US20080087408A1 - Multi -Channeled Flat Tube And Heat Exchanger - Google Patents
Multi -Channeled Flat Tube And Heat Exchanger Download PDFInfo
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- US20080087408A1 US20080087408A1 US11/660,918 US66091805A US2008087408A1 US 20080087408 A1 US20080087408 A1 US 20080087408A1 US 66091805 A US66091805 A US 66091805A US 2008087408 A1 US2008087408 A1 US 2008087408A1
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- tube
- partitions
- tubes
- channeled
- channeled flat
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F1/00—Tubular elements; Assemblies of tubular elements
- F28F1/02—Tubular elements of cross-section which is non-circular
- F28F1/022—Tubular elements of cross-section which is non-circular with multiple channels
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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
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F1/00—Tubular elements; Assemblies of tubular elements
- F28F1/10—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
- F28F1/12—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
- F28F1/24—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 and extending transversely
- F28F1/32—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 and extending transversely the means having portions engaging further tubular elements
Definitions
- the present invention relates to the construction of a multi-channeled flat tube used in a heat exchanger.
- a plate-fin heat exchanger equipped with a plurality of plate fins disposed in parallel at regular intervals and a plurality of tubes disposed so as to pass through such fins is known as one example of a heat exchanger used in refrigeration apparatuses, radiators, and the like.
- One method of manufacturing a plate-fin heat exchanger includes passing the tubes through the fins to assemble, and expanding or enlarging the tubes to join the tubes and fins together. In the expanding the tubes, a rigid rod or a tube expander is inserted into the tubes to press out and widen the tubes from the inside. By expanding the tubes, the tubes and fins are brought into contact.
- a multi-channeled flat tube includes a plurality of partitions provided inside of the tube to divide the inside of the tube into a plurality of parallel channels.
- Japanese Laid-Open Patent Publication No. S62-19691 discloses a tube with an oval or rectangular cross-section. By expanding the surface of the tube bridging between pairs of joints, the tube surface is pressed onto cooling fins. When the tube (wall of tube) expands outward, the joints deform from their original “mountain” shapes (chevron shapes) to flat shapes, thereby preventing the wall of the tube from contracting or shrinking to their original positions.
- One aspect of the present invention is a multi-channeled flat tube including: a flat outer tube; and a plurality of partitions that divide an inside of the outer tube into a plurality of channels.
- Each of the plurality of partitions has a chevron (mountain-shaped) cross-sectional form composed of two sides. Each of the two sides has a thickness ti and a length a.
- the plurality of partitions are disposed so that a face-to-face distance between adjacent partitions of the plurality of partitions along inner surfaces of the outer tube is Li.
- a thickness to of the outer tube satisfies Condition (1) below Equation ⁇ ⁇ 1 Li ⁇ ti ⁇ a 2 - ti 2 3 ⁇ a ⁇ to . ( 1 )
- One method of expanding tube is inserting tube expanders into channels of a multi-channeled flat tube. Aside from this method, research has been conducted into introducing a fluid into a multi-channeled flat tube to raise the internal pressure and thereby extend the partitions. Regardless of whether a method that raises the internal pressure of the tube (hereinafter referred to as “pressurized tube expansion”) or expansion using tube expanders is carried out, it is not preferable for the outer tubes located between adjacent partitions (hereinafter referred to as “outer walls”) to expand outward so that the tube outer surface deforms into a wavy or undulating form. This would reduce the contact surface area between the tube outer surface and the fins and reduce the heat transfer performance. However, if tube expansion is stopped before the partitions have extended to reach the desired size, the desired performance cannot be obtained.
- the tensile stress that acts from both ends of the partition causes deformation (hereinafter, “stretch deformation”) that reduces the thickness of the partition.
- the amount of stress that changes the inclination of a partition differs to the amount of stress that causes stretch deformation of the partition and makes the partition thinner, with less stress being required to change the inclination of the partition.
- a multi-channeled flat tube with an outer tube whose thickness satisfies Condition (1) given above, the outer walls at parts of the outer tube between partitions will not deform in a range of pressure that is high enough to change the inclination of the partitions. Accordingly, a multi-channeled flat tube that satisfies Condition (1) described above can prevent deformation in the outer walls until the partitions have become straightened out. This means that by using an internal pressure in a range where there is deformation in the inclination of the partitions, the multi-channeled flat tube can be expanded in a state where deformation in the tube outer surface into a wavy or undulating state is prevented.
- the amount of deformation in the inclination of the partitions varies due to the influence of tolerances for the multi-channeled flat tube and fluctuations in the applied pressure.
- the tube should preferably be expanded with a maximum pressure (internal pressure) in the range where deformation occurs in the inclination of the partitions, or a higher pressure.
- internal pressure internal pressure
- By expanding the tube with such pressure it is possible to expand a tube until a state where the inclined partitions become substantially straightened out. Accordingly, during expansion, it is possible to expand the multi-channeled flat tube to a desired state without having to carry out control of the pressure varying step-by-step.
- the thickness to of the outer tube is small so that the thickness to of the outer tube is outside the range of Condition (1), there is the possibility of deformation occurring in the outer tube before the partitions have become straightened out. Accordingly, pressure control during tube expansion becomes difficult.
- Another aspect of this invention is a heat exchanger that includes: a plurality of multi-channeled flat tubes that satisfy Condition (1); and a plurality of fins that are attached to the multi-channeled flat tubes. It is preferable that the plurality of multi-channeled flat tubes pass through the plurality of fins.
- Condition (1) regardless of whether pressurized tube expansion is carried out using a fluid or whether the tube is expanded using tube expanders, it will be possible to extend the partitions while suppressing deformation in the outer walls. This means that it is possible to raise the contact efficiency after tube expansion between the plurality of multi-channeled flat tubes and the plate fins through which the tubes pass and to which the tubes are attached.
- One of other aspects of the present invention is a multi-channeled flat tube where in addition to Condition (1) above, the thickness to of the outer tube also satisfies Condition (2) below Equation ⁇ ⁇ 2 2 ⁇ Li ⁇ ti ⁇ a 2 - ti 2 3 ⁇ a ⁇ to . ( 2 )
- one of other aspects of the present invention is a multi-channeled flat tube where in addition to Condition (1) above, the thickness to of the outer tube also satisfies Condition (3) below Equation ⁇ ⁇ 3 Li ⁇ ti 2 ⁇ to . ( 3 )
- a pressure that is equal to or greater than the pressure used during tube expansion is not a normal operating pressure of a multi-channeled flat tube. If such pressure were applied during normal operation, there would be the possibility of further deformation in the multi-channeled flat tube since this is not how multi-channeled flat tubes are designed. Accordingly, the pressure used during tube expansion is an upper limit of the withstand pressure conditions for normal operation or even higher. Also, the pressure used during tube expansion is set up to at a pressure whereby the partitions become straightened out and is not set at a pressure whereby stretch deformation of partitions, which makes the partitions thinner, commences. This means it is economical to set the thickness of the outer tubes so that the outer walls deform at a pressure where stretch deformation, which makes the partitions thinner, commences. The heat transfer efficiency also increasing when thin outer tubes are used.
- FIG. 1 schematically shows a heat exchanger
- FIG. 2 shows a state where multi-channeled flat tubes and fins of the heat exchanger shown in FIG. 1 have been joined together.
- FIG. 3 ( a ) shows a cross section in a length direction of the multi-channeled flat tubes before tube expansion and
- FIG. 3 ( b ) shows a cross section of one of the multi-channeled flat tubes in a minor axis direction.
- FIG. 4 ( a ) shows a cross section in the length direction of the multi-channeled flat tubes after tube expansion
- FIG. 4 ( b ) shows a cross section in the minor axis direction of an end part of one of the multi-channeled flat tubes
- FIG. 4 ( c ) shows a cross section in the minor axis direction of another part of such multi-channeled flat tube.
- FIG. 5 ( a ) shows “angle deformation” of partitions and FIG. 5 ( b ) shows “stretch deformation” of the partitions.
- FIG. 6 shows an enlargement of a cross section of a multi-channeled flat tube.
- FIG. 7 shows changes in the inner diameter of a multi-channeled flat tube when the internal pressure has been raised.
- FIG. 8 shows how fluctuations occur in the amount by which the multi-channeled flat tubes expand due to tolerances and the like.
- FIG. 9 shows examples of an upper limit and a lower limit for the thickness of the outer tube of a multi-channeled flat tube.
- FIG. 1 schematically shows a heat exchanger that uses multi-channeled flat tubes.
- FIG. 2 is a perspective view showing an enlargement of a state where the multi-channeled flat tubes have been expanded.
- the heat exchanger 1 is a plate fin-type heat exchanger.
- the heat exchanger 1 has a plurality of plate-like fins 2 disposed in parallel at regular intervals and a plurality of multi-channeled flat tubes 3 that are disposed in parallel and are joined to the fins 2 in a state where the multi-channeled flat tubes 3 pass through the fins 2 .
- Each multi-channeled flat tube (flat multi-channeled tube, multi-channel flat tube) 3 is constructed so that the inside of a flat outer tube 21 is divided into a plurality of parallel channels 14 by a plurality of partitions 15 .
- End parts 4 at both ends of the multi-channeled flat tubes 3 are connected to joining holes 19 formed in side walls 9 of headers 6 and 7 positioned on the left and right sides of the heat exchanger 1 .
- a heat transfer medium (internal fluid) introduced from a supply outlet 11 of the header 6 passes through the channels 14 of the multi-channeled flat tubes 3 and is guided or led to an output outlet 12 of the header 7 .
- FIG. 3 ( a ) shows the multi-channeled flat tubes 3 before the tubes have been expanded.
- the multi-channeled flat tubes 3 are inserted into burring holes 18 provided in advance in the fins 2 to provisionally assemble the fins 2 and the multi-channeled flat tubes 3 together.
- FIG. 3 ( b ) shows an enlargement of the cross-section of a multi-channeled flat tube 3 .
- the outer tube 21 of the multi-channeled flat tube 3 includes outer walls 21 w that oppose each other at the top and bottom of the multi-channeled flat tube 3 .
- the multi-channeled flat tube 3 is a flat tube molded so that the outer wall 21 w that forms the upper wall or top wall of the outer tube 21 and the outer wall 21 w that forms the lower wall or bottom wall are substantially parallel.
- a plurality of partitions 15 that connect the upper and lower outer walls 21 w and respectively have cross-section bent like “mountain”-shaped (V-shaped) to the length direction X of the cross-section of the multi-channeled flat tube 3 are provided inside each multi-channeled flat tube 3 .
- These partitions 15 divide the inside of the flat tube 3 to form the plurality of parallel channels 14 .
- the end parts 4 of the multi-channeled flat tubes 3 that have been assembled so as to pass through the fins 2 are inserted into the joining holes 19 provided in the headers 6 and 7 . These end parts 4 are joined to the headers 6 and 7 by brazing or another suitable method. By doing so, the parallel flow channels 14 of the individual flat tubes 3 are connected via the headers 6 and 7 and form internal paths through which the heat transfer medium flows.
- FIGS. 4 ( a ), 4 ( b ), and 4 ( c ) are cross-sectional views showing the state of the multi-channeled flat tubes 3 after pressurized tube expansion.
- FIGS. 5 ( a ) and 5 ( b ) show how the partitions 15 of the multi-channeled flat tubes 3 are straightened.
- a compressed fluid can be supplied via the headers 6 and 7 to the multi-channeled flat tubes 3 .
- the compressed fluid raises the internal pressure of the parallel channels 14 and can expand multi-channeled flat tubes 3 (pressurized tube expansion).
- FIG. 4 ( a ) By expanding the tubes 3 , as shown in FIG. 4 ( a ), the multi-channeled flat tubes 3 and the respective fins 2 are tightly joined.
- the headers 6 and 7 are joined to the end parts 4 of the multi-channeled flat tubes 3 in advance. This means that as shown in FIG. 4 ( b ), the bent partitions 15 are not straightened at the end parts 4 of the tubes 3 . At other parts, including the parts where the multi-channeled flat tubes 3 pass through the fins 2 , the bent partitions 15 are straightened as shown in FIG. 4 ( c ).
- Each of the partitions 15 of the multi-channeled flat tubes 3 that is used in the heat exchanger 1 has a thickness ti and each side out of the two sides forming the mountain shape has a length a.
- the gap (face-to-face distance (distance between surfaces)) between the partitions (adjacent partitions) 15 along the inner surfaces of the outer walls 21 w of the flat outer tube 21 is the distance Li.
- the thickness to of the outer tube 21 satisfies Equation (1) below. Equation ⁇ ⁇ 1 Li ⁇ ti ⁇ a 2 - ti 2 3 ⁇ a ⁇ to . ( 1 )
- the straighten or straitened state of this specification is the state that a corner (base) 26 where the partition 15 is connected to the wall 21 w of the outer tube 21 and the peak point 25 where the two sides 27 that form the mountain shape meet become offset substantially by only the thickness ti of the partition 15 .
- This state is shown in FIG. 6 .
- deformation that occurs thereafter is assumed to be deformation (referred to as “stretch deformation”) caused by stretching that reduces the thickness of the partitions 15 .
- stretch deformation the mechanism by which the partitions 15 deform changes. This means that by applying pressure in a range from a pressure where angle deformation ends to a pressure where stretch deformation commences, it is possible to stably cause the partitions 15 to deform until the partitions 15 become substantially straight.
- FIG. 7 shows the result of measuring the relationship between the inner height of the tube (the inner diameter or inner dimension in the minor axis Y) Hi and the internal pressure (the applied pressure).
- the solid line A 1 shown in FIG. 7 shows measured values for the case where the plate thickness ti of the partitions 15 is set at 0.19 mm and the dot-dash line A 2 shows values produced by calculating the tangent (tan) from the measured values of the angle ⁇ by which the partitions 15 are bent.
- the tube height Hi suddenly increases from a point where the internal pressure exceeds 2 MPa or thereabouts, showing that angle deformation is occurring for the partitions 15 .
- the peak points 25 of the partitions 15 are positioned so as to be displaced from the base parts 26 by only the thickness ti of the partitions 15 , it is assumed that the partitions 15 have been the straightened state and angle deformation has ended.
- angle deformation ends at an internal pressure of around 7 to 8 MPa. Accordingly, if the internal pressure used to expand the tubes is set at around 7 to 8 MPa or higher, it will be possible the partitions 15 become the straightened state.
- the target value of the height Hi during tube expansion is set at a position like H 3 in FIG. 8 where angle deformation has ended, it will be possible to set the internal pressure during tube expansion at a value such as P 3 in FIG. 8 , which can be the pressure at which angle deformation ends or an even higher pressure.
- P 3 in FIG. 8 can be the pressure at which angle deformation ends or an even higher pressure.
- the force (internal pressure) required for angle deformation of the partitions 15 can be calculated from the force applied when the partitions 15 become the straightened state as shown in FIG. 6 . Having no intentional deformation of at least the outer walls 21 w of the outer tubes 21 when such internal pressure is applied is one condition for the present invention. In FIG.
- the stress co produced in the outer walls 21 w when the internal pressure P acts on the outer walls 21 w is as follows.
- a partition 15 is pulled upward and downward by the forces that act at the bases 26 .
- the partition 15 is thought to deform due to the bending moment acting on the bases 26 and the peak point 25 where the center of the partition and the two sides 27 are joined.
- the partition 15 can be modeled as a fixed beam (beam whose both ends are fixed) of an effective length 2 a and a thickness ti that receives a concentrated load W′ at the center 25 thereof.
- the concentrated load W′ that acts on the partition 15 will be minimized when tan ⁇ is maximized, and therefore calculations can proceed for the conditions where angle deformation occurs for a minimum concentrated load W′.
- the condition that the tan ⁇ is maximized indicates that angle deformation has ended for the partition 15 and the partition 15 has been the straightened state, which means that the inclination ⁇ can be expressed by Equation (7). Accordingly, the concentrated load W′ can be found as shown in Equation (8).
- Equation 9 The maximum bending moment Mmax during angle deformation of the partitions 15 is as shown in Equation (9).
- the maximum stress ⁇ i occurring in the partitions 15 is as shown in Equation (11). Note that since modeling is carried out based on the cross-sectional form of a multi-channeled flat tube, stress is calculated in one dimension.
- the outer walls 21 w should not deform in a range of pressure where angle deformation occurs for the partitions 15 . Accordingly, when the minimum pressure Pmin for expanding the tubes is applied to the multi-channeled flat tubes 3 , the threshold stress ⁇ lim of the material that constructs the outer walls 21 w and the partitions 15 , for example, a metal material including aluminum and copper, the maximum stress ⁇ i when angle deformation occurs for the partitions 15 , and the maximum stress ⁇ o applied to the outer walls 21 w should satisfy Equation (12) below.
- Equation (12) From Equation (12), it is possible to reach Condition (1) above. Note that the length a of one side 27 of a partition 15 is expressed as shown in Equation (13) below.
- Equation 13 a ⁇ square root over (( Hi/ 2) 2 +ti 2 ) ⁇ (13)
- multi-channeled flat tubes One merit of multi-channeled flat tubes is that the strength of the flat tubes is increased by the partitions disposed inside the tubes, and therefore the outer walls 21 w , or in other words, the outer tubes 21 can be made thinner.
- the maximum stress co produced in the outer walls 21 w is as shown by Equation (6) given earlier.
- the thickness to of the outer walls 21 w should preferably satisfy Condition (2). Equation ⁇ ⁇ 2 2 ⁇ Li ⁇ ti ⁇ a 2 - ti 2 3 ⁇ a ⁇ to ( 2 )
- the thickness to of the outer tubes 21 can be such that the flat outer tubes 21 deform at a pressure that causes stretch deformation of the partitions 15 .
- the outer walls 21 w deform when a pressure P that causes stretch deformation of the partitions 15 is applied, it will be clear that excessive pressure is being applied from the external appearance of the multi-channeled flat tubes 3 , and therefore such appearance can be used as one judgment made to confirm the quality of the multi-channeled flat tubes 3 and of the heat exchanger 1 that uses such multi-channeled flat tubes 3 .
- the outer walls 21 w should deform before stretch deformation occurs for the partitions 15 . Accordingly, when the maximum pressure Pmax for expanding the tubes is applied to the multi-channeled flat tubes 3 , the threshold stress ⁇ lim of the material of the multi-channeled flat tubes 3 , the stress as when stretch deformation occurs for the partitions 15 , and the maximum stress so applied to the outer walls 21 w should satisfy Equation (15) below.
- FIG. 9 shows the thickness to of the outer walls 21 w of the multi-channeled flat tubes 3 relative to the inter-partition distance Li and the partition wall thickness ti when the target value of the inner dimension Hi during tube expansion is 1.5 mm.
- the plane Cu shown in FIG. 9 shows the upper limit of the thickness to according to Condition (3)
- the plane Cl shows the lower limit of the thickness to according to Condition (1). If the multi-channeled flat tubes 3 have outer tubes 21 with a thickness to in this range, it is possible to set a suitable pressure P 3 , as shown in FIG. 8 , for expanding the tubes and therefore the tubes can be expanded with a favorable yield (lower defect rate).
- the pressure P 3 which is suited to expanding the tubes until the inner dimension Hi reaches the desired target value within a range where angle deformation occurs for the partitions 15 without stretch deformation occurring for the partitions 15 can be set based on the threshold stress ⁇ lim of the material that constructs the multi-channeled flat tubes 3 .
- the pressure P 3 for expanding the tubes should preferably be set in the range given below. 2 ⁇ a 2 - ti 2 3 ⁇ ⁇ Li ⁇ a ⁇ ⁇ ⁇ ⁇ lim ⁇ P ⁇ ⁇ 3 ⁇ ti Li ⁇ ⁇ ⁇ ⁇ lim Equation ⁇ ⁇ 16
- the form of the fins is not limited to a plate-like form and wave-like corrugated fins may be used.
- a heat exchanger that uses corrugated fins only the parts of the multi-channeled flat tubes that are attached to the headers need to be expanded and it is fundamentally unnecessary to expand the parts of the multi-channeled flat tubes that are joined to the fins.
- a method that extends the partitions by increasing the internal pressure by introducing a fluid into the multi-channeled flat tubes is more suitable than a method that expands the tubes by inserting tube expanders.
Abstract
There is provided a multi-channeled flat tube that includes a flat outer tube and a plurality of partitions that divide the inside of the outer tube into a plurality of channels. Each partition in the multi-channeled flat tube has a mountain-shaped cross-sectional form composed of two sides, each of the two sides has a thickness ti and a length a, the partitions are disposed so that a face-to-face distance between adjacent partitions along inner surfaces of the outer tube is Li, and a thickness to of the outer tube satisfies a condition below. By selecting an appropriate pressure when expanding the multi-channeled flat tube, it is possible to prevent deformation of the tube outer surface into a wavy or undulating pattern
Description
- The present invention relates to the construction of a multi-channeled flat tube used in a heat exchanger.
- A plate-fin heat exchanger equipped with a plurality of plate fins disposed in parallel at regular intervals and a plurality of tubes disposed so as to pass through such fins is known as one example of a heat exchanger used in refrigeration apparatuses, radiators, and the like. One method of manufacturing a plate-fin heat exchanger includes passing the tubes through the fins to assemble, and expanding or enlarging the tubes to join the tubes and fins together. In the expanding the tubes, a rigid rod or a tube expander is inserted into the tubes to press out and widen the tubes from the inside. By expanding the tubes, the tubes and fins are brought into contact.
- The use of multi-channeled flat tubes (multi-channel flat tubes) in heat exchangers is also known. A multi-channeled flat tube includes a plurality of partitions provided inside of the tube to divide the inside of the tube into a plurality of parallel channels.
- Japanese Laid-Open Patent Publication No. S62-19691 discloses a tube with an oval or rectangular cross-section. By expanding the surface of the tube bridging between pairs of joints, the tube surface is pressed onto cooling fins. When the tube (wall of tube) expands outward, the joints deform from their original “mountain” shapes (chevron shapes) to flat shapes, thereby preventing the wall of the tube from contracting or shrinking to their original positions.
- One aspect of the present invention is a multi-channeled flat tube including: a flat outer tube; and a plurality of partitions that divide an inside of the outer tube into a plurality of channels. Each of the plurality of partitions has a chevron (mountain-shaped) cross-sectional form composed of two sides. Each of the two sides has a thickness ti and a length a. The plurality of partitions are disposed so that a face-to-face distance between adjacent partitions of the plurality of partitions along inner surfaces of the outer tube is Li. In addition, a thickness to of the outer tube satisfies Condition (1) below
- One method of expanding tube is inserting tube expanders into channels of a multi-channeled flat tube. Aside from this method, research has been conducted into introducing a fluid into a multi-channeled flat tube to raise the internal pressure and thereby extend the partitions. Regardless of whether a method that raises the internal pressure of the tube (hereinafter referred to as “pressurized tube expansion”) or expansion using tube expanders is carried out, it is not preferable for the outer tubes located between adjacent partitions (hereinafter referred to as “outer walls”) to expand outward so that the tube outer surface deforms into a wavy or undulating form. This would reduce the contact surface area between the tube outer surface and the fins and reduce the heat transfer performance. However, if tube expansion is stopped before the partitions have extended to reach the desired size, the desired performance cannot be obtained.
- When examining how partitions that are bent into “mountain” shapes (chevron shapes, defined here as the shape of the Japanese hiragana character “Ku” (equivalent to a V shape)) become extended, the tensile stress that acts from both ends of each partition first causes the partition to deform so that the angle between both sides that construct the mountain shape (the V shape) opens up (i.e., the angle increases). After this, once the angle between the two sides has reached a certain magnitude, deformation of the partition that further increases the angle (i.e., deformation that changes the inclination of the partition, “angle deformation”) largely ceases and the inclination of the partition stops changing (i.e., the partition becomes straightened out). Hereafter, the tensile stress that acts from both ends of the partition causes deformation (hereinafter, “stretch deformation”) that reduces the thickness of the partition. The amount of stress that changes the inclination of a partition differs to the amount of stress that causes stretch deformation of the partition and makes the partition thinner, with less stress being required to change the inclination of the partition.
- With a multi-channeled flat tube with an outer tube whose thickness satisfies Condition (1) given above, the outer walls at parts of the outer tube between partitions will not deform in a range of pressure that is high enough to change the inclination of the partitions. Accordingly, a multi-channeled flat tube that satisfies Condition (1) described above can prevent deformation in the outer walls until the partitions have become straightened out. This means that by using an internal pressure in a range where there is deformation in the inclination of the partitions, the multi-channeled flat tube can be expanded in a state where deformation in the tube outer surface into a wavy or undulating state is prevented.
- The amount of deformation in the inclination of the partitions varies due to the influence of tolerances for the multi-channeled flat tube and fluctuations in the applied pressure. This means that the tube should preferably be expanded with a maximum pressure (internal pressure) in the range where deformation occurs in the inclination of the partitions, or a higher pressure. By expanding the tube with such pressure, it is possible to expand a tube until a state where the inclined partitions become substantially straightened out. Accordingly, during expansion, it is possible to expand the multi-channeled flat tube to a desired state without having to carry out control of the pressure varying step-by-step. If the thickness to of the outer tube is small so that the thickness to of the outer tube is outside the range of Condition (1), there is the possibility of deformation occurring in the outer tube before the partitions have become straightened out. Accordingly, pressure control during tube expansion becomes difficult.
- Another aspect of this invention is a heat exchanger that includes: a plurality of multi-channeled flat tubes that satisfy Condition (1); and a plurality of fins that are attached to the multi-channeled flat tubes. It is preferable that the plurality of multi-channeled flat tubes pass through the plurality of fins. As described earlier, with a multi-channeled flat tube that satisfies Condition (1), regardless of whether pressurized tube expansion is carried out using a fluid or whether the tube is expanded using tube expanders, it will be possible to extend the partitions while suppressing deformation in the outer walls. This means that it is possible to raise the contact efficiency after tube expansion between the plurality of multi-channeled flat tubes and the plate fins through which the tubes pass and to which the tubes are attached. Accordingly, it is possible to raise the heat transfer efficiency of the heat exchanger. In particular, when using pressurized tube expansion using a fluid, it is not necessary to insert a tube expander, which makes this method suited to expanding all of the narrow channels of the multi-channeled flat tubes substantially uniformly.
- One of other aspects of the present invention is a multi-channeled flat tube where in addition to Condition (1) above, the thickness to of the outer tube also satisfies Condition (2) below
- Here, in terms of making products smaller and lighter, it would not be economic to increase the thickness of the outer tube of a multi-channeled flat tube that includes a plurality of partitions to the thickness of an outer tube required for a flat tube not equipped with partitions. One merit of using multi-channeled flat tubes is that since the flat tubes can be made sufficiently strong by providing partitions inside the tube, it is possible to reduce the thickness of the outer walls or outer tube.
- Further one of other aspects of the present invention is a multi-channeled flat tube where in addition to Condition (1) above, the thickness to of the outer tube also satisfies Condition (3) below
- A pressure that is equal to or greater than the pressure used during tube expansion is not a normal operating pressure of a multi-channeled flat tube. If such pressure were applied during normal operation, there would be the possibility of further deformation in the multi-channeled flat tube since this is not how multi-channeled flat tubes are designed. Accordingly, the pressure used during tube expansion is an upper limit of the withstand pressure conditions for normal operation or even higher. Also, the pressure used during tube expansion is set up to at a pressure whereby the partitions become straightened out and is not set at a pressure whereby stretch deformation of partitions, which makes the partitions thinner, commences. This means it is economical to set the thickness of the outer tubes so that the outer walls deform at a pressure where stretch deformation, which makes the partitions thinner, commences. The heat transfer efficiency also increasing when thin outer tubes are used.
- In addition, with multi-channeled flat tubes that satisfy Condition (3), if excessive internal pressure that would cause stretch deformation of the partitions is applied during pressurized tube expansion, there is the possibility of the outer walls also expanding, resulting in the tube outer surfaces deforming. Accordingly, the state of the tube outer surfaces can also serve as one factor used when checking the pressure during tube expansion.
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FIG. 1 schematically shows a heat exchanger. -
FIG. 2 shows a state where multi-channeled flat tubes and fins of the heat exchanger shown inFIG. 1 have been joined together. -
FIG. 3 (a) shows a cross section in a length direction of the multi-channeled flat tubes before tube expansion andFIG. 3 (b) shows a cross section of one of the multi-channeled flat tubes in a minor axis direction. -
FIG. 4 (a) shows a cross section in the length direction of the multi-channeled flat tubes after tube expansion,FIG. 4 (b) shows a cross section in the minor axis direction of an end part of one of the multi-channeled flat tubes, andFIG. 4 (c) shows a cross section in the minor axis direction of another part of such multi-channeled flat tube. -
FIG. 5 (a) shows “angle deformation” of partitions andFIG. 5 (b) shows “stretch deformation” of the partitions. -
FIG. 6 shows an enlargement of a cross section of a multi-channeled flat tube. -
FIG. 7 shows changes in the inner diameter of a multi-channeled flat tube when the internal pressure has been raised. -
FIG. 8 shows how fluctuations occur in the amount by which the multi-channeled flat tubes expand due to tolerances and the like. -
FIG. 9 shows examples of an upper limit and a lower limit for the thickness of the outer tube of a multi-channeled flat tube. -
FIG. 1 schematically shows a heat exchanger that uses multi-channeled flat tubes.FIG. 2 is a perspective view showing an enlargement of a state where the multi-channeled flat tubes have been expanded. Theheat exchanger 1 is a plate fin-type heat exchanger. Theheat exchanger 1 has a plurality of plate-like fins 2 disposed in parallel at regular intervals and a plurality of multi-channeledflat tubes 3 that are disposed in parallel and are joined to thefins 2 in a state where the multi-channeledflat tubes 3 pass through thefins 2. Each multi-channeled flat tube (flat multi-channeled tube, multi-channel flat tube) 3 is constructed so that the inside of a flatouter tube 21 is divided into a plurality ofparallel channels 14 by a plurality ofpartitions 15.End parts 4 at both ends of the multi-channeledflat tubes 3 are connected to joiningholes 19 formed inside walls 9 ofheaders heat exchanger 1. A heat transfer medium (internal fluid) introduced from asupply outlet 11 of theheader 6 passes through thechannels 14 of the multi-channeledflat tubes 3 and is guided or led to anoutput outlet 12 of theheader 7. When an external fluid B such as air passes over theheat exchanger 1, the external fluid B contacts the multi-channeledflat tubes 3 and thefins 2, heat exchange occurs between the heat transfer medium and the external fluid so that the heat transfer medium and/or the external fluid is cooled or heated. -
FIG. 3 (a) shows the multi-channeledflat tubes 3 before the tubes have been expanded. When manufacturing theheat exchanger 1, the multi-channeledflat tubes 3 are inserted into burringholes 18 provided in advance in thefins 2 to provisionally assemble thefins 2 and the multi-channeledflat tubes 3 together. -
FIG. 3 (b) shows an enlargement of the cross-section of a multi-channeledflat tube 3. Theouter tube 21 of the multi-channeledflat tube 3 includesouter walls 21 w that oppose each other at the top and bottom of the multi-channeledflat tube 3. The multi-channeledflat tube 3 is a flat tube molded so that theouter wall 21 w that forms the upper wall or top wall of theouter tube 21 and theouter wall 21 w that forms the lower wall or bottom wall are substantially parallel. A plurality ofpartitions 15 that connect the upper and lowerouter walls 21 w and respectively have cross-section bent like “mountain”-shaped (V-shaped) to the length direction X of the cross-section of the multi-channeledflat tube 3 are provided inside each multi-channeledflat tube 3. Thesepartitions 15 divide the inside of theflat tube 3 to form the plurality ofparallel channels 14. - The
end parts 4 of the multi-channeledflat tubes 3 that have been assembled so as to pass through thefins 2 are inserted into the joiningholes 19 provided in theheaders end parts 4 are joined to theheaders parallel flow channels 14 of the individualflat tubes 3 are connected via theheaders - FIGS. 4(a), 4(b), and 4(c) are cross-sectional views showing the state of the multi-channeled
flat tubes 3 after pressurized tube expansion. FIGS. 5(a) and 5(b) show how thepartitions 15 of the multi-channeledflat tubes 3 are straightened. A compressed fluid can be supplied via theheaders flat tubes 3. The compressed fluid raises the internal pressure of theparallel channels 14 and can expand multi-channeled flat tubes 3 (pressurized tube expansion). By expanding thetubes 3, as shown inFIG. 4 (a), the multi-channeledflat tubes 3 and therespective fins 2 are tightly joined. With theheat exchanger 1, theheaders end parts 4 of the multi-channeledflat tubes 3 in advance. This means that as shown inFIG. 4 (b), thebent partitions 15 are not straightened at theend parts 4 of thetubes 3. At other parts, including the parts where the multi-channeledflat tubes 3 pass through thefins 2, thebent partitions 15 are straightened as shown inFIG. 4 (c). - Each of the
partitions 15 of the multi-channeledflat tubes 3 that is used in theheat exchanger 1 has a thickness ti and each side out of the two sides forming the mountain shape has a length a. The gap (face-to-face distance (distance between surfaces)) between the partitions (adjacent partitions) 15 along the inner surfaces of theouter walls 21 w of the flatouter tube 21 is the distance Li. The thickness to of theouter tube 21 satisfies Equation (1) below. - The expansion of the multi-channeled
flat tube 3 withpartitions 15 which in cross-section are bent into mountain shapes (V-shapes) with twosides 27 of the length a and meeting with an angle 2θ was investigated. As shown inFIG. 5 (a), when the internal pressure is raised, the force that acts on thewalls 21 w of theouter tube 21 pulls thepartitions 15 that are bent in mountain shapes outward, thereby causing thepartitions 15 to deform so that the inclination angle (half angle) θ of eachside 27 approaches 90°. This deformation changes the inclination of the partitions and is referred to as “angle deformation”. The angle deformation is assumed to be deformation that ends or is ceased where apartition 15 becomes straightened state. The straighten or straitened state of this specification is the state that a corner (base) 26 where thepartition 15 is connected to thewall 21 w of theouter tube 21 and thepeak point 25 where the twosides 27 that form the mountain shape meet become offset substantially by only the thickness ti of thepartition 15. This state is shown inFIG. 6 . - As shown in
FIG. 5 (b), deformation that occurs thereafter is assumed to be deformation (referred to as “stretch deformation”) caused by stretching that reduces the thickness of thepartitions 15. Accordingly, depending on the applied internal pressure, the mechanism by which thepartitions 15 deform changes. This means that by applying pressure in a range from a pressure where angle deformation ends to a pressure where stretch deformation commences, it is possible to stably cause thepartitions 15 to deform until thepartitions 15 become substantially straight. -
FIG. 7 shows the result of measuring the relationship between the inner height of the tube (the inner diameter or inner dimension in the minor axis Y) Hi and the internal pressure (the applied pressure). The solid line A1 shown inFIG. 7 shows measured values for the case where the plate thickness ti of thepartitions 15 is set at 0.19 mm and the dot-dash line A2 shows values produced by calculating the tangent (tan) from the measured values of the angle θ by which thepartitions 15 are bent. As can be understood from the solid line A1, when the thickness ti of thepartitions 15 is 0.19 mm, the tube height Hi suddenly increases from a point where the internal pressure exceeds 2 MPa or thereabouts, showing that angle deformation is occurring for thepartitions 15. When the internal pressure is around 7.2 MPa, the increasing of amount of deformation in thepartitions 15 starts to fall and when the internal pressure is around 7.5 MPa, thepartitions 15 substantially stop deforming. By applying a pressure of over 7.5 MPa or so, thepartitions 15 become the straightened state, and even if the pressure is increased further, deformation of thepartitions 15 does not proceed. It is therefore supposed that angle deformation of thepartitions 15 has ended. - By comparing the calculated values shown by the dot-dash line A2 in
FIG. 7 and the measured values shown by the solid line A1, it can be seen that angle deformation of the tubes has substantially ended at the point “tan θ=Hi/(2 ti)”. As described earlier, when the peak points 25 of thepartitions 15 are positioned so as to be displaced from thebase parts 26 by only the thickness ti of thepartitions 15, it is assumed that thepartitions 15 have been the straightened state and angle deformation has ended. When judging from the measured values A1, angle deformation ends at an internal pressure of around 7 to 8 MPa. Accordingly, if the internal pressure used to expand the tubes is set at around 7 to 8 MPa or higher, it will be possible thepartitions 15 become the straightened state. - As shown in
FIG. 8 , there are tolerances for dimensions such as the thickness ti of thepartitions 15. Due to such tolerances, the relationship between the amount of deformation (i.e., the height of the tube) Hi and the internal pressure P changes. If the target value of the height Hi during tube expansion is set at a position like H2 inFIG. 8 where angle deformation has not ended, it will be necessary to control the internal pressure P in the individual tubes so that the height H1 becomes the target value H2. This kind of tube expansion operation is not economical to carry out and since there is a fall in the accuracy of the dimensions after expansion, the manufacturing yield of a heat exchanger that uses multi-channeled flat tubes also falls. On the other hand, if the target value of the height Hi during tube expansion is set at a position like H3 inFIG. 8 where angle deformation has ended, it will be possible to set the internal pressure during tube expansion at a value such as P3 inFIG. 8 , which can be the pressure at which angle deformation ends or an even higher pressure. This means that regardless of any differences between individual tubes, it will be possible to expand the tubes to the same height Hi by expanding the tubes with the same pressure. Since the accuracy of the dimensions of thetubes 3 after expansion is stabilized, the yield and quality of theheat exchanger 1 that uses the multi-channeledflat tubes 3 are improved. - In this way, by expanding the multi-channeled
flat tubes 3 until thepartitions 15 are the straightened state, that is, until the target value H3 shown inFIG. 8 is reached, it is possible to expand the multi-channeledflat tubes 3 stably. The pressure required to expand the tubes in this way is the pressure P3 shown inFIG. 8 , and the thickness to of theouter walls 21 w of theouter tubes 21 is determined so that hardly any deformation is observed in the tube outer surface at such pressure P3. - The force (internal pressure) required for angle deformation of the
partitions 15 can be calculated from the force applied when thepartitions 15 become the straightened state as shown inFIG. 6 . Having no intentional deformation of at least theouter walls 21 w of theouter tubes 21 when such internal pressure is applied is one condition for the present invention. InFIG. 6 , when the length of one side of thepartitions 15 is expressed as length a, the inclination (bent angle) as angle θ, the face-to-face distance betweenadjacent partitions 15 along the inner surfaces of theouter walls 21 w of the flat outer tubes 21 (i.e., the distance between surfaces of facing partitions 15) as Li, and the height of the multi-channeled flat tubes 3 (i.e., the inner diameter or inner dimension in the minor axis direction of the flat outer tubes 21) as Hi, the stress co produced in theouter walls 21 w when the internal pressure P acts on theouter walls 21 w is as follows. First, since theouter walls 21 w can be regarded as fixed beams (beams whose both ends are fixed respectively) subjected to a uniformly distributed load of the pressure P along the inter-partition distance Li, the maximum bending moment Mmax and the section modulus Z are as shown by Equations (4) and (5). Accordingly, the maximum stress co applied to theouter walls 21 w is shown by Equation (6). - A
partition 15 is pulled upward and downward by the forces that act at thebases 26. Thebases 26 are subjected to a force (load) W (where W=applied pressure P×pressure-receiving surface length Li) due to the internal pressure P. Thepartition 15 is thought to deform due to the bending moment acting on thebases 26 and thepeak point 25 where the center of the partition and the twosides 27 are joined. Thepartition 15 can be modeled as a fixed beam (beam whose both ends are fixed) of an effective length 2 a and a thickness ti that receives a concentrated load W′ at thecenter 25 thereof. If the force W is constant, the concentrated load W′ that acts on thepartition 15 will be minimized when tan θ is maximized, and therefore calculations can proceed for the conditions where angle deformation occurs for a minimum concentrated load W′. The condition that the tan θ is maximized indicates that angle deformation has ended for thepartition 15 and thepartition 15 has been the straightened state, which means that the inclination θ can be expressed by Equation (7). Accordingly, the concentrated load W′ can be found as shown in Equation (8). - The maximum bending moment Mmax during angle deformation of the
partitions 15 is as shown in Equation (9). By using the section modulus Z in Equation (10), the maximum stress σi occurring in thepartitions 15 is as shown in Equation (11). Note that since modeling is carried out based on the cross-sectional form of a multi-channeled flat tube, stress is calculated in one dimension. - To expand the tubes according to the conditions described above, the
outer walls 21 w should not deform in a range of pressure where angle deformation occurs for thepartitions 15. Accordingly, when the minimum pressure Pmin for expanding the tubes is applied to the multi-channeledflat tubes 3, the threshold stress σlim of the material that constructs theouter walls 21 w and thepartitions 15, for example, a metal material including aluminum and copper, the maximum stress σi when angle deformation occurs for thepartitions 15, and the maximum stress σo applied to theouter walls 21 w should satisfy Equation (12) below. -
Equation 12
σo≦σlim≦σi (12) - From Equation (12), it is possible to reach Condition (1) above. Note that the length a of one
side 27 of apartition 15 is expressed as shown in Equation (13) below. - Equation 13
a=√{square root over ((Hi/2)2 +ti 2)} (13) - One merit of multi-channeled flat tubes is that the strength of the flat tubes is increased by the partitions disposed inside the tubes, and therefore the
outer walls 21 w, or in other words, theouter tubes 21 can be made thinner. Here, suppose the case of a double-channeled flat tube with twochannels 14 that is the minimum configuration of a multi-channeled flat tube. When the internal pressure P is applied, the maximum stress co produced in theouter walls 21 w is as shown by Equation (6) given earlier. For a flat tube with the same internal cross-sectional area as such double-channeled flat tube, that is, a single flat tube with the distance 2Li between walls and a tube inner dimension (i.e., height) of Hi, to achieve the same strength as the double-channeled flat tube, it would be necessary to double the thickness to of theouter walls 21 w. This means that if the thickness of theouter walls 21 w is more than double the minimum value calculated using Equation (1), one of the merits of multi-channeled flat tubes will be lost. Accordingly, the thickness to of theouter walls 21 w should preferably satisfy Condition (2). - In
FIG. 8 , if the pressure P is increased further, stretch deformation occurs for thepartitions 15, so that thepartitions 15 continue to extend while becoming thinner. In this case, it is difficult to know when thepartitions 15 will rupture or break. For this reason, it is not preferable to expand the multi-channeledflat tubes 3 using a pressure P that causes stretch deformation to commence. Also, regarding the pressure used during expanding, it is not necessary for theouter walls 21 w of theouter tubes 21 to withstand a pressure P thereby the stretch deformation commences without deforming, since such pressure is at or above the withstand pressure of the multi-channeled flat tubes for service. In addition, in view of cost and heat exchanging efficiency, the thickness to of the flatouter tubes 21 should preferably be thin. Accordingly, the thickness to of theouter tubes 21 can be such that the flatouter tubes 21 deform at a pressure that causes stretch deformation of thepartitions 15. In addition, if theouter walls 21 w deform when a pressure P that causes stretch deformation of thepartitions 15 is applied, it will be clear that excessive pressure is being applied from the external appearance of the multi-channeledflat tubes 3, and therefore such appearance can be used as one judgment made to confirm the quality of the multi-channeledflat tubes 3 and of theheat exchanger 1 that uses such multi-channeledflat tubes 3. - When stretch deformation occurs for the
partitions 15, the tensile stress as that acts on thepartitions 15 is as shown in Equation (14). - It is thought that the
outer walls 21 w should deform before stretch deformation occurs for thepartitions 15. Accordingly, when the maximum pressure Pmax for expanding the tubes is applied to the multi-channeledflat tubes 3, the threshold stress σlim of the material of the multi-channeledflat tubes 3, the stress as when stretch deformation occurs for thepartitions 15, and the maximum stress so applied to theouter walls 21 w should satisfy Equation (15) below. -
Equation 15
σs≦σlim≦σo (15) - From Equation (15), it is possible to reach Condition (3), and the thickness to of the
outer walls 21 w should more preferably satisfy this condition. -
FIG. 9 shows the thickness to of theouter walls 21 w of the multi-channeledflat tubes 3 relative to the inter-partition distance Li and the partition wall thickness ti when the target value of the inner dimension Hi during tube expansion is 1.5 mm. The plane Cu shown inFIG. 9 shows the upper limit of the thickness to according to Condition (3), and the plane Cl shows the lower limit of the thickness to according to Condition (1). If the multi-channeledflat tubes 3 haveouter tubes 21 with a thickness to in this range, it is possible to set a suitable pressure P3, as shown inFIG. 8 , for expanding the tubes and therefore the tubes can be expanded with a favorable yield (lower defect rate). In addition, it is possible to prevent deformation of theouter walls 21 w during expansion of the tubes, and therefore it is possible to achieve a high yield when manufacturing theheat exchanger 1 where the multi-channeledflat tubes 3 have a stabilized outer form and achieve a sufficient contact surface area with thefins 2, resulting in high heat exchanging efficiency. A specific example of the pressure P3 which is suited to expanding the tubes until the inner dimension Hi reaches the desired target value within a range where angle deformation occurs for thepartitions 15 without stretch deformation occurring for thepartitions 15 can be set based on the threshold stress σlim of the material that constructs the multi-channeledflat tubes 3. By referring to Equations (12) and (15), it can be understood that the pressure P3 for expanding the tubes should preferably be set in the range given below. - Note that as described above, although a procedure for manufacturing the
heat exchanger 1 that has plate-like fins 2 has been described, the form of the fins is not limited to a plate-like form and wave-like corrugated fins may be used. In a heat exchanger that uses corrugated fins, only the parts of the multi-channeled flat tubes that are attached to the headers need to be expanded and it is fundamentally unnecessary to expand the parts of the multi-channeled flat tubes that are joined to the fins. However, it is possible to expand the multi-channeled flat tubes after the fins have been joined to increase the contact surface area. When the insides of the multi-channeled flat tubes are partitioned into narrow channels by a plurality of partitions, since the individual channels have small cross-sectional areas, a method that extends the partitions by increasing the internal pressure by introducing a fluid into the multi-channeled flat tubes is more suitable than a method that expands the tubes by inserting tube expanders. However, by using multi-channeled flat tubes that satisfy Condition (1) given earlier, regardless of whether a method that raises the internal pressure (sometimes referred to as “pressurized tube expansion”) or an expansion method that uses tube expanders is used, it will be possible to prevent the outer walls of the outer tubes, from deforming due to the internal pressure caused by the fluid or tube expanders, which would result in the outer surfaces of the outer tubes becoming wavy or undulating, before the partitions have extended to reach a desired size. That is, by using pressurized tube expansion or the like, when the multi-channeled flat tubes are expanded by internal pressure, it is possible to extend the partitions while suppressing deformation of the tube outer walls, and therefore the outer form of the tubes can be controlled until the multi-channeled flat tubes reach the desired size. By preventing the tube outer walls from deforming into an unintended shape, it is possible to achieve a sufficient contact surface area between the tube outer surfaces and the fins, thereby improving the heat transfer performance. Accordingly, it is possible to provide a heat exchanger that has high heat exchanging efficiency and high reliability.
Claims (4)
1. A multi-channeled flat tube comprising:
a flat outer tube; and
a plurality of partitions that divide an inside of the outer tube into a plurality of channels,
wherein each of the plurality of partitions has a mountain-shaped cross-sectional form composed of two sides, each of the two sides has a thickness ti and a length a, the plurality of partitions are disposed so that a face-to-face distance between adjacent partitions of the plurality of partitions along inner surfaces of the outer tube is Li, and a thickness to of the outer tube satisfies a condition below
2. The multi-channeled flat tube according to claim 1 , wherein the thickness to of the outer tube also satisfies a condition below
3. The multi-channeled flat tube according to claim 1 , wherein the thickness to of the outer tube also satisfies a condition below
4. A heat exchanger comprising:
a plurality of multi-channeled flat tubes according to claim 1; and
a plurality of fins that are attached to the plurality of multi-channeled flat tubes and the plurality of multi-channeled flat tubes passing through the plurality of fins.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2004252671 | 2004-08-31 | ||
JP2004-252671 | 2004-08-31 | ||
PCT/JP2005/015940 WO2006025465A1 (en) | 2004-08-31 | 2005-08-31 | Flat perforated pipe and heat exchanger |
Publications (1)
Publication Number | Publication Date |
---|---|
US20080087408A1 true US20080087408A1 (en) | 2008-04-17 |
Family
ID=36000114
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US11/660,918 Abandoned US20080087408A1 (en) | 2004-08-31 | 2005-08-31 | Multi -Channeled Flat Tube And Heat Exchanger |
Country Status (5)
Country | Link |
---|---|
US (1) | US20080087408A1 (en) |
EP (1) | EP1795848A1 (en) |
JP (1) | JP4664918B2 (en) |
CN (1) | CN100516755C (en) |
WO (1) | WO2006025465A1 (en) |
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US20100234824A1 (en) * | 2009-03-16 | 2010-09-16 | Roche Diagnostics International Ag | Bubble trap systems for infusion pump devices |
US20110000254A1 (en) * | 2008-04-24 | 2011-01-06 | Mitsubishi Electric Corporation | Heat exchanger and air conditioner using the same |
US20110030932A1 (en) * | 2009-08-07 | 2011-02-10 | Johnson Controls Technology Company | Multichannel heat exchanger fins |
US20120037346A1 (en) * | 2009-04-20 | 2012-02-16 | Kim Young Mo | Heat exchanger |
US20220250136A1 (en) * | 2020-12-16 | 2022-08-11 | Mahle International Gmbh | Method for producing a heat exchanger |
CN116379826A (en) * | 2023-06-02 | 2023-07-04 | 广东美的暖通设备有限公司 | Heat exchange assembly, assembling method thereof, micro-channel heat exchanger and heating ventilation equipment |
US20230314093A1 (en) * | 2022-03-31 | 2023-10-05 | Deere & Company | Heat exchanger |
CN116379826B (en) * | 2023-06-02 | 2024-04-16 | 广东美的暖通设备有限公司 | Heat exchange assembly, assembling method thereof, micro-channel heat exchanger and heating ventilation equipment |
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JP4659779B2 (en) * | 2007-03-23 | 2011-03-30 | 三菱電機株式会社 | Heat exchanger and air conditioner equipped with the heat exchanger |
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US20050061494A1 (en) * | 2001-11-09 | 2005-03-24 | Masanori Tsuji | Heat exchanger and method of manufacturing the same |
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JPS58164995A (en) * | 1982-03-25 | 1983-09-29 | Kobe Steel Ltd | Heat exchanger and manufacture thereof |
JPS61268985A (en) * | 1985-05-24 | 1986-11-28 | Matsushita Refrig Co | Heat exchanger |
JPS6219691A (en) * | 1985-07-19 | 1987-01-28 | ペドロ・マンチン・ベルテイ | Nonshrinkable expansible conduit for heat exchanger or similar article |
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JPH01127175A (en) * | 1987-11-11 | 1989-05-19 | Hitachi Ltd | Structure for fitting pipe to pipe plate |
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- 2005-08-31 CN CNB2005800291190A patent/CN100516755C/en not_active Expired - Fee Related
- 2005-08-31 EP EP05781541A patent/EP1795848A1/en not_active Withdrawn
- 2005-08-31 US US11/660,918 patent/US20080087408A1/en not_active Abandoned
- 2005-08-31 WO PCT/JP2005/015940 patent/WO2006025465A1/en active Application Filing
- 2005-08-31 JP JP2006532761A patent/JP4664918B2/en not_active Expired - Fee Related
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US20050061494A1 (en) * | 2001-11-09 | 2005-03-24 | Masanori Tsuji | Heat exchanger and method of manufacturing the same |
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US20230314093A1 (en) * | 2022-03-31 | 2023-10-05 | Deere & Company | Heat exchanger |
CN116379826A (en) * | 2023-06-02 | 2023-07-04 | 广东美的暖通设备有限公司 | Heat exchange assembly, assembling method thereof, micro-channel heat exchanger and heating ventilation equipment |
CN116379826B (en) * | 2023-06-02 | 2024-04-16 | 广东美的暖通设备有限公司 | Heat exchange assembly, assembling method thereof, micro-channel heat exchanger and heating ventilation equipment |
Also Published As
Publication number | Publication date |
---|---|
CN100516755C (en) | 2009-07-22 |
EP1795848A1 (en) | 2007-06-13 |
JP4664918B2 (en) | 2011-04-06 |
WO2006025465A1 (en) | 2006-03-09 |
JPWO2006025465A1 (en) | 2008-05-08 |
CN101010552A (en) | 2007-08-01 |
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