thereby can produce vertical vortex in the behind of each guide fins 21a~21d, therefore, can further improve heat transfer facilitation effect based on each guide fins 21a~21d.
(4) variation
In above-mentioned fin tube heat exchanger 1,, also can form to make and be stranded at straight line L in order more easily to discharge the discharge waters that produce on thermofin 2 surfaces between guide fins 21a, the 21b and the gap between guide fins 21c, the 21d 1, L 2Go up between adjacent mutually guide fins 21a, the 21b or the water between guide fins 21c, the 21d flow to the below, the slit 32,35 (with reference to Fig. 4) as draining promotion portion, otch 42,43 (with reference to Fig. 5) or water guide rib 52 (with reference to Fig. 6).Here, Fig. 4~Fig. 6 is the figure that is illustrated on the thermofin 2 the C part of the Fig. 1 when forming various draining promotion portion.
At first, use Fig. 4 explanation on thermofin 2, to form the situation of slit 32,35.In this variation, slit 32,35 is to cross straight line L on above-below direction 1, L 2Mode be formed at straight line L 1Go up between adjacent mutually guide fins 21a, the 21b and at straight line L 2Go up adjacent mutually guide fins 21c, the gap portion between the 21d.Here, in order not influence heat transfer property as far as possible, for example, make the slit width of slit 32,35 narrower thus by form slit (cutting the れ order) longitudinally on thermofin 2 surfaces.And,, also can form the slit 31,33,34,36 same with slit 32,35 between guide fins 21a, the 21b and the end of each guide fins 21a~21d beyond the gap portion between guide fins 21c, the 21d.
Then, use Fig. 5 explanation on thermofin 2, to form the situation of otch 42,43.In this variation, otch 42,43 is formed at straight line L 1, L 2Go up on the end of adjacent mutually guide fins 21a, 21b and guide fins 21c, 21d, promptly be formed at the part that becomes the bottom (that is, guide fins 21a, 21b and guide fins 21c, 21d's becomes the part of bottom along gravity direction) of guide fins 21a, 21b and guide fins 21c, 21d.Particularly, be formed on the bottom of guide fins 21b and the bottom of guide fins 21c.Here, otch the 42, the 43rd, in the bottom of guide fins 21b, 21c, with erect the slit longitudinally that formed slit pore 22b, 22c are communicated with when forming guide fins 21b, 21c mode forms by cutting out.And the end of each guide fins 21a, 21d beyond the part that becomes the bottom of guide fins 21b, 21c also can form the otch 41,44 same with otch 42,43.
Then, use Fig. 6 explanation on thermofin 2, to form the situation of water guide rib 52.In this variation, water guide rib 52 is to cross straight line L on above-below direction 1, L 2Mode be formed at straight line L 1Go up between adjacent mutually guide fins 21a, the 21b and at straight line L 2Go up adjacent mutually guide fins 21c, the gap portion between the 21d.Here, water guide rib 52 is by thermofin 2 surface being implemented the elongated projection at longitudinal extension that punch process etc. form, and forms the gap portion that connects continuously on above-below direction (being gravity direction) between guide fins 21a, the 21b and the gap portion between guide fins 21c, the 21d.In addition, near heat-transfer pipe 3, water guide rib 52 is extended as the crow flies on above-below direction, therefore circular-arc by only near the part of collar portion 23 being formed, keep the state that roughly on gravity direction, forms continuously.And, the part of the flow direction rear side of the part of the flow direction front side of air-flow beyond the gap portion between the gap portion between guide fins 21a, the 21b and guide fins 21c, 21d, guide fins 21a, 21c and the air-flow of guide fins 21b, 21d also can form the water guide rib 51,53 same with water guide rib 52.
As mentioned above, in the fin tube heat exchanger 1 of this variation, at the straight line L of thermofin 2 1Go up between adjacent mutually guide fins 21a, the 21b and straight line L 2Go up the slit 32,35, otch 42,43 or the water guide rib 52 that are formed with between adjacent mutually guide fins 21c, the 21d as draining promotion portion, therefore, can further improve the drainage of thermofin 2.
<the 2 embodiment 〉
Fig. 7~Fig. 9 illustrates the major part of the fin tube heat exchanger 101 of the 2nd embodiment of the present invention.Here, Fig. 7 is the profile of fin tube heat exchanger 101.Fig. 8 is the profile along the A-A line of Fig. 7.Fig. 9 is the profile along the B-B line of Fig. 7.
(1) basic structure of fin tube heat exchanger
About the basic structure of fin tube heat exchanger 101, except the guide fins 121a~121f of thermofin 102 described later, identical with the structure of the fin tube heat exchanger 1 of the 1st embodiment.Therefore, about the basic structure of fin tube heat exchanger 101, the label relevant with thermofin 102 replaced with 100 grades from 10 grades, and omit explanation.
Then, the detail shape to the fin tube heat exchanger 101 employed thermofins 102 of present embodiment describes.
On thermofin 102, in the both sides of each heat-transfer pipe 3 (promptly, the downside of each heat-transfer pipe 3 and upside), erect and form on thermofin 102 surface from the flow direction upstream side of air-flow by cutting out towards a plurality of (being 3 in the present embodiment) guide fins 121a, 121b, the 121c of the straight arrangement in downstream and guide fins 121d, 121e, 121f.The straight line L that this guide fins 121a, 121b, 121c or guide fins 121d, 121e, 121f are coupled together imaginaryly 1, L 2So that near the side directed mode behind the flow direction of the air-flow of heat-transfer pipe 3 of the air-flow the heat-transfer pipe 3 is tilted with respect to the flow direction of air-flow.Here, straight line L 1, L 2Angle of attack α with respect to the flow direction of air-flow 1, α 2Be set in 10 °~30 ° the scope.
And each guide fins 121a~121f forms its height to be increased gradually towards the flow direction downstream of air-flow.In the present embodiment, each guide fins 121a~121f be roughly trapezoidal shape or general triangular shape (with reference to Fig. 9, Fig. 9 is the figure that guide fins 121d, 121e, 121f are shown, guide fins 121a, 121b, 121c also have same shape), its maximum height h forms lower than the height H of collar portion 123.And, be configured in from heat-transfer pipe 3 side far away across guide fins 121a~121f cutting out slit pore 122a~122f of being formed on when erecting guide fins 121a~121d on the thermofin 102.
As mentioned above, the guide fins of the fin tube heat exchanger 1 of the 1st embodiment is two the structure of being divided into of guide fins 21a, 21b and guide fins 21c, 21d, relative therewith, in the fin tube heat exchanger 101 of present embodiment, three the structure of being divided into for guide fins 121a, 121b, 121c and guide fins 121d, 121e, 121f, therefore, be used to discharge the quantity increase in the gap between the guide fins of the thermofin 102 surperficial discharge waters that produce.Therefore, compare, can improve the drainage of discharge water with the fin tube heat exchanger 1 of the 1st embodiment.
(2) variation
In above-mentioned fin tube heat exchanger 101, same with the fin tube heat exchanger 1 of the 1st embodiment, in order more easily to discharge the discharge waters that produce on thermofin 102 surfaces, also can form to make and be stranded at straight line L between guide fins 121a, the 121b, between guide fins 121b, the 121c, between guide fins 121d, the 121e and the gap between guide fins 121e, the 121f 1, L 2Go up between adjacent mutually guide fins 121a, the 121b, between guide fins 121b, the 121c, between guide fins 121d, the 121e and the water between guide fins 121e, the 121f flow to the below, the slit 132,133,136,137 (with reference to Figure 10) as draining promotion portion, otch 142,143,144,145 (with reference to Figure 11) or water guide rib 152,153 (with reference to Figure 12).Here, Figure 10~Figure 12 is the figure that is illustrated on the thermofin 102 the C part of the Fig. 7 when forming various draining promotion portion.
In addition, the shape of slit, otch and water guide rib etc. are identical with slit 32,35, otch 42,43 or the water guide rib 52 of the variation of the 1st embodiment, therefore omit explanation.And, in this fin tube heat exchanger 101, same with the fin tube heat exchanger 1 of the variation of the 1st embodiment, in order to discharge the discharge water that on thermofin 102 surfaces, produces, part beyond between guide fins 121a, the 121b, between guide fins 121b, the 121c, between guide fins 121d, the 121e and between guide fins 121e, the 121f also can form slit 131,134,135,138, otch 141,146 or water guide rib 151,154.
<other embodiment 〉
More than, embodiments of the present invention have been described with reference to the accompanying drawings, still, concrete structure is not limited to these embodiments, can change in the scope that does not break away from inventive concept.
Utilizability on the industry
Utilize the present invention, in fin tube heat exchanger, can realize based on guide fins simultaneously Heat transfer facilitation effect and drainage.

Claims (6)

1. a fin tube heat exchanger (1,101), this fin tube heat exchanger (1,101) has:
Thermofin (2,102), it is configured in the air-flow; And
A plurality of heat-transfer pipes (3), it inserts described thermofin, and is configured in and the flow direction of air-flow roughly on the direction of quadrature,
On described thermofin, in the both sides of described heat-transfer pipe, by cut out erect and be formed with on described thermofin surface from the flow direction upstream side of air-flow towards a plurality of guide fins of the straight arrangement in downstream (21a~21d, 121a~121f),
Straight line (the L that described a plurality of guide fins are coupled together imaginaryly 1, L 2) so that near the side directed mode behind the flow direction of the air-flow of described heat-transfer pipe of the air-flow the described heat-transfer pipe is tilted with respect to the flow direction of air-flow.
2. fin tube heat exchanger according to claim 1 (1,101) is characterized in that,
(height of 21a~21d, 121a~121f) increases towards the flow direction downstream of air-flow described each guide fins gradually.
3. fin tube heat exchanger according to claim 1 and 2 (1,101) is characterized in that,
Be formed with draining promotion portion on described thermofin (2,102), this draining promotion portion is used to make and is stranded at described straight line (L 1, L 2) (water between 21a~21d, the 121a~121f) flows to the below to go up adjacent mutually described guide fins.
4. fin tube heat exchanger according to claim 3 (1,101) is characterized in that,
Described draining promotion portion is slit (32,35,132,133,136,137), and described slit (32,35,132,133,136,137) is formed at described straight line (L 1, L 2) go up adjacent mutually described guide fins (between 21a~21d, the 121a~121f).
5. fin tube heat exchanger according to claim 3 (1,101) is characterized in that,
Described draining promotion portion is otch (42,43,142,143,144,145), and described otch (42,43,142,143,144,145) is formed at described straight line (L 1, L 2) go up adjacent mutually described guide fins and (on the end of 21a~21d, 121a~121f), promptly be formed on the part that becomes the bottom of described guide fins.
6. fin tube heat exchanger according to claim 3 (1,101) is characterized in that,
Described draining promotion portion is water guide rib (52,151,154), and described water guide rib (52,151,154) is formed at described straight line (L 1, L 2) go up adjacent mutually described guide fins (between 21a~21d, the 121a~121f).
CNB2006800229226A 2005-07-01 2006-06-26 Fin tube heat exchanger Expired - Fee Related CN100554855C (en)

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JP2005194254A JP2007010279A (en) 2005-07-01 2005-07-01 Fin tube type heat exchanger
JP194254/2005 2005-07-01

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KR (1) KR100973225B1 (en)
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AU (1) AU2006266965B2 (en)
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105758246A (en) * 2014-12-15 2016-07-13 浙江盾安人工环境股份有限公司 Heat exchanger fin and heat exchanger
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Families Citing this family (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5162929B2 (en) * 2007-03-14 2013-03-13 ダイキン工業株式会社 Finned tube heat exchanger
JP2008232448A (en) * 2007-03-16 2008-10-02 Daikin Ind Ltd Fin tube-type heat exchanger and air conditioner
JP4293252B2 (en) * 2007-03-19 2009-07-08 ダイキン工業株式会社 Fin for heat exchanger, guide and method of using the same
JP2008249298A (en) * 2007-03-30 2008-10-16 Daikin Ind Ltd Fin tube type heat exchanger
JP5304024B2 (en) * 2008-05-27 2013-10-02 ダイキン工業株式会社 Finned tube heat exchanger
JP5304025B2 (en) * 2008-05-27 2013-10-02 ダイキン工業株式会社 Finned tube heat exchanger
CN102374816A (en) * 2011-11-09 2012-03-14 海信(山东)空调有限公司 Ring-wing bridge-type heat-exchanger fin, heat exchanger and air conditioner
US10005413B2 (en) 2016-10-05 2018-06-26 Toyota Motor Engineering & Manufacturing North America, Inc. Vehicles including front grille assemblies with air flow director fins
JP6680225B2 (en) * 2017-01-19 2020-04-15 株式会社デンソー Heat exchanger and method for manufacturing heat exchanger
US11236951B2 (en) * 2018-12-06 2022-02-01 Johnson Controls Technology Company Heat exchanger fin surface enhancement
US11988462B2 (en) * 2020-08-31 2024-05-21 Samsung Electronics Co., Ltd. Heat exchanger and air conditioner using the heat exchanger
CN112964112A (en) * 2021-03-25 2021-06-15 山东西努克机械科技有限公司 Efficient radiating fin

Family Cites Families (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59185992A (en) * 1983-04-06 1984-10-22 Mitsubishi Electric Corp Heat exchanger
JPS59208396A (en) * 1983-05-11 1984-11-26 Mitsubishi Electric Corp Heat exchanger
JPS59215596A (en) * 1983-05-19 1984-12-05 Mitsubishi Electric Corp Heat exchanger
JPS6020094A (en) * 1983-07-13 1985-02-01 Mitsubishi Electric Corp Heat exchanger
JPS616590A (en) * 1984-06-19 1986-01-13 Matsushita Electric Ind Co Ltd Finned heat exchanger
KR890002903B1 (en) * 1984-09-04 1989-08-08 마쯔시다덴기산교 가부시기가이샤 Heat exchanger
DE3737217C3 (en) * 1987-11-03 1994-09-01 Gea Luftkuehler Happel Gmbh Heat exchanger tube
JP2798959B2 (en) * 1989-03-30 1998-09-17 株式会社東芝 Heat exchanger
JPH05164489A (en) * 1991-12-12 1993-06-29 Daikin Ind Ltd Heat exchanger with fin
JPH09159390A (en) * 1995-12-06 1997-06-20 Matsushita Electric Ind Co Ltd Heat exchanger for hot-water supply
JPH109786A (en) * 1996-06-21 1998-01-16 Matsushita Refrig Co Ltd Finned heat exchanger
KR100210073B1 (en) * 1996-07-09 1999-07-15 윤종용 Heat exchanger of air conditioner
JPH10332291A (en) * 1997-05-30 1998-12-15 Mitsubishi Heavy Ind Ltd Fin and tube type heat-exchanger
JP2001147087A (en) * 1999-11-19 2001-05-29 Fujitsu General Ltd Fin-tube type of heat exchanger
KR100363317B1 (en) * 2000-03-31 2002-12-02 만도공조 주식회사 Radiation fin of heat exchanger
CA2391077A1 (en) * 2001-06-28 2002-12-28 York International Corporation High-v plate fin for a heat exchanger and a method of manufacturing
US7337831B2 (en) * 2001-08-10 2008-03-04 Yokohama Tlo Company Ltd. Heat transfer device

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114440328A (en) * 2014-05-15 2022-05-06 三菱电机株式会社 Heat exchanger and refrigeration cycle device provided with same
CN105758246A (en) * 2014-12-15 2016-07-13 浙江盾安人工环境股份有限公司 Heat exchanger fin and heat exchanger
CN105758246B (en) * 2014-12-15 2019-06-11 浙江盾安人工环境股份有限公司 Heat exchanger fin and heat exchanger

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AU2006266965B2 (en) 2009-08-13
CN100554855C (en) 2009-10-28
KR100973225B1 (en) 2010-07-30
JP2007010279A (en) 2007-01-18
US20100175864A1 (en) 2010-07-15
KR20080011445A (en) 2008-02-04
EP1906129B1 (en) 2011-09-07
ES2370795T3 (en) 2011-12-22
WO2007004457A1 (en) 2007-01-11
EP1906129A4 (en) 2010-08-11
AU2006266965A1 (en) 2007-01-11
WO2007004457A8 (en) 2008-01-31
EP1906129A1 (en) 2008-04-02

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