CN102667391B - Heat-exchangers of the plate type and heat pump assembly - Google Patents
Heat-exchangers of the plate type and heat pump assembly Download PDFInfo
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- CN102667391B CN102667391B CN201080052178.0A CN201080052178A CN102667391B CN 102667391 B CN102667391 B CN 102667391B CN 201080052178 A CN201080052178 A CN 201080052178A CN 102667391 B CN102667391 B CN 102667391B
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Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F3/00—Plate-like or laminated elements; Assemblies of plate-like or laminated elements
- F28F3/02—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations
- F28F3/04—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations the means being integral with the element
- F28F3/042—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations the means being integral with the element in the form of local deformations of the element
- F28F3/046—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations the means being integral with the element in the form of local deformations of the element the deformations being linear, e.g. corrugations
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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
- F28D9/00—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D9/0031—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other
- F28D9/0043—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other the plates having openings therein for circulation of at least one heat-exchange medium from one conduit to another
- F28D9/005—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other the plates having openings therein for circulation of at least one heat-exchange medium from one conduit to another the plates having openings therein for both heat-exchange media
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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
- F28F2275/00—Fastening; Joining
- F28F2275/04—Fastening; Joining by brazing
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- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The present invention by forming easily, provide the pressure loss of fluid few, heat-exchangers of the plate type that thermal conversion efficiency is good.Adjacent upper-side heat transfer plate (2), lower-side heat transfer plate (3) are carried out the processing of the waveform conjugated at stacked direction.This plate is each other in the occasion of watching from stacked direction, represent the wave base portion of upper-side heat transfer plate (2) and imaginary many bottoms crest line (21) extended in the direction different from the direction on long limit represent together the wave crest portion of lower-side heat transfer plate (3) and imaginary many top crest lines (22) extended in the direction different with the direction on long limit are intersected and form intersection point, the wave base portion represented with each bottom crest line contacts at intersection point with the wave crest portion represented with each top crest line and forms tie point.Upper-side heat transfer plate (2) and lower-side heat transfer plate (3) with in the intersection point be present on bottom crest line (21), closest to being formed in the position roughly consistent with the edge, periphery along long limit along the abutment (11) that the intersection point (23) of the end of the edge, periphery (2-3) on long limit is corresponding.
Description
Technical field
The present invention relates to heat-exchangers of the plate type.
Background technology
Heat-exchangers of the plate type in the past has the heat-exchangers of the plate type (for example, referring to patent document 1) arranging multiple ridges shape rib at the length direction of plate, support upper and lower plates.In addition, there is the heat-exchangers of the plate type (for example, referring to patent document 2) alignd in the summit in the V-arrangement ripple portion of upper and lower plates.
Patent document 1: Japanese Unexamined Patent Publication 10-103888 publication
Patent document 2: Japanese Unexamined Patent Publication 2002-107074 publication
Summary of the invention
The problem that invention will solve
In the past, there is following problem in heat-exchangers of the plate type: the first, increases the pressure loss that flow velocity brings increase to improve the heat-transfer effect of fluid; The second, the pressure loss increase cause sediment, grit blocking.In order to address these problems, although the solution of patent document 1 can be taked, because fluid only flows in the stream defined by the ridge shape rib of long axis direction, so fluid is deteriorated towards the expansion of short-axis direction.In addition, as the general problem of heat-exchangers of the plate type, as by patent document 2, at upper and lower plates, alignd in the summit of V-arrangement ripple, then the end existed due to the ripple of outer circumferential side becomes not line up and makes the soldering area at upper and lower plates junction surface become large, stream narrows, and the pressure loss increases such problem.
The object of the invention is to provide by forming easily the heat-exchangers of the plate type that a kind of pressure loss of fluid is few, thermal conversion efficiency is good.
For the means of dealing with problems
Heat-exchangers of the plate type of the present invention by long limit each other, minor face each other, the mode that overlaps each other of edge, periphery is stacked multiplely has long limit, minor face, formation to the plate of the rectangle of the edge, periphery in the space that fluid seals,
Each plate is carried out the processing of the waveform conjugated at stacked direction,
Adjacent plate is each other in the occasion of watching from stacked direction, represent the wave base portion of the plate of a side and imaginary many bottom crest lines extended in the direction different from the direction on aforementioned long limit with represent the wave crest portion of plate of the opposing party and imaginary many top crest lines extended in the direction different with the direction on aforementioned long limit intersect and form intersection point
The wave base portion represented by each afore-mentioned bottom crest line contacts at aforementioned intersection point with the wave crest portion represented by each aforementioned top crest line and forms contact site;
It is characterized in that:
Aforementioned adjacent plate each other with in the aforementioned intersection point be present on an afore-mentioned bottom crest line, closest to along aforementioned contact portion corresponding to the aforementioned intersection point of the end of the edge, aforementioned periphery on aforementioned long limit, the direction that the direction extended corresponding to afore-mentioned bottom crest line and aforementioned top crest line extend, is formed in the position of the distance that have left regulation from the edge, aforementioned periphery along aforementioned long limit at short side direction; And
With in the aforementioned intersection point be present on an afore-mentioned bottom crest line, the closest aforementioned contact portion corresponding along the aforementioned intersection point of the end of the edge, aforementioned periphery on aforementioned long limit, be in more than 60 degree relative to the direction on aforementioned long limit and the occasion of the scope of less than 70 degree in the direction of afore-mentioned bottom crest line, be formed in more than 3mm and the scope of below 4.5mm from the edge, aforementioned periphery along aforementioned long limit towards aforementioned short side direction.
The effect of invention
According to heat-exchangers of the plate type of the present invention, the pressure loss of fluid can be reduced, in addition, can rate of heat exchange be improved.In addition, by the minimizing of the pressure loss and the raising of the thermal efficiency, heat-exchangers of the plate type miniaturization (economizing volume) can be made.In addition, along with the raising of the thermal efficiency, power consumption reduces, and can reduce CO
2discharge rate.
Accompanying drawing explanation
Fig. 1 is the figure of the heat-exchangers of the plate type 100 representing embodiment 1.
Fig. 2 is the figure of the plate adjoined each other representing embodiment 1.
Fig. 3 is the figure of the size b representing embodiment 2.
Fig. 4 is the figure of the region c that embodiment 3 is described.
Fig. 5 is the figure of the region d that embodiment 4 is described.
Fig. 6 is the figure of the state of the crest line of ripple that shortens every 1 ripple that embodiment 5 is described.
Fig. 7 is the figure of the gap size e that embodiment 6 is described.
Fig. 8 is the figure in each cross section of the plate represented in heat-exchangers of the plate type 100.
Detailed description of the invention
Embodiment 1.
Fig. 1 is the figure of the heat-exchangers of the plate type 100 representing embodiment 1.
(1) Fig. 1 (a) is the side view of heat-exchangers of the plate type 100.
(2) Fig. 1 (b) is front view (X is to looking).The arrow X-direction of Fig. 1 (a) is the stacked direction of plate.The reinforcement side plate 1 of Fig. 1 (b) is positioned at outermost, possesses stream socket pipe.Reinforcement side plate 1 possesses inflow pipe 5, the inflow pipe 6 of second fluid, the effuser 7 of first fluid, the effuser 8 of second fluid of first fluid.
(3) Fig. 1 (c) represents the upper-side heat transfer plate 2 of the stream forming first fluid and second fluid.(4) Fig. 1 (d) represents the lower-side heat transfer plate 3 of placing, forming the stream of first fluid and second fluid by the mode faced by waveform and upper-side heat transfer plate 2.By making upper-side heat transfer plate 2 and lower-side heat transfer plate 3 alternately arrange, alternately repeat the stream forming first fluid and second fluid.
(5) Fig. 1 (e) expression is positioned at outermost reinforcement side plate 4.
(6) Fig. 1 (f) is the figure representing the state that upper-side heat transfer plate 2 has been overlapped with lower-side heat transfer plate 3.Fig. 1 (f) is under the state by both overlaps, and pressing the occasion of X-direction viewing of Fig. 1 (a), the shape of the upper-side heat transfer plate 2 that reality indicated by the solid line can be seen, represent the waveform of in fact invisible lower-side heat transfer plate 3 with dotted line.The enlarged drawing of the scope Y represented with dashed line is Fig. 2.
And, in fig. 8, illustrate section AA ' (Fig. 1 (c)), cross section BB ' ~ cross section DD ' (Fig. 2).
(form and illustrate)
As shown in Figure 1, in heat-exchangers of the plate type 100, multiple there is minor face (the minor face 2-1 of upper-side heat transfer plate 2, the minor face 3-1 of lower-side heat transfer plate 3), long limit (the long limit 2-2 of upper-side heat transfer plate 2, the long limit 3-2 of lower-side heat transfer plate 3) and formed to the rectangular slab of the edge, periphery (edge, the periphery 2-3 of upper-side heat transfer plate 2, edge, the periphery 3-3 of lower-side heat transfer plate 3) in the space that fluid seals by long limit each other, minor face each other, the mode that overlaps each other of edge, periphery is stacked.Each plate is embodied in the processing of the waveform that stacked direction (X-direction) conjugates.
Fig. 2 is the front view of heat transfer plate.Fig. 2 is the enlarged drawing of the scope Y of Fig. 1 (f).In fig. 2, the end 10 in the end 9 of the valley (bottom) of the ripple of upper-side heat transfer plate 2 and the mountain portion of lower side panel, formed from the 2-3 of edge, periphery short-axis direction (Z-direction) be in the shortest size, the abutment 11(contact site of upper and lower plates (upper-side heat transfer plate 2 and lower-side heat transfer plate 3)).Like this, size a(can be shortened in figure from edge, periphery 12 towards the size of short-axis direction (Z-direction)) be feature.Size a is the size from edge, periphery 2-3 towards short-axis direction (Z-direction).
And, the abutment occurred at first in the occasion that short-axis direction has advanced from edge, periphery 2-3 is referred at the abutment that short-axis direction (Z-direction) is in the shortest size.
More specifically be described below.In fig. 2, the solid line on the surface of upper-side heat transfer plate 2 represents waveform, and dotted line represents the waveform of the lower-side heat transfer plate 3 of the downside being in upper-side heat transfer plate 2.The scope 32 surrounded with interrupted wire frame represents the cross sectional shape of the ripple of upper-side heat transfer plate 2.Dotted line x1, y1, z1 represent mountain, paddy, mountain successively.The scope 33 surrounded with interrupted wire frame represents the cross sectional shape of the ripple of lower-side heat transfer plate 3.Dotted line x2, y2, z2 represent paddy, mountain, paddy successively.In Fig. 2 (stacked direction to looking), as the plate adjoined each other upper-side heat transfer plate 2 and lower-side heat transfer plate 3, the wave base portion that represents upper-side heat transfer plate 2 and imaginary many bottom crest lines 21 extended in the direction different from the direction of long limit 2-2 etc. with represent the wave crest portion of lower-side heat transfer plate 3 and imaginary many top crest lines 22 etc. extended in the direction different with the direction of long limit 3-2 intersect, formation intersection point 23.So the wave base portion represented by each bottom crest line engages (contact) with the wave crest portion represented by each top crest line at intersection point 23 and forms abutment (contact site).In this is formed, upper-side heat transfer plate 2 and lower-side heat transfer plate 3 with in the intersection point be present on a certain root bottom part crest line such as bottom crest line 21, closest to along abutment 11 corresponding to the intersection point 23 of the end of edge, the periphery 2-3 of long limit 2-2, be formed in the position roughly consistent with edge, the periphery 2-3 along long limit 2-2.
Fig. 3, relative to Fig. 2, represents the occasion that the size b corresponding with size a is longer than size a.Namely, in the occasion of Fig. 3, with in the intersection point be present on the crest line 21 of bottom, the closest abutment 11 corresponding along the intersection point 23 of the end of edge, the periphery 2-3 of long limit 2-2, formed with leaving size b from edge, the periphery 2-3 position that (Z-direction) have left to the inside along long limit 2-2.In the occasion that this size b is short as the size a of Fig. 2, stream broadening, for this reason, flow velocity when flowing through same flow declines, and the pressure loss reduces.In addition, in the occasion that size a is short, can reduce the hold-up of solder, for this reason, effective heat transfer area increases, and heat exchange performance improves.By shortening size a in this wise, can suppress pressure loss increase, and can heat exchange performance be improved.Therefore, the necessary plate number that can make the heat-exchangers of the plate type of the necessary ability relative to air conditioner is Min., and, can suppress the delay of the foreign matters such as the refrigerator oil in heat-exchangers of the plate type, grit, so, can provide and inhibit cost and the high heat-exchangers of the plate type of reliability.If heat-exchangers of the plate type 100, then the fluid that the pressure loss that hydrocarbon, low GWP cold-producing medium also can be used such is large.
Following effect can be obtained by the heat-exchangers of the plate type 100 of embodiment 1.
(1) crushing: heat-exchangers of the plate type 100 can make the pressure loss of fluid reduce effectively.The edge, periphery be formed as relative to the long axis direction of plate is in the configuration of the abutment of the upper and lower plates of the shortest size ripple roughly consistent with the edge, periphery of long axis direction at short-axis direction.Like this, be at short-axis direction relative to edge, periphery the abutment of the upper and lower plates of the shortest size distance (size a) shortens, so, the hold-up of the solder that circumference is outside formed can be reduced, expand stream, for this reason, can the pressure loss be reduced.
(2) efficiency: in addition, because stream expands, so heat transfer effective area also increases, and can provide the board-like heat exchanger with excellent heat exchanger effectiveness.
(3) miniaturized: to improve the heat transfer between plate in this wise, decrease the sheet number that the heat-exchangers of the plate type of the pressure loss can reduce stacked plate, the manufacturing cost such as fee of material, processing charges can be cut down significantly.
(4) CO
2discharge and reduce: according to the air-conditioning equipment being loaded with this heat-exchangers of the plate type, cheap, and also power consumption amount is inhibited, CO
2discharge rate also can reduce.In addition, the minimizing of the pressure loss can suppress the refrigerator oil, sludge, grit blocking etc. be detained in a heat exchanger, and its reliability also improves.
In above embodiment 1, heat-exchangers of the plate type is folded by the multi-disc flaggy of the via hole being provided with the gateway becoming fluid in corner and forms, in this heat-exchangers of the plate type, the edge, periphery illustrating by the long axis direction relative to plate is in the abutment of the upper and lower plates of the shortest size mode roughly consistent with the edge, periphery of long axis direction and configures the heat-exchangers of the plate type that rolling land engages at short-axis direction.
Embodiment 2.
In above embodiment 1, by making the terminal of crest line bottom the end 9(in the trough portion of upper-side heat transfer plate 2) with the terminal of 10(top, the end crest line in the mountain portion of lower-side heat transfer plate 3) consistent, make edge, the periphery 2-3 of plate be minimum with the distance being in the abutment 11 of the upper and lower plates of the shortest size at short-axis direction (Z-direction).That is, make this abutment 11 roughly consistent with edge, periphery 2-3.Like this, the pressure loss is reduced.Below, in embodiment 2, edge, periphery (edge, periphery along long limit) and the abutment being in the upper and lower plates of the shortest size at short-axis direction (Z-direction) of the long axis direction of display plate have the occasion of specific distance (specific dimensions b described later).
Be described referring again to the Fig. 3 employed in embodiment 1.In embodiment 1, describe the effective this point of the minimizing of occasion to the pressure loss that size b is short to the degree of size a.In present embodiment 2, even if illustrate that size b does not have the little degree to size a, if place within the limits prescribed, then stream obtain guaranteeing, suitable occasion.
If the edge, periphery of plate is too small with the size b being in the abutment 11 of the upper and lower plates of the shortest size at short-axis direction (Z-direction), namely, size b is not small enough to size a degree, and is small enough to the such halfway degree of the effect that can not obtain size a, then there is following problem.The collecting with the solder at the abutment of solder of circumference outside during soldering, solder is detained between size b, and stream narrows.On the other hand, if size b is wide, then the abutment 11 of upper and lower plates and the abutment 13(on the side at abutment 11 are on top crest line 22, be only second to abutment 11 second close to edge, periphery) size shorten, abutment 11 is gathered with the solder at abutment 13, solder is detained between these abutments, and stream narrows.In the plate of embodiment 2, size b is set as the size of the regulation that solder is not detained.Like this, also work as the stream of fluid in the region of size b.If have the heat-exchangers of the plate type of such structure, then pressure loss minimizing and heat transfer area expand and become possibility.
Such as, when the short-axis direction of plate is of a size of 70mm, size b is preferably 3 ~ 4.5mm.Size b can adjust corresponding to the size of the short-axis direction of plate, wave angle degree θ, wave pitch, the physical property of fluid, service condition.Such as in figure 3, when size b is 3 ~ 4.5mm, best wave angle degree θ (the wave angle degree θ 1 of upper-side heat transfer plate 2, the wave angle degree θ 2 of lower-side heat transfer plate 3) is about more than 60 degree ~ less than 70 degree.If the scope of 62.5 degree ~ 67.5 degree is then better.
As described above, upper-side heat transfer plate 2 and lower-side heat transfer plate 3 each other with in the intersection point be present on a root bottom part crest line, closest to along abutment (contact site) corresponding to the intersection point of the end of the edge, periphery on long limit, corresponding to the direction (direction of the top crest line determined by wave angle degree θ 2) of the direction (direction of the bottom crest line determined by wave angle degree θ 1) of the extension of bottom crest line and the extension of top crest line, be formed in the position of the distance (3 ~ 4.5mm) that have left regulation from the edge, periphery along long limit at short side direction (Z-direction).
And the direction that upper-side heat transfer plate 2 is orthogonal with direction that is more close with the direction of top crest line and long limit, the direction of the bottom crest line of lower-side heat transfer plate 3, then junction surface is formed in and leaves position far away from the edge, periphery along long limit.That is, best wave angle degree θ 1 and wave angle degree θ 2 is more close to 90 degree, then size b more increases from " 3 ~ 4.5mm " left and right.
In above embodiment 2, heat-exchangers of the plate type is folded by the multi-disc flaggy of the via hole being provided with the gateway becoming fluid in corner and forms, in this heat-exchangers of the plate type, the edge, periphery describing the long axis direction of plate have left the heat-exchangers of the plate type of the size b of regulation with the abutment being in the upper and lower plates of the shortest size at short-axis direction.
Embodiment 3.
Referring to Fig. 4, embodiment 3 is described.In above embodiment 1,2, for relating to the occasion of the size (distance) between the abutment of upper and lower plates and edge, periphery.Below, in embodiment 3, the occasion of the crest line of the ripple of the plate of the side shortening upper and lower plates is described.
Fig. 4 is the front view of the plate of embodiment 3.Upper-side heat transfer plate 2 and lower-side heat transfer plate 3 is showed in the same manner as Fig. 2.Such as shown in Fig. 4, shorten the crest line of ripple of upper-side heat transfer plate 2, make the terminal of crest line bottom the end 9(of ripple) compare the terminal of 10(top, the end crest line of lower side panel) be formed in inside plate.Like this, the stream of region c that surrounds of formation dashed line in the diagram.
By such stream c is formed in side, edge, periphery, solder collecting outward between circumference and " being in the abutment of the upper and lower plates of the shortest size at short-axis direction " can be avoided to cause flow path width to reduce.In addition, the plate of a side owing to being waveform, so, the pressure loss can be reduced when maintain the heat transfer facilitation effect produced by the stirring action that flows and being constant.In addition, at fluid of more than two kinds along the dynamic occasion of plate current, also can lose the mode compoboard that large fluid side is the short plate of the crest line of ripple, the pressure loss is little fluid side is the long plate of the crest line of ripple by pressing force, form heat exchanger.Fig. 4 at two outer circumferential side forming region c of the short-axis direction of plate, but also can make the distribution of the differential pressure in plate become equably only at the outer circumferential side setting area c of a side corresponding to the direction, gateway of fluid.
In above embodiment 3, heat-exchangers of the plate type is folded by the multi-disc flaggy of the via hole being provided with the gateway becoming fluid in corner and forms, in this heat-exchangers of the plate type, describe the heat-exchangers of the plate type of the crest line of the ripple of the plate of the side shortening upper and lower plates.
Embodiment 4.
Referring to Fig. 5, embodiment 4 is described.In aforementioned embodiments 3, describe the occasion of the crest line of the ripple of the plate of the side shortening upper and lower plates.In present embodiment 4, the occasion of crest line of the ripple shortening upper and lower plates two side is described.
Fig. 5 is the front view of the heat transfer plate of embodiment 4.If shorten the crest line of the ripple of upper and lower plates two side, then the stream of the region d surrounded with dashed line in formation figure.Side, circumference forms such stream outside, prevents the flow path width caused that collects of solder from reducing.Comprise dirt, cellulosic fluid easily becomes the starting point of stream obturation at the abutment of upper and lower plates, if but the formation of Fig. 5, then dirt, cellulosic are from the flow path of region d, thus effectively.In addition, even if to there is pressure increase due to the obturation of stream at high-pressure fluids such as cold-producing mediums, likely develop into pipe arrangement and to break such occasion in the past, refrigerator oil accumulate make in a heat exchanger to compressor oil return delay, likely made the damaged such occasion of compressor in the past, the stream of the region d of Fig. 5 becomes bypass flow path, can prevent above-mentioned occasion.
As described in above embodiment 3,4, as at least either party the plate in the upper-side heat transfer plate 2 of adjacent plate and lower-side heat transfer plate 3, there is distance W(Fig. 4, the Fig. 5 by the regulation from the direction (Z-direction) gone to another long limit along edge, the periphery 2-3 on long limit) scope and size L(Fig. 4, Fig. 5 from the direction that a minor face goes to another minor face) the region c of undressed waveform or region d.
In above embodiment 4, heat-exchangers of the plate type is folded by the multi-disc flaggy of the via hole being provided with the gateway becoming fluid in corner and forms, in this heat-exchangers of the plate type, describe the crest line of the ripple shortening upper and lower plates two side, define the heat-exchangers of the plate type of stream.
Embodiment 5.
Referring to Fig. 6, embodiment 5 is described.In aforementioned embodiments 4, describe the occasion of the crest line of the ripple shortening upper and lower plates two side.In present embodiment 5, the occasion shortening the crest line of the ripple of at least plate of either party every 1 ripple is described.Fig. 6 is the front view of the heat transfer plate of embodiment 5.In figure 6, the crest line of the ripple of upper-side heat transfer plate 2, lower-side heat transfer plate 3 is shortened every 1 ripple.Like this, the abutment 11 being in the upper and lower plates of the shortest size relative to edge, periphery 2-3 at short-axis direction (Z-direction) is not formed.That is, the size b in unsuitable about size b(embodiment 1 that solder collects can there is) position do not form abutment.For this reason, there is not collecting of solder between circumference 2-3 and the abutment of upper and lower plates outside, different every 1 ripple crest line size, for this reason, promote heat transfer by the mixing effect of the flowing of short-axis direction.If the formation of Fig. 6, then can provide and the increase of the pressure loss suppressed and improves the heat-exchangers of the plate type of heat transfer property.And, although Fig. 6 shortens crest line size every 1 ripple, even if make the change in size of crest line corresponding to the liquid form of the design conditions such as heat transfer, the pressure loss, fluid, also same effect can be obtained.
Like this in embodiment 5, the direction of many bottom crest lines of such as upper-side heat transfer plate 2 is towards edge, the periphery 2-3 along long limit.So, many bottom crest lines relative to each end of " edge, the periphery 2-3 along long limit " be alternately formed near " edge, the periphery 2-3 along long limit " position T, compare near position T away from edge, periphery 2-3 and the position S be positioned in front of the T of position.
In above embodiment 5, heat-exchangers of the plate type is folded by the multi-disc flaggy of the via hole being provided with the gateway becoming fluid in corner and forms, in this heat-exchangers of the plate type, the flow direction described at fluid shortens the heat-exchangers of the plate type of the crest line of the ripple of plate every 1 ripple.
Embodiment 6.
Referring to Fig. 7, embodiment 6 is described.In aforementioned embodiments 5, describe the occasion shortening the crest line of the ripple of plate every 1 ripple.In present embodiment 6, illustrate that the suitable portion, abutment being in the upper and lower plates of the shortest size at short-axis direction (Z-direction) in the edge, periphery relative to upper and lower plates (does not engage, there is gap) point, between the paddy (bottom) of the ripple of upper-side heat transfer plate 2 and the mountain portion (top) of the ripple of lower-side heat transfer plate 3, be provided with the occasion in the gap of more than 0.2mm.
The figure that Fig. 7 has been the signal suitable with the sectional view of heat transfer plate.Fig. 7 is the suitable figure for being described gap size e described later.If (there is gap as described above in the upper and lower plates abutment being in the shortest size at short-axis direction (Z-direction) relative to edge, the periphery 2-3 of plate, so, be precisely the abutment suitable portion suitable with abutment) size b(and Fig. 3 same) the ripple portion of upper plate and the mountain portion of lower plate between gap be size e.If size e is at more than 0.2mm, eliminate the joint of upper and lower plates, collecting of the solder preventing the abutment of edge, periphery 2-3 and upper and lower plates from causing.As its result, same with embodiment 1 ~ 5, the heat-exchangers of the plate type of the increase having in the lump and suppress the pressure loss and the effect improving heat transfer property can be provided.
Like this in embodiment 6, in adjacent upper-side heat transfer plate 2, the intersection point of lower-side heat transfer plate 3 each other on a root bottom part crest line of upper-side heat transfer plate 2, closest to the intersection point of the end of " edge, periphery along long limit ", between the wave base portion represented with afore-mentioned bottom crest line and the wave crest portion represented with the top crest line of lower-side heat transfer plate 3, form gap.In addition, the intersection point beyond the intersection point of aforesaid end, the wave base portion represented with bottom crest line and the ripple top contact represented with top crest line.
In above embodiment 6, heat exchanger is folded by the multi-disc flaggy of the via hole being provided with the gateway becoming fluid in corner and forms, in this heat-exchangers of the plate type, describe the suitable portion, abutment of the upper and lower plates being in the shortest size in the edge, periphery relative to upper and lower plates at short-axis direction, be provided with the heat-exchangers of the plate type in the gap of more than 0.2mm in the valley of the ripple of plate and mountain portion.
The heat transfer plate described in above embodiment 1 ~ 6 can be used for air-conditioning, generating, food pasteurization treatment facility etc. be loaded with many industry, the housed device of heat-exchangers of the plate type.Such as, can be used for pipe arrangement connect compressor, radiator, expansion mechanism, the aforementioned heat sink of heat pump assembly of evaporimeter or evaporimeter or they both.
The explanation of Reference numeral
1 reinforcement side plate, 2 upper-side heat transfer plate, 2-1, 3-1 minor face, 2-2, the long limit of 3-2, 2-3, edge, 3-3 periphery, 3 lower-side heat transfer plate, 4 reinforcement side plates, the inflow pipe of 5 first fluids, the inflow pipe of 6 second fluids, the effuser of 7 first fluids, the effuser of 8 second fluids, the end of the valley of the ripple of 9 upper-side heat transfer plate, the end in the mountain portion of the ripple of 10 lower-side heat transfer plate, 11 abutments being in the upper and lower plates of the shortest size from edge, periphery at short-axis direction, the edge, periphery of 12 plates, 13 abutments being in the second short upper and lower plates from edge, periphery at short-axis direction, 100 heat-exchangerss of the plate type.
Claims (6)
1. a heat-exchangers of the plate type, by long limit each other, minor face each other, the mode that overlaps each other of edge, periphery is stacked multiplely has long limit, minor face, formation to the plate of the rectangle of the edge, periphery in the space that fluid seals,
Each plate is carried out the processing of the waveform conjugated at stacked direction,
Adjacent plate is each other in the occasion of watching from stacked direction, represent the wave base portion of the plate of a side and imaginary many bottom crest lines extended in the direction different from the direction on aforementioned long limit with represent the wave crest portion of plate of the opposing party and imaginary many top crest lines extended in the direction different with the direction on aforementioned long limit intersect and form intersection point
The wave base portion represented by each afore-mentioned bottom crest line contacts at aforementioned intersection point with the wave crest portion represented by each aforementioned top crest line, forms the contact site by soldered joint;
It is characterized in that:
Aforementioned adjacent plate each other with in the aforementioned intersection point be present on an afore-mentioned bottom crest line, closest to along aforementioned contact portion corresponding to the aforementioned intersection point of the end of the edge, aforementioned periphery on aforementioned long limit, the direction that the direction extended corresponding to afore-mentioned bottom crest line and aforementioned top crest line extend, is formed in the position of the distance that have left regulation from the edge, aforementioned periphery along aforementioned long limit at short side direction; And
With in the aforementioned intersection point be present on an afore-mentioned bottom crest line, the closest aforementioned contact portion corresponding along the aforementioned intersection point of the end of the edge, aforementioned periphery on aforementioned long limit, more than 60 degree are in and the scope of less than 70 degree relative to the direction on aforementioned long limit in the direction of afore-mentioned bottom crest line, and under the state passing through soldered joint, the stream of fluid is formed together with the edge, aforementioned periphery along aforementioned long limit
The plate of aforementioned two adjacent sides, has the scope of distance by the regulation in the direction gone to another long limit from the edge, aforementioned periphery along aforementioned long limit and the region from the undressed forementioned waveform of the size in the direction that a minor face goes to another minor face.
2. heat-exchangers of the plate type according to claim 1, is characterized in that:
With in the aforementioned intersection point be present on an afore-mentioned bottom crest line, closest to along aforementioned contact portion corresponding to the aforementioned intersection point of the end of the edge, aforementioned periphery on aforementioned long limit, the direction of aforementioned top crest line is in more than 60 degree and the scope of less than 70 degree relative to the direction on aforementioned long limit.
3. heat-exchangers of the plate type according to claim 2, is characterized in that:
With in the aforementioned intersection point be present on an afore-mentioned bottom crest line, closest to along aforementioned contact portion corresponding to the aforementioned intersection point of the end of the edge, aforementioned periphery on aforementioned long limit, the direction of afore-mentioned bottom crest line is in the scope of more than 62.5 degree less than 67.5 degree relative to the direction on aforementioned long limit and the direction of aforementioned top crest line relative to the direction on aforementioned long limit.
4. the heat-exchangers of the plate type according to any one of claims 1 to 3, is characterized in that:
The direction that the direction of aforementioned adjacent plate afore-mentioned bottom crest line each other and the direction of aforementioned top crest line direction that is more close and aforementioned long limit is orthogonal, aforementioned contact portion is formed in leaves position far away from the edge, aforementioned periphery along aforementioned long limit.
5. a heat pump assembly, with pipe arrangement connect compressor, the first heat exchanger, expansion mechanism, the second heat exchanger form; It is characterized in that:
As at least any one heat exchanger in aforementioned first heat exchanger, aforementioned second heat exchanger, it is the heat-exchangers of the plate type according to any one of claims 1 to 3.
6. a heat pump assembly, with pipe arrangement connect compressor, the first heat exchanger, expansion mechanism, the second heat exchanger form; It is characterized in that:
As at least any one heat exchanger in aforementioned first heat exchanger, aforementioned second heat exchanger, it is heat-exchangers of the plate type according to claim 4.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2009263598A JP2011106764A (en) | 2009-11-19 | 2009-11-19 | Plate type heat exchanger and heat pump device |
JP2009-263598 | 2009-11-19 | ||
PCT/JP2010/070192 WO2011062118A1 (en) | 2009-11-19 | 2010-11-12 | Plate-type heat exchanger and heat pump device |
Publications (2)
Publication Number | Publication Date |
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CN102667391A CN102667391A (en) | 2012-09-12 |
CN102667391B true CN102667391B (en) | 2016-03-02 |
Family
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201080052178.0A Active CN102667391B (en) | 2009-11-19 | 2010-11-12 | Heat-exchangers of the plate type and heat pump assembly |
Country Status (6)
Country | Link |
---|---|
US (1) | US20120227438A1 (en) |
EP (1) | EP2503277B1 (en) |
JP (1) | JP2011106764A (en) |
CN (1) | CN102667391B (en) |
HK (1) | HK1172080A1 (en) |
WO (1) | WO2011062118A1 (en) |
Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8544294B2 (en) * | 2011-07-11 | 2013-10-01 | Palo Alto Research Center Incorporated | Plate-based adsorption chiller subassembly |
US10690421B2 (en) | 2012-03-28 | 2020-06-23 | Modine Manufacturing Company | Heat exchanger and method of cooling a flow of heated air |
EP2657636B1 (en) | 2012-04-23 | 2015-09-09 | GEA Ecoflex GmbH | Plate heat exchanger |
WO2015082348A1 (en) * | 2013-12-05 | 2015-06-11 | Swep International Ab | Heat exchanging plate with varying pitch |
JP6947314B2 (en) * | 2018-12-28 | 2021-10-13 | 三菱電機株式会社 | Plate heat exchanger and heat pump device |
EP4166880A1 (en) * | 2021-10-12 | 2023-04-19 | Valeo Autosystemy SP. Z.O.O. | A plate for a heat exachanger |
RS20221182A1 (en) | 2022-12-26 | 2024-06-28 | Euro Heat Doo | Heat exchanger with welded internal exchange plates |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002107074A (en) * | 2000-09-29 | 2002-04-10 | Sanyo Electric Co Ltd | Plate type heat exchanger and heat pump hot water supply apparatus using the same |
CN1833153A (en) * | 2003-08-01 | 2006-09-13 | 贝洱两合公司 | Heat exchanger and method for the production thereof |
JP2008039255A (en) * | 2006-08-03 | 2008-02-21 | Toshiba Corp | Heat exchanger and its manufacturing method |
WO2009123517A1 (en) * | 2008-04-04 | 2009-10-08 | Alfa Laval Corporate Ab | A plate heat exchanger |
Family Cites Families (17)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
SE356123B (en) | 1971-10-08 | 1973-05-14 | Alfa Laval Ab | |
JPS6218867Y2 (en) * | 1981-03-20 | 1987-05-14 | ||
JPS6060592U (en) * | 1983-09-27 | 1985-04-26 | 株式会社日阪製作所 | Plate heat exchanger |
JPS6183882A (en) * | 1984-09-29 | 1986-04-28 | Hisaka Works Ltd | Plate type heat exchanger |
SE458884B (en) * | 1987-05-29 | 1989-05-16 | Alfa Laval Thermal Ab | PERMANENT COMBINED PLATE HEAT EXCHANGE WITH CONTAINING BODY AT THE PORTS |
FR2705445B1 (en) * | 1993-05-18 | 1995-07-07 | Vicarb Sa | Plate heat exchanger. |
DE4431413C2 (en) * | 1994-08-24 | 2002-10-10 | Rehberg Michael | Plate heat exchangers for liquid and gaseous media |
SE504868C2 (en) * | 1995-10-23 | 1997-05-20 | Swep International Ab | Plate heat exchanger with end plate with pressed pattern |
JP3682343B2 (en) | 1996-09-30 | 2005-08-10 | 株式会社日阪製作所 | Plate heat exchanger |
JP3094979B2 (en) * | 1997-12-10 | 2000-10-03 | ダイキン工業株式会社 | Plate heat exchanger |
DE10348803B4 (en) * | 2003-10-21 | 2024-03-14 | Modine Manufacturing Co. | Housing-less plate heat exchanger |
SE528879C2 (en) * | 2005-07-04 | 2007-03-06 | Alfa Laval Corp Ab | Heat exchanger plate, pair of two heat exchanger plates and plate package for plate heat exchanger |
JP2009036468A (en) * | 2007-08-02 | 2009-02-19 | Denso Corp | Housingless heat exchanger |
US8596343B2 (en) * | 2008-04-04 | 2013-12-03 | Alfa Laval Corporate Ab | Plate heat exchanger |
PT2267391T (en) * | 2009-06-26 | 2018-06-20 | Swep Int Ab | Asymmetric heat exchanger |
CN103688128B (en) * | 2011-07-13 | 2015-11-25 | 三菱电机株式会社 | Plate type heat exchanger and heat pump assembly |
DE102014226479A1 (en) * | 2014-12-18 | 2016-06-23 | Mahle International Gmbh | Heat exchanger |
-
2009
- 2009-11-19 JP JP2009263598A patent/JP2011106764A/en active Pending
-
2010
- 2010-11-12 WO PCT/JP2010/070192 patent/WO2011062118A1/en active Application Filing
- 2010-11-12 US US13/510,633 patent/US20120227438A1/en not_active Abandoned
- 2010-11-12 CN CN201080052178.0A patent/CN102667391B/en active Active
- 2010-11-12 EP EP10831513.6A patent/EP2503277B1/en active Active
-
2012
- 2012-12-13 HK HK12112886.8A patent/HK1172080A1/en unknown
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002107074A (en) * | 2000-09-29 | 2002-04-10 | Sanyo Electric Co Ltd | Plate type heat exchanger and heat pump hot water supply apparatus using the same |
CN1833153A (en) * | 2003-08-01 | 2006-09-13 | 贝洱两合公司 | Heat exchanger and method for the production thereof |
JP2008039255A (en) * | 2006-08-03 | 2008-02-21 | Toshiba Corp | Heat exchanger and its manufacturing method |
WO2009123517A1 (en) * | 2008-04-04 | 2009-10-08 | Alfa Laval Corporate Ab | A plate heat exchanger |
Also Published As
Publication number | Publication date |
---|---|
WO2011062118A1 (en) | 2011-05-26 |
EP2503277A1 (en) | 2012-09-26 |
EP2503277A4 (en) | 2014-08-13 |
JP2011106764A (en) | 2011-06-02 |
EP2503277B1 (en) | 2019-09-04 |
US20120227438A1 (en) | 2012-09-13 |
HK1172080A1 (en) | 2013-04-12 |
CN102667391A (en) | 2012-09-12 |
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