CN101266109A - Total-heat exchanger and manufacturing method thereof - Google Patents

Total-heat exchanger and manufacturing method thereof Download PDF

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Publication number
CN101266109A
CN101266109A CNA2008100044752A CN200810004475A CN101266109A CN 101266109 A CN101266109 A CN 101266109A CN A2008100044752 A CNA2008100044752 A CN A2008100044752A CN 200810004475 A CN200810004475 A CN 200810004475A CN 101266109 A CN101266109 A CN 101266109A
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China
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stream
corrugated sheet
mentioned
barrier film
parts
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CNA2008100044752A
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Chinese (zh)
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CN101266109B (en
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小田岛贞雄
高桥健造
冈田诚
井上彰
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Massachusetts Institute of Technology
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Massachusetts Institute of Technology
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    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/56—Heat recovery units

Abstract

The aim of the invention is to supply an opposite flow full heat exchanger which achieves reducing the bonding part and expanding effective heat transfer area as well as improving heat exchange efficiency actually. Multiple pieces of heat exchange parts (20) composed of a membrane (1) and a stream forming part (2) bonded on the membrane (1) to form a stream (7) are laminated up and down; the opposite flow full heat exchanger exchanges heat to the sensible heat and the latent heat of two gases through the membrane (1); the stream forming part (2) has multiple frame parts (3) set along the outer margin (1a) of the membrane (1), and a thin rib part (4) which is collocated between the two frame parts (3) in set interval and has width size smaller than the frame parts (3); a strip plate corrugated sheet part (9A) is at the inlet (5) and the outlet (6) of the stream (7) for preventing the inlet (5) and the outlet (6) changing.

Description

Total-heat exchanger and manufacture method thereof
Technical field
The present invention relates to make simultaneously the total-heat exchanger of sensible heat and latent heat heat exchange, relate to the flow pattern in opposite directions of packing air-conditioning system or air regenerating device into and using or the total-heat exchanger and the manufacture method thereof of positive AC type via the exhaust that barrier film carries out the air feed of fresh extraneous air and dirty room air.
Background technology
In recent years, advance the high thermal insulationization of living space, high airtightization for the effect that improves changes in temperature equipment, accompany with it, the pollution of room air becomes problem, and the importance of ventilation is familiar with once more.The method of taking a breath as not damaging changes in temperature equipment effect, the method for carrying out heat exchange between air feed and exhaust is effective.At this moment, as if the exchange with temperature (sensible heat), carry out the exchange of humidity (latent heat) simultaneously, then its effect is remarkable.As the structure that adapts to this requirement, for example the accompanying drawing of patent documentation 1 records via dividing plate and makes air feed and exhaust carry out the positive AC type total-heat exchanger of full heat exchange.
This positive AC type total-heat exchanger as shown in figure 28, the stream of fitted flat heat exchanger plate 41 and waveform is formed plate 42 (wherein, among Figure 28 this stream form plate 42 describe greatly, actual then be the waveform of very little pitch and height) heat-exchanging part 43 when alternately stacked, the direction that makes stream formation plate 42 forms air feed stream and exhaust flow path every one deck ground quadrature.For example, as air feed, the fresh but cold dry air of open air in winter is passed through, as exhaust, make the indoor dirt of being warmed oneself but the warm high air of humidity passes through, then carry out the exchange of temperature and humidity, make that air feed is heated, humidification and supply to indoor via above-mentioned heat exchanger plate 41.On the other hand, make exhaust cooling, dehumidification and exhaust outside the room.
Patent documentation 1: special public clear 47-19990 communique
Summary of the invention
Bonding more flat heat exchanger plate 41 is simple owing to manufacture method with the above-mentioned positive AC type total-heat exchanger that the stream formation plate 42 of making waveform forms, so just on market, sold in the past, though it is bonding portion is effective to the heat transfer of sensible heat, invalid to the heat transfer (seeing through of steam) of latent heat.And, positive AC type total-heat exchanger on principle heat exchanger effectiveness than flow pattern total-heat exchanger in opposite directions low because above-mentioned two reasons, the limit of full heat exchanger effectiveness just 50%～60%.Therefore the objective of the invention is to the total-heat exchanger of realizing that heat exchanger effectiveness is higher.And its purpose is, uses or under the situation of cold place frosting, prevents from because of the change of shape of wind path the pressure loss to be increased long-time.Particularly, its purpose is, prevents owing to peristome (inlet, outlet) distortion makes wind be difficult to rise by (air quantity reduction), deterioration of efficiency or the pressure loss.
And, the object of the present invention is to provide a kind of manufacture method of total-heat exchanger, can effectively utilize tabular corrugated sheet parts and reduce manufacturing cost.
To achieve the above object, the present invention relates to a kind of total-heat exchanger, with many by barrier film be bonded on this barrier film and the stream that forms stream forms the heat-exchanging part stacked on top of one another that parts constitute, via this barrier film the sensible heat and the latent heat of two kinds of gases is carried out heat exchange, wherein, above-mentioned stream forms parts, have a plurality of members of frame that are provided with along the outer rim of above-mentioned barrier film, and between two these members of frame with set arranged spaced and the width dimensions thin flank spare littler than the width dimensions of this members of frame, and, inlet at above-mentioned stream, the exit has and is used to prevent this inlet, the tabular corrugated sheet parts of band shape of the change of shape of outlet, above-mentioned corrugated sheet parts are upper wall surfaces, lower wall surface is shaped integratedly with a plurality of fins that are connected this upper wall surface and lower wall surface and constitutes.
And, with many by the barrier film of hexagon shape be bonded on this barrier film and the stream that forms stream forms the heat-exchanging part stacked on top of one another that parts constitute, in the total-heat exchanger of the flow pattern in opposite directions of the sensible heat and the latent heat of two kinds of gases being carried out heat exchange via this barrier film, above-mentioned stream forms parts, have a plurality of members of frame that are provided with along the outer rim of above-mentioned barrier film, and between two these members of frame with set arranged spaced and the width dimensions thin flank spare littler than the width dimensions of this members of frame, and comprise the inlet that has with above-mentioned stream, the triangle profile of the triangular portion correspondence of outlet side and be formed with the area that accounts for above-mentioned triangular portion more than 70% and the reinforcement of one or more through holes of 95% following scope with the tabular corrugated sheet parts of triangular planar, above-mentioned corrugated sheet parts are upper wall surfaces, lower wall surface is shaped integratedly with a plurality of fins that are connected this upper wall surface and lower wall surface and constitutes.
And, with many by the barrier film of hexagon shape and be bonded on this barrier film and the stream that forms stream forms heat-exchanging part stacked on top of one another that parts constitute, in the total-heat exchanger of the flow pattern in opposite directions of the sensible heat and the latent heat of two kinds of gases being carried out heat exchange via this barrier film, above-mentioned stream formation parts have: along a plurality of members of frame of the outer rim setting of above-mentioned barrier film; Have the triangle profile corresponding with the triangular portion of the inlet of above-mentioned stream, outlet side and be formed with the area that accounts for above-mentioned triangular portion more than 70% and the reinforcement of one or more through holes of 95% following scope with the tabular corrugated sheet parts of triangular planar; And have the quadrangle shape profile corresponding with the quadrangle portion that triangular portion clipped of the inlet of above-mentioned stream, outlet side and be formed with the area that accounts for above-mentioned quadrangle portion more than 70% and the reinforcement of one or more through holes of 95% following scope with quadrangle tabular corrugated sheet parts, above-mentioned corrugated sheet parts upper wall surface, lower wall surface are shaped integratedly with a plurality of fins that are connected this upper wall surface and lower wall surface and constitute.
And, with many by the barrier film of hexagon shape be bonded on this barrier film and the stream that forms stream forms the heat-exchanging part stacked on top of one another that parts constitute, in the total-heat exchanger of the flow pattern in opposite directions of the sensible heat and the latent heat of two kinds of gases being carried out heat exchange via this barrier film, above-mentioned stream forms parts and has a plurality of members of frame that are provided with along the outer rim of above-mentioned barrier film, with having the hexagonal portion that clipped with above-mentioned members of frame corresponding hexagon shape profile and being formed with account for above-mentioned hexagonal portion area more than 70% and the reinforcement of one or more through holes of 95% following scope with hexagon tabular corrugated sheet parts, above-mentioned corrugated sheet parts are upper wall surfaces, lower wall surface is shaped integratedly with a plurality of fins that are connected this upper wall surface and lower wall surface and constitutes.
In addition, above-mentioned members of frame and above-mentioned corrugated sheet parts utilize chimeric and fixing.
And, with many by barrier film be bonded on this barrier film and the stream that forms stream forms the heat-exchanging part stacked on top of one another that parts constitute, in the total-heat exchanger of the flow pattern in opposite directions of the sensible heat and the latent heat of two kinds of gases being carried out heat exchange via this barrier film, above-mentioned stream forms parts, comprise a plurality of members of frame that are provided with along the outer rim of above-mentioned barrier film, and be arranged on two tabular corrugated sheet parts of the band shape between this members of frame, and inlet at above-mentioned stream, the exit has and is used to prevent this inlet, the tabular corrugated sheet parts of band shape of the change of shape of outlet, and, by chimeric and fixing, above-mentioned corrugated sheet parts are upper wall surfaces with above-mentioned members of frame and the tabular corrugated sheet parts of above-mentioned band shape, lower wall surface is shaped integratedly with a plurality of fins that are connected this upper wall surface and lower wall surface and constitutes.
And, be provided with the tabular corrugated sheet parts of band shape at the flow direction pars intermedia of stream.
And, with many by barrier film be bonded on this barrier film and the stream that forms stream forms the heat-exchanging part stacked on top of one another that parts constitute, in the total-heat exchanger of the positive AC type that the sensible heat and the latent heat of two kinds of gases is carried out heat exchange via this barrier film, above-mentioned stream forms parts, have a plurality of members of frame that are provided with along the outer rim of above-mentioned barrier film, and between two these members of frame with set arranged spaced and the width dimensions thin flank spare littler than the width dimensions of this members of frame, and inlet at above-mentioned stream, the exit has and is used to prevent this inlet, the tabular corrugated sheet parts of band shape of the change of shape of outlet, above-mentioned corrugated sheet parts are upper wall surfaces, lower wall surface is shaped integratedly with a plurality of fins that are connected this upper wall surface and lower wall surface and constitutes.
And, with many by barrier film be bonded on this barrier film and the stream that forms stream forms the heat-exchanging part stacked on top of one another that parts constitute, in the total-heat exchanger of the positive AC type that the sensible heat and the latent heat of two kinds of gases is carried out heat exchange via this barrier film, above-mentioned stream forms parts, has the thin flank spare of outer rim that is provided with along the outer rim of above-mentioned barrier film, with between two thin flank spares of this outer rim with set arranged spaced and the width dimensions thin flank spare identical with the width dimensions of the thin flank spare of this outer rim, and inlet at above-mentioned stream, the exit has and is used to prevent this inlet, the tabular corrugated sheet parts of band shape of the change of shape of outlet, above-mentioned corrugated sheet parts are upper wall surfaces, lower wall surface is shaped integratedly with a plurality of fins that are connected this upper wall surface and lower wall surface and constitutes.
And, to form alternately stacked on top of one another of parts by square barrier film and the stream that forms stream, in the total-heat exchanger of the positive AC type that the sensible heat and the latent heat of two kinds of gases is carried out heat exchange via this barrier film, above-mentioned stream forms parts by having the square shaped cross-sectional profile corresponding with above-mentioned barrier film, and be formed with the area that accounts for above-mentioned barrier film more than 70% and the reinforcement of a plurality of through holes of 95% following scope constitute with square tabular corrugated sheet parts, above-mentioned corrugated sheet parts are upper wall surfaces, lower wall surface is shaped integratedly with a plurality of fins that are connected this upper wall surface and lower wall surface and constitutes.
And above-mentioned reinforcement is made of a plurality of tabular corrugated sheet parts of cutting apart with square tabular corrugated sheet parts, and above-mentioned at least one that cut apart in the tabular corrugated sheet parts is the comb shape shape.
And the fin of above-mentioned corrugated sheet parts forms the linearity or the continuous wave shape of above-below direction.
And, the manufacture method of total-heat exchanger of the present invention is that barrier film and the stream that forms stream are formed alternately stacked on top of one another of parts, the manufacture method of the total-heat exchanger of the positive AC type that the sensible heat and the latent heat of two kinds of gases is carried out heat exchange via this barrier film, wherein, from upper wall surface, lower wall surface is shaped integratedly with a plurality of fins that are connected this upper wall surface and lower wall surface and the tabular corrugated sheet parts of 1 Zhang Ping that constitute, cutting off and making the corrugated sheet parts of cutting apart of two comb shape shapes is to mesh shape relatively, use this to cut apart the corrugated sheet parts, formation has the reinforcement with a plurality of through holes of the square shaped cross-sectional profile corresponding with above-mentioned barrier film with square tabular corrugated sheet parts, utilizes this reinforcement to make stream with square tabular corrugated sheet parts and forms parts.
According to total-heat exchanger of the present invention, can improve sensible heat exchange efficiency, latent heat exchange efficiency and full heat exchanger effectiveness, and reduce the pressure loss.For example, can make the sensible heat exchange efficiency is more than 85%, and the latent heat exchange efficiency is more than 70%, and full heat exchanger effectiveness is more than 75%, and the pressure loss is below the 45Pa.Particularly, inlet, outlet are strengthened fully and can not be out of shape, and wind passes through easily thus, and the pressure loss also reduces, and full heat exchanger effectiveness improves.
And,, can effectively utilize tabular corrugated sheet parts and reduce manufacturing cost according to the manufacture method of total-heat exchanger of the present invention.
Description of drawings
Fig. 1 is the stereogram of expression the 1st embodiment of the present invention.
Fig. 2 is the simple stereogram of decomposition of expression the 1st embodiment of the present invention.
Fig. 3 is the vertical view of expression the 1st embodiment of the present invention.
Fig. 4 is the vertical view of expression heat-exchanging part
Fig. 5 is the vertical view of expression the 2nd embodiment.
Fig. 6 is the vertical view of expression the 3rd embodiment.
Fig. 7 is the vertical view of expression the 4th embodiment.
Fig. 8 is the vertical view of expression the 5th embodiment.
Fig. 9 is the vertical view of expression the 6th embodiment.
Figure 10 is the vertical view of expression the 7th embodiment.
Figure 11 is the vertical view of expression the 8th embodiment.
Figure 12 is the vertical view of expression the 9th embodiment.
Figure 13 is the vertical view of expression the 10th embodiment.
Figure 14 is the cross sectional plan view of an example of expression user mode.
Figure 15 is the stereogram of an example of expression corrugated sheet parts.
Figure 16 is the stereogram of another example of expression corrugated sheet parts.
Figure 17 is the side view that expression has the tabular corrugated sheet parts of band shape of breach.
Figure 18 is the vertical view of expression the 11st embodiment.
Figure 19 is the longitudinal section of expression the 11st embodiment.
Figure 20 is the vertical view of expression the 12nd embodiment.
Figure 21 is the longitudinal section of expression the 12nd embodiment.
Figure 22 is the vertical view of expression the 13rd embodiment.
Figure 23 is the longitudinal section of expression the 13rd embodiment.
Figure 24 is the vertical view of expression the 14th embodiment.
Figure 25 is the vertical view of expression the 15th embodiment.
Figure 26 is the key diagram of the manufacture method of expression the 14th embodiment.
Figure 27 is the key diagram of the manufacture method of expression the 15th embodiment.
Figure 28 is a stereogram of representing positive AC type total-heat exchanger in the past.
Description of reference numerals:
1 barrier film
The 1a outer rim
2 streams form parts
3 members of frame
The thin flank spare of 3A outer rim
4 thin flank spares
5 inlets
6 outlets
7 streams
9 corrugated sheet parts
The tabular corrugated sheet parts of 9A band shape
16 upper wall surfaces
17 lower wall surfaces
18 fins
20 heat-exchanging parts
34 triangular portion
35 quadrangle portions
36 hexagonal portion
37 through holes
38 through holes
39 through holes
44 through holes
The tabular corrugated sheet parts of 90a triangular planar
90b quadrangle tabular corrugated sheet parts
90c hexagon tabular corrugated sheet parts
90d square tabular corrugated sheet parts
100 cut apart the corrugated sheet parts
D 3Width dimensions
D 4Width dimensions
S 1Area
S 2Area
S 3Area
S 4Area
The specific embodiment
Fig. 1～Fig. 4 represents the 1st embodiment of the present invention.This total-heat exchanger is that many are formed heat-exchanging part 20 stacked on top of one another that parts 2 are formed, made the sensible heat of two kinds of gases and the total-heat exchanger of flow pattern in opposite directions that latent heat carries out heat exchange via barrier film 1 by the barrier film 1 of hexagon shape and stream bonding with barrier film 1 and that form stream 7.Heat-exchanging part 20 forms the shape of the hexagonal portion 36 of the triangular portion 34 that has quadrangle portion 35 and be configured in its two ends.The air feed that forms air feed stream 10 is alternately stacked with heat-exchanging part 20B with the exhaust of heat-exchanging part 20A and formation exhaust flow path 11.Air feed is different with heat-exchanging part 20B direction with exhaust with heat-exchanging part 20A.That is, air feed be not configured (formation) up and down with heat-exchanging part 20A and exhaust on hexagonal different limit overlappingly with inlet 5 (air supply inlet 32, exhaust entrance 22), outlet 6 (air supply outlet 31, the air exits 21) of heat-exchanging part 20B.
Figure 14 is the figure of an example of expression user mode of the present invention, sets up the casing 25 that has total-heat exchanger 40 in inside in divided chamber on the wall Z of X and outdoor Y.And, in casing 25, be provided with air feed pressure fan 12 and exhaust pressure fan 13, be attached with filter 24 at the suction inlet 26a of indoor X side and the suction inlet 26b of outdoor Y side.Air feed pressure fan 12 is arranged on the downstream of air feed stream 10 (with reference to Fig. 2), and exhaust pressure fan 13 is arranged on the downstream of exhaust flow path 11, and this total-heat exchanger 40 forms double suction and goes into mode.A represents to flow through the flow direction that is formed the air (air feed air) of the air feed stream 10 that parts 2 form by stream, and B represents to flow through the flow direction that is formed the air (evacuating air) of the exhaust flow path 11 that parts 2 form by stream.In casing 25,, air feed air and evacuating air, be provided with a plurality of space bars 27 by total-heat exchanger 40 for not being mixed.
According to Fig. 4 the 1st embodiment is described.Stream form parts 2 have along a plurality of members of frame 3 of the outer rim 1a configuration of barrier film 1 and between two members of frame 3 by set arranged spaced and than the width dimensions D of members of frame 3 3Little width dimensions D 4 Thin flank spare 4, and, the tabular corrugated sheet parts of band shape (cut-out parts) 9A with change of shape of the inlet 5 that is used to prevent stream 7, outlet 6.
Barrier film 1 is by the hydrophilic macromolecule thin film coated is being formed for the moisture permeable membrane that forms on the surface of raw-material porous matter sheet material with for example polyethylene, polypropylene, acetate fiber, polytetrafluoroethylene (PTFE) etc.
Members of frame 3 is formed by for example paper, resin etc.The gauge T of members of frame 3 3(with reference to Fig. 2) is set at more than the 1.5mm and below the 2.5mm.At gauge T 3Under the situation less than lower limit, undercapacity.At gauge T 3Surpass under the situation of higher limit the heat exchanger effectiveness variation.
Thin flank spare 4 is formed by for example paper, resin etc.The gauge T of thin flank spare 4 4(with reference to Fig. 2) is set at below the above 2.5mm of 1.5mm.At gauge T 4Under the situation less than lower limit, undercapacity.At gauge T 4Surpass under the situation of higher limit the heat exchanger effectiveness variation.
Corrugated sheet parts 9 are formed by material of for example resin system such as polyethylene, polypropylene or made of paper or the metal formings such as aluminium that have been shaped etc.Particularly, as shown in figure 15, corrugated sheet parts 9 are by upper wall surface 16, lower wall surface 17 and be connected that a plurality of fins 18 of upper wall surface 16 and lower wall surface 17 are integrally formed to be constituted.In Figure 15, the fin 18 of corrugated sheet parts 9 is linearities of above-below direction.As shown in figure 16, the fin 18 of corrugated sheet parts 9 also can form the continuous wave shape.The gauge T of corrugated sheet parts 9 9Be set at below the above 2.5mm of 1.5mm.At gauge T 9Under the situation less than lower limit, make difficulty.At gauge T 9Surpass under the situation of higher limit the heat exchanger effectiveness variation.
Below, the step of making total-heat exchanger 40 is described.
In Fig. 2, strengthen with substrate 15 by seeing that from stacked direction having plastic plate that the shape identical with barrier film 1 and thickness is 2～20mm or metallic plate or plank forms, and is provided with hole portion 19 on each position, summit C of substrate 15.
And, making a pair of substrate 15 clip a plurality of heat-exchanging parts 20 and dispose, the perforation shape is made by the hole portion 29 that will form on the top of each heat-exchanging part 20, is linked by stirrup 28.Particularly, an end of stirrup 28 is embedded in a side the hole portion 19 of each position, summit C of substrate 15, then, the stream that makes stirrup 28 run through each heat-exchanging part 20 forms the hole portion 29 of parts 2 (members of frame 3).Like this, a plurality of heat-exchanging parts 20 are stacked gradually, and make stirrup 28 from wherein passing through, and embed in the opposing party's the hole portion 19 of substrate 15 at the other end of stirrup 28.Then the both ends of stirrup 28 by screw thread fix, bonding agent is bonding or welding etc. is fixed on the substrate 15,15.Stirrup 28 is formed by metals such as aluminium, iron, stainless steel or resin.
In addition, Fig. 1 is a schematic drawing, and total-heat exchanger 40 alternately is laminated with 150～250 layers, most preferably is about 200 layers of air feed with air feed stream 10 with heat-exchanging part 20A with have the exhaust heat-exchanging part 20B of exhaust flow path 11.
Fig. 5 represents the 2nd embodiment.Stream formation parts 2 have reinforcement, and 90a (promptly with the tabular corrugated sheet parts of triangular planar (stamping-out parts), leg-of-mutton tabular corrugated sheet parts 9B), it has with the triangular portion 34 corresponding triangle profiles of the inlet 5 of stream 7, outlet 6 sides and is formed with the area S that accounts for triangular portion 34 1More than 70% and three through holes 37 of 95% following scope.Other structure is identical with the 1st embodiment.
Fig. 6 represents the 3rd embodiment.Stream forms parts 2 to have: have with the triangular portion 34 corresponding triangle profiles of the inlet 5 of stream 7, outlet 6 sides and be formed with the area S that accounts for triangular portion 34 1More than 70% and the reinforcement of three through holes 37 of 95% following scope with the tabular corrugated sheet parts of triangular planar 90a; And have with by the quadrangle portion 35 corresponding quadrangle shape profiles that clip of triangular portion 34 of inlet 5, outlet 6 sides and be formed with the area S that accounts for quadrangle portion 35 2More than 70% and the reinforcement of three through holes 38 of 95% following scope with quadrangle tabular corrugated sheet parts (stamping-out parts) 90b (that is tetragonal tabular corrugated sheet parts 9B).Other structure is identical with the 1st embodiment.
Fig. 7 represents the 4th embodiment.Stream formation parts 2 have reinforcement, and 90c (promptly with hexagon tabular corrugated sheet parts (stamping-out parts), hexagonal tabular corrugated sheet parts 9B), its have the hexagonal portion 36 corresponding hexagon shape profiles that clip with members of frame 3 and be formed with the area that accounts for hexagonal portion 36 more than 70% and nine through holes 39 of 95% following scope.Other structure is identical with the 1st embodiment.
Fig. 8 represents the 5th embodiment.Members of frame 3 and corrugated sheet parts 9 are by chimeric and fixing.That is, on a side of members of frame 3 and corrugated sheet parts 9, form dovetail groove 23, and on the opposing party, be formed with can freely load and unload and the chimeric prominent bar 33 of dovetail groove 23.Triangular planar tabular corrugated sheet parts 90a and quadrangle tabular corrugated sheet parts 90b are by chimeric and fixing.That is, on the side of triangular planar tabular corrugated sheet parts 90a and quadrangle tabular corrugated sheet parts 90b, form dovetail groove 23, and on the opposing party, be formed with can freely load and unload and the chimeric prominent bar 33 of dovetail groove 23.Other structure is identical with the 6th embodiment.
Fig. 9 represents the 6th embodiment.Members of frame 3 and corrugated sheet parts 9 are fixed by chimeric.Other structure is identical with the 4th embodiment.
Figure 10 represents the 7th embodiment.Stream formation parts 2 comprise along a plurality of members of frame 3 of the outer rim 1a configuration of barrier film 1 and the tabular corrugated sheet parts of the band shape 9A of configuration between two members of frame 3.Be provided with at the inlet 5 of stream 7, outlet 6 places be used to prevent to enter the mouth 5, the tabular corrugated sheet parts of the band shape 9A of the change of shape of outlet 6.On width (above-below direction of Figure 10), dispose the 4 tabular corrugated sheet parts of band shape 9A.Dispose the tabular corrugated sheet parts of band shape 9A abreast with the formation inlet 5 of triangular portion 34, the limit of outlet 6.Members of frame 3 and the tabular corrugated sheet parts of band shape 9A are fixed by chimeric.The contact site of two the tabular corrugated sheet parts of band shape 9A is fixed by chimeric.Other structure is identical with the 1st embodiment.
Figure 11 represents the 8th embodiment.Stream formation parts 2 comprise along a plurality of members of frame 3 of the outer rim 1a configuration of barrier film 1 and the tabular corrugated sheet parts of the band shape 9A of configuration between two members of frame 3.Be provided with at the inlet 5 of stream 7, outlet 6 places be used to prevent to enter the mouth 5, the tabular corrugated sheet parts of the band shape 9A of the change of shape of outlet 6.Dispose the 4 tabular corrugated sheet parts of band shape 9A at width (above-below direction of Figure 11) with going up the straight line shape, and on length direction (left and right directions of Figure 11), dispose the 5 tabular corrugated sheet parts of band shape 9A.Members of frame 3 and the tabular corrugated sheet parts of band shape 9A are fixed by chimeric.The contact site of two the tabular corrugated sheet parts of band shape 9A is fixed by chimeric.Other structure is identical with the 1st embodiment.
Figure 12 represents the 9th embodiment.Flow direction pars intermedia at stream 7 disposes the tabular corrugated sheet parts of band shape 9A.As the tabular corrugated sheet parts of this band shape 9A, preferably for example has the breach 30 that is used to insert thin flank spare 4 as shown in Figure 17.And, the width dimensions D of the tabular corrugated sheet parts of the band shape 9A of this flow direction pars intermedia 9For example be set at 10mm above, below the 20mm.At width dimensions D 9Under the situation less than lower limit, undercapacity.At gauge D 9Surpass under the situation of higher limit the heat exchanger effectiveness variation.Other structure is identical with the 1st embodiment.
Figure 13 represents the 10th embodiment.Flow direction pars intermedia at stream 7 disposes the tabular corrugated sheet parts of band shape 9A.Other structure is identical with the 2nd embodiment.
In addition, the total-heat exchanger of flow pattern in opposite directions of the present invention (as described above) disposes members of frame 3 or stream formation parts 2 along the whole outer rim 1a of barrier film 1.And, can prevent to enter the mouth 5, outlet 6 produces distortion because of long-term use etc.
Then, Figure 18 and Figure 19 represent the 11st embodiment, and the major part (main composition parts) of positive AC type total-heat exchanger is shown for example.The heat-exchanging part 20 that will have foursquare barrier film 1 and stream formation parts 2 changes 90 ° of phase places and stacked many (omitting the diagram of assembly drawing) successively.
Stream forms that parts 2 have two members of frame 3,3 that outer rim (parallel both sides) 1a, 1a along foursquare barrier film 1 be provided with and at 3,3 thin flank spares 4 by set arranged spaced of this members of frame.The width dimensions D of this thin flank spare 4 4Width dimensions D than members of frame 3 3Little.The heat-exchanging part 20 of Figure 18 and Figure 19 is changed 90 ° of phase places and stacked (diagram omission successively, in addition, with reference to Fig. 1), be used to prevent to enter the mouth 5, the warpage of outlet 6, realize the tabular corrugated sheet parts of band shape (cut-out parts) 9A of the purpose strengthened additional being provided with of the inlet 5 of stream 7, outlet 6 places.
Members of frame 3 and thin flank spare 4 and be with the tabular corrugated sheet parts 9 of shape material, size separately separately identical with described embodiment.
Then, Figure 20 and Figure 21 represent the 12nd embodiment, the major part (main composition parts) of positive AC type total-heat exchanger is shown for example, if the different part of explanation and Figure 18 and Figure 19, be that then stream forms outer rim (parallel both sides) 1a, the 1a setting of parts 2 along barrier film 1, but (replacing members of frame 3) is the thin flank spare 3A of outer rim.Thus, the width dimensions D of the thin flank spare 3A of outer rim 3Width dimensions D with the thin flank spare 4 that disposes abreast betwixt 4Identical.
In Figure 19～21, owing to many bonding the stacking gradually in quadrature shape ground, thin flank spare 4 is at right angles reported to the leadship after accomplishing a task (quadrature), and rigidity and intensity are big, can omit Fig. 2 stirrup 28 shown in the example of passing the imperial examinations at the provincial level, and preferably also can omit substrate 15.
Figure 22 and Figure 23 represent the 13rd embodiment, and the major part (main composition parts) of positive AC type total-heat exchanger is shown for example.The stream of foursquare barrier film 1 and formation stream 7 forms alternately stacked on top of one another (omitting the diagram of assembly drawing) of parts 2.Barrier film 1 and stream form parts 2 and are as a result of got final product by stacked on top of one another alternately.Promptly, stacked method can be that foursquare barrier film 1 and the stream that forms stream 7 are formed parts 2 temporarily as heat-exchanging part 20, heat-exchanging part 20 being changed 90 ° of phase places successively and stacked, perhaps also can be foursquare barrier film 1 and the stream that forms stream 7 to be formed parts 2 (simultaneously stream is formed parts 2 and change 90 ° of phase places successively) alternately laminated separately individually.
Stream forms parts 2 by having the square shaped cross-sectional profile corresponding with barrier film 1 and being formed with (upper surface) area S that accounts for barrier film 1 4More than 70% and the square tabular corrugated sheet parts 90d of the reinforcement usefulness of a plurality of through holes 44 of 95% following scope constitute.Particularly, stream formation parts 2 are made of foursquare tabular corrugated sheet parts 9B.The material of corrugated sheet parts 9 and each size are identical with described embodiment.
Figure 24 represents the 14th embodiment, and stream forms parts 2 and is made of the tabular corrugated sheet parts 9B that is with shape tabular corrugated sheet parts 9A and comb shape shape.In other words, strengthening cutting apart tabular corrugated sheet parts 100 with square tabular corrugated sheet parts 9 by two constitutes.And one that cuts apart in the tabular corrugated sheet parts 100 is (whole and barrier film 1 same size) comb shape shape, and another is that band shape is tabular.Other structure is identical with the 13rd embodiment.
Figure 25 represents the 15th embodiment, and stream forms the tabular corrugated sheet parts 9B formation of parts 2 by two (integral body is half size of barrier film 1) comb shape shapes.In other words, strengthening cutting apart tabular corrugated sheet parts 100 with square tabular corrugated sheet parts 9 by two constitutes.And two cut apart tabular corrugated sheet parts 100 all is the comb shape shape.Other structure is identical with the 13rd embodiment.
The major part (manufacture method 1) of manufacture method of the total-heat exchanger of the 14th embodiment then, is described.
As shown in figure 26, from upper wall surface 16 (with reference to Figure 15, Figure 16), lower wall surface 17, the integrally formed and tabular corrugated sheet parts 9 of 1 Zhang Ping that constitute of a plurality of fins 18 that connect upper wall surface 16 and lower wall surface 17, cut off and make (whole with barrier film 1 same size) two comb shape shapes cut apart 100 one-tenth relative engagement shapes of corrugated sheet parts.That is, cut apart that corrugated sheet parts 100 are for example made by the resin of polyethylene, polypropylene etc. or paper is made or the material of the metal formings such as aluminium that have been shaped etc. forms.Use one of them comb shape shape to cut apart corrugated sheet parts 100 and the band shape of preparing in addition is tabular cuts apart corrugated sheet parts 100 (with reference to Figure 24), formation has the reinforcement with a plurality of through holes 44 of the square shaped cross-sectional profile corresponding with barrier film 1 with square tabular corrugated sheet parts 9, utilizes and strengthens making stream formation parts 2 with square tabular corrugated sheet parts 9.In addition, E represents waste material (useless discarded part) among the figure.
The major part (manufacture method 2) of manufacture method of the total-heat exchanger of the 15th embodiment then, is described.
From upper wall surface 16, lower wall surface 17, the integrally formed and tabular corrugated sheet parts 9 of 1 Zhang Ping that constitute of a plurality of fins 18 that connect upper wall surface 16 and lower wall surface 17, cut off and make the corrugated sheet parts of cutting apart of (size of whole half for barrier film 1) two comb shape shapes mesh shapes relatively for 100 one-tenths.Use these two comb shape shapes to cut apart corrugated sheet parts 100, formation has the reinforcement with a plurality of through holes 44 of the square shaped cross-sectional profile corresponding with barrier film 1 (with reference to Figure 25) with square tabular corrugated sheet parts 9, is that stream formation parts 2 are made on the basis to strengthen with square tabular corrugated sheet parts 9.
The present invention can freely change design, and for example, corrugated sheet parts 9 also can be made of paper, is that upper wall surface 16, lower wall surface 17, a plurality of fins that connect upper wall surface 16 and lower wall surface 17 18 are integrally formed and constitute.And, the quantity of freely-increased/decreased members of frame 3, thin flank spare 4.And quantity, the reinforcement strengthened with the through hole 37 of the tabular corrugated sheet parts of triangular planar 90a also can freely increase and decrease with the quantity of the through hole 39 of hexagon tabular corrugated sheet parts 90c with quantity, the reinforcement of the through hole 38 of quadrangle tabular corrugated sheet parts 90b.And, can freely change shape and the allocation position of the tabular corrugated sheet parts of the band shape 9A of the 7th embodiment (Figure 10), the 8th embodiment (Figure 11).And, preferably be set at air feed littler with the gauge of heat-exchanging part 20B with the gauge of heat-exchanging part 20A than exhaust.In this case, better rate of heat exchange is arranged.
And the shape of cutting apart corrugated sheet parts 100 of the comb shape shape in the manufacture method 1 for example, also can be to cut off tabular corrugated sheet parts 9 and make the length of part of tooth of comb all identical so long as the comb shape shape gets final product.And, the shape of cutting apart corrugated sheet parts 100 of the comb shape shape in the manufacture method 2 so long as the comb shape shape get final product, for example, also can cut off tabular corrugated sheet parts 9, thereby the comb shape shape of length part shortening/prolongation that becomes the part of the tooth that makes comb tails off the quantity of waste material.
[embodiment]
Embodiment 1 makes as follows.That is, the moisture permeable membrane (barrier film 1) that will unite (Rengo) Co., Ltd. exploitation is cut to width dimensions P as illustrated in fig. 3 3Be 390mm, length dimension P 2Be 780mm, the size P of stream portion in opposite directions 1Be the hexagon of 420mm, the heat-exchanging part 20 of the corrugated sheet parts 9 of made members of frame 3 bonding as illustrated in fig. 4, thin flank spare 4 and band shape are tabular.With width dimensions is that 18mm, gauge are that the members of frame 3 of 2mm is bonded on the periphery (outer rim 1a) of hexagonal barrier film 1, is that 4mm, gauge are that 7 thin flank spares 4 of 2mm are bonded in its inboard with width dimensions.With length dimension is that 247mm, width dimensions are that 20mm, gauge are inlet 5, outlet 6 places that the tabular corrugated sheet parts 9 of band shape of 2mm are bonded in wind path (stream 7).The area of the moisture permeable membrane of hexagon shape is 2418cm 2, the gross area of members of frame 3, thin flank spare 4 and the tabular corrugated sheet parts of band shape 9A is about 580cm 2, therefore effectively heat transfer area is 1838cm 2, confirm as 76% of moisture permeable membrane.To strengthen as illustrated in fig. 2 folding 200 layers towards two kinds of different heat-exchanging parts 20, and clip with substrate 15 by reinforcement with replacing the stratum on the substrate 15, fixing at each position, summit C by stirrup 28, make the total-heat exchanger of flow pattern in opposite directions as shown in Figure 1.
Embodiment 2 makes as follows.That is, the moisture permeable membrane with United Co., Ltd's exploitation is cut to width dimensions P as illustrated in fig. 3 3Be 390mm, length dimension P 2Be 780mm, the size P of stream portion in opposite directions 1Be the hexagon of 420mm, made members of frame 3 bonding as illustrated in fig. 5, the heat-exchanging part 20 of thin flank spare 4 and leg-of-mutton tabular corrugated sheet parts 9B.With width dimensions is that 18mm, gauge are that the members of frame 3 of 2mm is bonded on the periphery of hexagonal barrier film 1, is that 4mm, gauge are that the thin flank spare 4 of 2mm is bonded in its inboard with 7 width dimensions.On the tabular corrugated sheet parts 9B of triangle, form the through hole 37 of 60% the scope account for surface area.The area of the moisture permeable membrane of hexagon shape is 2418cm 2, the gross area of members of frame 3, thin flank spare 4 and leg-of-mutton tabular corrugated sheet parts 9B is about 600cm 2, therefore effectively heat transfer area is 1818cm 2, confirm as 75% of moisture permeable membrane.To strengthen as illustrated in fig. 2 folding 200 layers towards two kinds of different heat-exchanging parts 20, and clip with substrate 15 by reinforcement with replacing the stratum on the substrate 15, fixing at each position, summit C by stirrup 28, make the total-heat exchanger of flow pattern in opposite directions as shown in Figure 1.
Embodiment 3 makes as follows.That is, the moisture permeable membrane with United Co., Ltd's exploitation is cut to width dimensions P as illustrated in fig. 3 3Be 390mm, length dimension P 2Be 780mm, the size P of stream portion in opposite directions 1Be the hexagon of 420mm, made members of frame 3 bonding as illustrated in fig. 6, be cut to the heat-exchanging part 20 of triangle and tetragonal tabular corrugated sheet parts 9B.With width dimensions is that 18mm, gauge are that the members of frame 3 of 2mm is bonded on the periphery of hexagonal barrier film 1, and side is packed into and is cut to triangle and tetragonal tabular corrugated sheet parts 9B within it.Be cut on the leg-of-mutton tabular corrugated sheet parts 9B through hole 37 that forms 75% the scope that accounts for surface area.Be cut on the tetragonal tabular corrugated sheet parts 9B through hole 38 that forms 75% the scope that accounts for surface area.The area of the moisture permeable membrane of hexagon shape is 2418cm 2, the gross area of members of frame 3 and tabular corrugated sheet parts 9B is about 720cm 2, therefore effectively heat transfer area is 1698cm 2, confirm as 70% of moisture permeable membrane.To strengthen as illustrated in fig. 2 folding 200 layers towards two kinds of different heat-exchanging parts 20, and clip with substrate 15 by reinforcement with replacing the stratum on the substrate 15, fixing at each position, summit C by stirrup 28, make the total-heat exchanger of flow pattern in opposite directions as shown in Figure 1.In addition, as illustrated in fig. 7 triangle also had identical performance with the total-heat exchanger of flow pattern in opposite directions that tetragonal tabular corrugated sheet parts 9B forms one.
Embodiment 4 makes as follows.That is, produce the members of frame 3 of the total-heat exchanger of flow pattern in opposite directions of embodiment 3 and tabular corrugated sheet parts 9B tabling and incorporate total-heat exchanger.
Embodiment 5 makes as follows.That is, the moisture permeable membrane with United Co., Ltd's exploitation is cut to width dimensions P as illustrated in fig. 3 3Be 390mm, length dimension P 2Be 780mm, the size P of stream portion in opposite directions 1Be the hexagon of 420mm, made members of frame 3 bonding as illustrated in fig. 10 and the heat-exchanging part 20 of the tabular corrugated sheet parts of band shape 9A.With width dimensions is that 18mm, gauge are that the members of frame 3 of 2mm is bonded on the periphery of hexagonal barrier film 1, is that 10mm, gauge are that the thin flank spare of 2mm is bonded in its inboard with 6 width dimensions.With length dimension is that 247mm, width dimensions are that 20mm, gauge are inlet 5, outlet 6 places that the tabular corrugated sheet parts 9B of band shape of 2mm is bonded in wind path.The area of the moisture permeable membrane of hexagon shape is 2418cm 2, the gross area of members of frame 3, thin flank spare 4 and the tabular corrugated sheet parts of band shape 9A is 550cm 2, therefore effectively heat transfer area is 1868cm 2, confirm as 77% of moisture permeable membrane.To strengthen as illustrated in fig. 2 folding 200 layers towards two kinds of different heat-exchanging parts 20, and clip with substrate 15 by reinforcement with replacing the stratum on the substrate 15, fixing at each position, summit C by stirrup 28, make the total-heat exchanger of flow pattern in opposite directions as shown in Figure 1.In addition, will also have identical performance with the total-heat exchanger of flow pattern in opposite directions of the tabular corrugated sheet parts of shape 9A formation one as illustrated in fig. 11.
Embodiment 6 makes as follows.Promptly, the moisture permeable membrane of United Co., Ltd's exploitation is cut to as illustrated in fig. 18 the square of 480mm, with width dimensions is that 9mm, thickness are that the members of frame 3 of 2mm is bonded on the parallel both sides, thin flank spare 4 is also identical with the above embodiments, with same structure the structure phase place of Figure 18 is changed 90 ° and stacked 200 layers.
Comparative example 1 is made as follows.That is, the moisture permeable membrane of United Co., Ltd exploitation is cut on one side as shown in figure 28 be the square of 500mm, the brown paper of making high rigidity carries out the heat-exchanging part that ripple is processed as shown in figure 28.The height of the brown paper after the ripple processing is 2.0mm, and width is 2.5mm, and adhesion width is about 1mm.The area of the moisture permeable membrane of square shape is 2500cm 2, the gross area of adhesive portion is 1000cm 2, therefore effectively heat transfer area is 1500cm 2, confirm as 60% of moisture permeable membrane.With heat-exchanging part as shown in figure 28 with the direction of air-flow orthogonally, alternately stacked 200 layers, and clip by stiffener, fix by stirrup on each summit, make positive AC type total-heat exchanger as shown in figure 28.
Sensible heat exchange efficiency, latent heat exchange efficiency and the full heat exchanger effectiveness of the total-heat exchanger of flow pattern in opposite directions (embodiment 1～5) of the foregoing description and comparative example manufacturing, positive AC type total-heat exchanger (comparative example 1) have been measured.And, measured the pressure loss.The measurement result of the sensible heat exchange efficiency under the air conditions the during heat supply in winter of JIS-B8628 defined, latent heat exchange efficiency and full heat exchanger effectiveness is as shown in table 1.And the measurement result of the sensible heat exchange efficiency under the air conditions when freeze summer, latent heat exchange efficiency and full heat exchanger effectiveness is as shown in table 2.In table 1,2, also put down in writing the measurement result of the pressure loss.
[table 1]
The sensible heat exchange efficiency The latent heat exchange efficiency Full heat exchanger effectiveness The pressure loss
Embodiment
1 88％ 75％ 82％ 40Pa
Embodiment
2 86％ 72％ 80％ 45Pa
Embodiment
3 86％ 72％ 80％ 45Pa
Embodiment
4 86％ 71％ 80％ 45Pa
Embodiment
5 88％ 75％ 82％ 40Pa
Embodiment
6 85％ 70％ 75％ 20Pa
Comparative example 1 65％ 50％ 59％ 120Pa
[table 2]
The sensible heat exchange efficiency The latent heat exchange efficiency Full heat exchanger effectiveness The pressure loss
Embodiment
1 88％ 75％ 80％ 40Pa
Embodiment
2 86％ 72％ 78％ 45Pa
Embodiment
3 86％ 71％ 77％ 45Pa
Embodiment
4 86％ 71％ 76％ 45Pa
Embodiment
5 88％ 74％ 80％ 40Pa
Embodiment
6 85％ 70％ 75％ 20Pa
Comparative example 1 65％ 50％ 53％ 120Pa
According to table 1, table 2, confirm that the sensible heat exchange efficiency of embodiments of the invention is more than 85%, for good, the latent heat exchange efficiency is more than 70%, for good.Full heat exchanger effectiveness is according to air conditions and difference, but affirmation is in embodiment 1～5, and full heat exchanger effectiveness is that full heat exchanger effectiveness is more than 75% under the air conditions more than 80%, when freeze summer under the air conditions during heat supply in winter, is good.On the other hand, the sensible heat exchange efficiency of the embodiment 6 of positive AC type total-heat exchanger, latent heat exchange efficiency and full heat exchanger effectiveness are respectively 85%, 70%, 75%, and be relatively better.But confirm to be respectively about 50%～65% in the comparative example 1 of type in the past, not high.About the pressure loss, confirm that embodiment is below the 60Pa, lower, be roughly 1/2 of comparative example 1.
As mentioned above, the present invention is by barrier film 1 be bonded on the barrier film 1 and total-heat exchanger that the stream that forms stream 7 forms heat-exchanging part 20 stacked on top of one another that parts 2 constitute, carries out heat exchange via the sensible heat and the latent heat of 1 pair of two kinds of gas of barrier film with many, wherein, stream forms parts 2, have a plurality of members of frame 3 of being provided with along the outer rim 1a of barrier film 1 and 3 of two members of frame with set arranged spaced and width dimensions D 4Width dimensions D than members of frame 3 3Little thin flank spare 4, and have at the inlet 5 of stream 7, outlet 6 places be used to prevent to enter the mouth 5, the tabular corrugated sheet parts 9 of band shape (9A) of the change of shape of outlet 6, corrugated sheet parts 9 upper wall surfaces 16, lower wall surface 17 and a plurality of fins 18 that are connected upper wall surface 16 and lower wall surface 17 are shaped integratedly and constitute, therefore, can improve sensible heat exchange efficiency, latent heat exchange efficiency and full heat exchanger effectiveness, and reduce the pressure loss.In long-time use or under the situation of cold place frosting, can prevent the situation that the pressure loss is increased owing to stream 7 change of shape.Particularly, can prevent owing to peristome (inlet 5, outlet 6) distortion makes wind be difficult to situation about rising by (air quantity reduction), deterioration of efficiency or the pressure loss.
And, with many by the barrier film 1 of hexagon shape and be bonded on the barrier film 1 and the stream that forms stream 7 forms heat-exchanging part 20 stacked on top of one another that parts 2 constitute, in the total-heat exchanger of the flow pattern in opposite directions of carrying out heat exchange via the sensible heat and the latent heat of 1 pair of two kinds of gas of barrier film, stream forms parts 2, have a plurality of members of frame 3 of being provided with along the outer rim 1a of barrier film 1 and 3 of two members of frame with set arranged spaced and width dimensions D 4Width dimensions D than members of frame 3 3Little thin flank spare 4, and have and strengthen with the tabular corrugated sheet parts 9 of triangular planar (90a), described reinforcement has with the inlet 5 of stream 7, exports the corresponding triangle profile of the triangular portion 34 of 6 sides and be formed with the area S that accounts for triangular portion 34 with the tabular corrugated sheet parts 9 of triangular planar (90a) 1More than 70% and one or more through holes 37 of 95% following scope, corrugated sheet parts 9 upper wall surfaces 16, lower wall surface 17 and a plurality of fins 18 that are connected upper wall surface 16 and lower wall surface 17 are shaped integratedly and constitute, therefore, can improve sensible heat exchange efficiency, latent heat exchange efficiency and full heat exchanger effectiveness, and reduce the pressure loss.In long-time use or under the situation of cold place frosting, can prevent to make the situation of pressure loss increase because of the change of shape of stream 7.Particularly, can prevent owing to peristome (inlet 5, outlet 6) distortion makes wind be difficult to situation about rising by (air quantity reduction), deterioration of efficiency or the pressure loss.And, can simplify manufacturing process.
And, with many by the barrier film 1 of hexagon shape and be bonded on the barrier film 1 and the stream that forms stream 7 forms heat-exchanging part 20 stacked on top of one another that parts 2 constitute, in the total-heat exchanger of the flow pattern in opposite directions of carrying out heat exchange via the sensible heat and the latent heat of 1 pair of two kinds of gas of barrier film, stream formation parts 2 have: along a plurality of members of frame 3 of the outer rim 1a setting of barrier film 1; Have the triangle profile corresponding and be formed with the area S that accounts for triangular portion 34 with the triangular portion 34 of the inlet 5 of stream 7, outlet 6 sides 1More than 70% and the reinforcement of one or more through holes 37 of 95% following scope with the tabular corrugated sheet parts 9 of triangular planar (90a); And have and by the corresponding quadrangle shape profile of the quadrangle portion that clips of triangular portion 34 35 of inlet 5, outlet 6 sides and be formed with the area S that accounts for quadrangle portion 35 2More than 70% and the reinforcement of one or more through holes 38 of 95% following scope with quadrangle tabular corrugated sheet parts 9 (90b), corrugated sheet parts 9 upper wall surfaces 16, lower wall surface 17 and a plurality of fins 18 that are connected upper wall surface 16 and lower wall surface 17 are shaped integratedly and constitute, therefore, can improve sensible heat exchange efficiency, latent heat exchange efficiency and full heat exchanger effectiveness, and reduce the pressure loss.In long-time use or under the situation of cold place frosting, can prevent to make the situation of pressure loss increase because of the change of shape of stream 7.Particularly, can prevent owing to peristome (inlet 5, outlet 6) distortion makes wind be difficult to situation about rising by (air quantity reduction), deterioration of efficiency or the pressure loss.And, can simplify manufacturing process.
And, with many by the barrier film 1 of hexagon shape and be bonded on the barrier film 1 and the stream that forms stream 7 forms heat-exchanging part 20 stacked on top of one another that parts 2 constitute, in the total-heat exchanger of the flow pattern in opposite directions of carrying out heat exchange via the sensible heat and the latent heat of 1 pair of two kinds of gas of barrier film, stream forms parts 2, has a plurality of members of frame 3 that are provided with along the outer rim 1a of barrier film 1 and have the hexagon shape profile corresponding with the hexagonal portion that clipped by members of frame 3 36 and be formed with to account for hexagonal portion 36 area S 3More than 70% and the reinforcement of one or more through holes 39 of 95% following scope with hexagon tabular corrugated sheet parts 9 (90c), corrugated sheet parts 9 upper wall surfaces 16, lower wall surface 17 and a plurality of fins 18 that are connected upper wall surface 16 and lower wall surface 17 are shaped integratedly and constitute, therefore, can improve sensible heat exchange efficiency, latent heat exchange efficiency and full heat exchanger effectiveness, and reduce the pressure loss.In long-time use or under the situation of cold place frosting, can prevent to make the situation of pressure loss increase because of the change of shape of stream 7.Particularly, can prevent owing to peristome (inlet 5, outlet 6) distortion makes wind be difficult to situation about rising by (air quantity reduction), deterioration of efficiency or the pressure loss.And, can simplify manufacturing process.
And, since with members of frame 3 and corrugated sheet parts 9 by chimeric and fixing, so can prevent the position skew of members of frame 3 and corrugated sheet parts 9, and, can prevent from barrier film 1, to produce wrinkle.And the shape of stream 7 keeps effect to improve, the rising that can be suppressed at long-time use or lose in the situation downforce of cold place frosting.
And, with many by barrier film 1 be bonded on the barrier film 1 and the stream that forms stream 7 forms heat-exchanging part 20 stacked on top of one another that parts 2 constitute, in the total-heat exchanger of the flow pattern in opposite directions of carrying out heat exchange via the sensible heat and the latent heat of 1 pair of two kinds of gas of barrier film, stream forms parts 2, comprise a plurality of members of frame 3 that are provided with along the outer rim 1a of barrier film 1, with the tabular corrugated sheet parts 9 of the band shape that is arranged on 3 of two members of frame (9A), and inlet 5 at stream 7, exporting 6 places has and is used to prevent to enter the mouth 5, the tabular corrugated sheet parts 9 of band shape (9A) of the change of shape of outlet 6, and, pass through members of frame 3 and the band tabular corrugated sheet parts 9 of shape (9A) chimeric and fixing, corrugated sheet parts 9 are upper wall surfaces 16, lower wall surface 17 is shaped integratedly with a plurality of fins 18 that are connected upper wall surface 16 and lower wall surface 17 and constitutes, therefore, can improve the sensible heat exchange efficiency, latent heat exchange efficiency and full heat exchanger effectiveness, and reduce the pressure loss.In long-time use or under the situation of cold place frosting, can prevent to make the situation of pressure loss increase because of the change of shape of stream 7.Particularly, can prevent owing to peristome (inlet 5, outlet 6) distortion makes wind be difficult to situation about rising by (air quantity reduction), deterioration of efficiency or the pressure loss.And, can effectively utilize tabular corrugated sheet parts 9B than higher price.And, can cost degradation.
And, with many by barrier film 1 and be bonded on the barrier film 1 and the stream that forms stream 7 forms heat-exchanging part 20 stacked on top of one another that parts 2 constitute, in the total-heat exchanger of the positive AC type that carries out heat exchange via the sensible heat and the latent heat of 1 pair of two kinds of gas of barrier film, stream forms parts 2, have a plurality of members of frame 3 of being provided with along the outer rim 1a of barrier film 1 and 3 of two members of frame with set arranged spaced and width dimensions D 4Width dimensions D than members of frame 3 3Little thin flank spare 4, and have at the inlet 5 of stream 7, outlet 6 places be used to prevent to enter the mouth 5, the tabular corrugated sheet parts 9 of band shape of the change of shape of outlet 6, corrugated sheet parts 9 upper wall surfaces 16, lower wall surface 17 and a plurality of fins 18 that are connected upper wall surface 16 and lower wall surface 17 are shaped integratedly and constitute, therefore, can improve sensible heat exchange efficiency, latent heat exchange efficiency and full heat exchanger effectiveness, and reduce the pressure loss.In long-time use or under the situation of cold place frosting, can prevent to make the situation of pressure loss increase because of the change of shape of stream 7.Particularly, can prevent owing to peristome (inlet 5, outlet 6) distortion makes wind be difficult to situation about rising by (air quantity reduction), deterioration of efficiency or the pressure loss.
And, with many by barrier film 1 and be bonded on the barrier film 1 and the stream that forms stream 7 forms heat-exchanging part 20 stacked on top of one another that parts 2 constitute, in the total-heat exchanger of the positive AC type that carries out heat exchange via the sensible heat and the latent heat of 1 pair of two kinds of gas of barrier film, stream forms parts 2, have the thin flank spare 3A of outer rim that is provided with along the outer rim 1a of barrier film 1 and between two thin flank spare 3A of outer rim with set arranged spaced and width dimensions D 4Width dimensions D with the thin flank spare 3A of outer rim 3Identical thin flank spare 4, and have at the inlet 5 of stream 7, outlet 6 places be used to prevent to enter the mouth 5, the tabular corrugated sheet parts 9 of band shape of the change of shape of outlet 6, corrugated sheet parts 9 upper wall surfaces 16, lower wall surface 17 and a plurality of fins 18 that are connected upper wall surface 16 and lower wall surface 17 are shaped integratedly and constitute, therefore, can improve sensible heat exchange efficiency, latent heat exchange efficiency and full heat exchanger effectiveness, and reduce the pressure loss.In long-time use or under the situation of cold place frosting, can prevent to make the situation of pressure loss increase because of the change of shape of stream 7.Particularly, can prevent owing to peristome (inlet 5, outlet 6) distortion makes wind be difficult to situation about rising by (air quantity reduction), deterioration of efficiency or the pressure loss.And, make thin flank spare 3A of outer rim and thin flank spare 4 generalizations, can realize the easy of reduction, cost reduction and the stock control etc. of part kind.
And, because the flow direction pars intermedia at stream 7 is provided with the band tabular corrugated sheet parts 9 of shape (9A), thus barrier film 1 is opened tightly, under the situation of long-time use or frosting etc., can alleviate the distortion of barrier film 1, suppress the rising of the pressure loss.
And, with the barrier film 1 of square shape and the stream that forms stream 7 form parts 2 reciprocally stacked on top of one another, carry out heat exchange via the sensible heat and the latent heat of 1 pair of two kinds of gas of barrier film the total-heat exchanger of positive AC type in, stream forms parts 2 by having the square shaped cross-sectional profile corresponding with barrier film 1 and being formed with the area S that accounts for barrier film 1 4More than 70% and the reinforcement of a plurality of through holes 44 of 95% following scope with square tabular corrugated sheet parts 9 formations, corrugated sheet parts 9 upper wall surfaces 16, lower wall surface 17 and a plurality of fins 18 that are connected upper wall surface 16 and lower wall surface 17 are shaped integratedly and constitute, therefore effective heat transfer area of barrier film 1 of removing the bonding portion of corrugated sheet parts 9 reaches more than 80%, and rate of heat exchange is improved.And, can prevent the inlet 5 of stream 7, the change of shape of outlet 6, therefore can reduce the pressure loss, and, suppress the rising of the pressure loss in long-term the use.
And, strengthen constituting by a plurality of tabular corrugated sheet parts 100 of cutting apart with square tabular corrugated sheet parts 9, at least one that cut apart in the tabular corrugated sheet parts 100 is the comb shape shape, therefore, from the tabular corrugated sheet parts 9 of 1 Zhang Ping, cutting off and making the corrugated sheet parts 100 of cutting apart of two comb shape shapes is to mesh shape relatively, can effectively utilize and make tabular corrugated sheet parts 9.
And the fin of corrugated sheet parts 9 forms the linearity or the continuous wave shape of above-below direction, therefore makes simple and good strength.
And, be that the stream that will form barrier film 1 and stream 7 forms alternately stacked on top of one another of parts 2, the manufacture method of the total-heat exchanger of the positive AC type that carries out heat exchange via the sensible heat and the latent heat of 1 pair of two kinds of gas of barrier film, wherein, from upper wall surface 16, lower wall surface 17 is the tabular corrugated sheet parts 9 of 1 Zhang Ping that constitute with being connected that the upper wall surface 16 a plurality of fins 18 with lower wall surface 17 are shaped integratedly, cutting off and making the corrugated sheet parts 100 of cutting apart of two comb shape shapes is to mesh shape relatively, corrugated sheet parts 100 are cut apart in use, the reinforcement with a plurality of through holes 44 that formation has a square shaped cross-sectional profile corresponding with barrier film 1 is with square tabular corrugated sheet parts 9, to strengthen with square tabular corrugated sheet parts 9 is that stream formation parts 2 are made on the basis, therefore, can effectively utilize tabular corrugated sheet parts 9 (can reduce waste material E).And can reduce manufacturing cost.

Claims (13)

1. total-heat exchanger, with many by barrier film (1) be bonded in that this barrier film (1) is gone up and the stream that forms stream (7) forms heat-exchanging part (20) stacked on top of one another of parts (2) formation, via this barrier film (1) sensible heat and the latent heat of two kinds of gases carried out heat exchange, it is characterized in that
Above-mentioned stream forms parts (2), have a plurality of members of frame (3) of being provided with along the outer rim (1a) of above-mentioned barrier film (1) and between two these members of frame (3) with set arranged spaced and width dimensions (D 4) than the width dimensions (D of this members of frame (3) 3) little thin flank spare (4), and the tabular corrugated sheet parts of band shape (9) of locating to have the change of shape that is used to prevent this inlet (5), outlet (6) in the inlet (5) of above-mentioned stream (7), outlet (6),
Above-mentioned corrugated sheet parts (9) upper wall surfaces (16), lower wall surface (17) and a plurality of fins (18) that are connected this upper wall surface (16) and lower wall surface (17) are shaped integratedly and constitute.
2. total-heat exchanger of flow pattern in opposite directions, with many barrier films (1) be bonded in that this barrier film (1) is gone up and the stream that forms stream (7) forms heat-exchanging part (20) stacked on top of one another of parts (2) formation, via this barrier film (1) sensible heat and the latent heat of two kinds of gases carried out heat exchange by the hexagon shape, it is characterized in that
Above-mentioned stream forms parts (2), have a plurality of members of frame (3) of being provided with along the outer rim (1a) of above-mentioned barrier film (1) and between two these members of frame (3) with set arranged spaced and width dimensions (D 4) than the width dimensions (D of this members of frame (3) 3) little thin flank spare (4), and comprise having the triangle profile corresponding and be formed with the area (S that accounts for above-mentioned triangular portion (34) with the triangular portion (34) of the inlet (5) of above-mentioned stream (7), outlet (6) side 1) more than 70% and the reinforcement of one or more through holes (37) of 95% following scope with the tabular corrugated sheet parts of triangular planar (9),
Above-mentioned corrugated sheet parts (9) upper wall surfaces (16), lower wall surface (17) and a plurality of fins (18) that are connected this upper wall surface (16) and lower wall surface (17) are shaped integratedly and constitute.
3. total-heat exchanger of flow pattern in opposite directions, with many barrier films (1) be bonded in that this barrier film (1) is gone up and the stream that forms stream (7) forms heat-exchanging part (20) stacked on top of one another of parts (2) formation, via this barrier film (1) sensible heat and the latent heat of two kinds of gases carried out heat exchange by the hexagon shape, it is characterized in that
Above-mentioned stream forms parts (2) to have: a plurality of members of frame (3) that are provided with along the outer rim (1a) of above-mentioned barrier film (1); Have the triangle profile corresponding and be formed with the area (S that accounts for above-mentioned triangular portion (34) with the triangular portion (34) of the inlet (5) of above-mentioned stream (7), outlet (6) side 1) more than 70% and the reinforcement of one or more through holes (37) of 95% following scope with the tabular corrugated sheet parts of triangular planar (9); And have with by the corresponding quadrangle shape profile of the quadrangle portion (35) that clipped of triangular portion (34) of above-mentioned inlet (5), outlet (6) side and be formed with the area (S that accounts for above-mentioned quadrangle portion (34) 2) more than 70% and the reinforcement of one or more through holes (38) of 95% following scope with quadrangle tabular corrugated sheet parts (9),
Above-mentioned corrugated sheet parts (9) upper wall surfaces (16), lower wall surface (17) and a plurality of fins (18) that are connected this upper wall surface (16) and lower wall surface (17) are shaped integratedly and constitute.
4. total-heat exchanger of flow pattern in opposite directions, with many barrier films (1) be bonded in that this barrier film (1) is gone up and the stream that forms stream (7) forms heat-exchanging part (20) stacked on top of one another of parts (2) formation, via this barrier film (1) sensible heat and the latent heat of two kinds of gases carried out heat exchange by the hexagon shape, it is characterized in that
Above-mentioned stream forms parts (2), has a plurality of members of frame (3) that are provided with along the outer rim (1a) of above-mentioned barrier film (1) and have the hexagon shape profile corresponding with the hexagonal portion (36) that is clipped by above-mentioned members of frame (3) and be formed with to account for above-mentioned hexagonal portion (36) area (S 3) more than 70% and the reinforcement of one or more through holes (39) of 95% following scope with hexagon tabular corrugated sheet parts (9),
Above-mentioned corrugated sheet parts (9) upper wall surfaces (16), lower wall surface (17) and a plurality of fins (18) that are connected this upper wall surface (16) and lower wall surface (17) are shaped integratedly and constitute.
5. as claim 3 or 4 described total-heat exchangers, it is characterized in that above-mentioned members of frame (3) and above-mentioned corrugated sheet parts (9) are by chimeric and fixing.
6. total-heat exchanger of flow pattern in opposite directions, with many by barrier film (1) be bonded in that this barrier film (1) is gone up and the stream that forms stream (7) forms heat-exchanging part (20) stacked on top of one another of parts (2) formation, via this barrier film (1) sensible heat and the latent heat of two kinds of gases carried out heat exchange, it is characterized in that
Above-mentioned stream forms parts (2), comprise a plurality of members of frame (3) that are provided with along the outer rim (1a) of above-mentioned barrier film (1) and be arranged on tabular corrugated sheet parts of band shape (9) between two these members of frame (3), and inlet (5), outlet (6) in above-mentioned stream (7) locate to have the tabular corrugated sheet parts of band shape (9) that are used to prevent this inlet (5), export the change of shape of (6), and, pass through above-mentioned members of frame (3) and the tabular corrugated sheet parts of above-mentioned band shape (9) chimeric and fixing
Above-mentioned corrugated sheet parts (9) upper wall surfaces (16), lower wall surface (17) and a plurality of fins (18) that are connected this upper wall surface (16) and lower wall surface (17) are shaped integratedly and constitute.
7. total-heat exchanger as claimed in claim 1 or 2 is characterized in that, is provided with the band tabular corrugated sheet parts of shape (9) at the flow direction pars intermedia of stream (7).
8. the total-heat exchanger of a positive AC type, with many by barrier film (1) be bonded in that this barrier film (1) is gone up and the stream that forms stream (7) forms heat-exchanging part (20) stacked on top of one another of parts (2) formation, via this barrier film (1) sensible heat and the latent heat of two kinds of gases carried out heat exchange, it is characterized in that
Above-mentioned stream forms parts (2), have a plurality of members of frame (3) of being provided with along the outer rim (1a) of above-mentioned barrier film (1) and between two these members of frame (3) with set arranged spaced and width dimensions (D 4) than the width dimensions (D of this members of frame (3) 3) little thin flank spare (4), and the tabular corrugated sheet parts of band shape (9) of locating to have the change of shape that is used to prevent this inlet (5), outlet (6) in the inlet (5) of above-mentioned stream (7), outlet (6),
Above-mentioned corrugated sheet parts (9) upper wall surfaces (16), lower wall surface (17) and a plurality of fins (18) that are connected this upper wall surface (16) and lower wall surface (17) are shaped integratedly and constitute.
9. the total-heat exchanger of a positive AC type, with many by barrier film (1) be bonded in that this barrier film (1) is gone up and the stream that forms stream (7) forms heat-exchanging part (20) stacked on top of one another of parts (2) formation, via this barrier film (1) sensible heat and the latent heat of two kinds of gases carried out heat exchange, it is characterized in that
Above-mentioned stream forms parts (2), have the thin flank spare of outer rim (3A) that is provided with along the outer rim (1a) of above-mentioned barrier film (1) and between two thin flank spares of this outer rim (3A) with set arranged spaced and width dimensions (D 4) with the width dimensions (D of the thin flank spare of this outer rim (3A) 3) identical thin flank spare (4), and the tabular corrugated sheet parts of band shape (9) of locating to have the change of shape that is used to prevent this inlet (5), outlet (6) in the inlet (5) of above-mentioned stream (7), outlet (6),
Above-mentioned corrugated sheet parts (9) upper wall surfaces (16), lower wall surface (17) and a plurality of fins (18) that are connected this upper wall surface (16) and lower wall surface (17) are shaped integratedly and constitute.
10. the total-heat exchanger of a positive AC type, with foursquare barrier film (1) and the stream that forms stream (7) form parts (2) alternately stacked on top of one another, via this barrier film (1) sensible heat and the latent heat of two kinds of gases is carried out heat exchange, it is characterized in that,
Above-mentioned stream forms parts (2) by having the square shaped cross-sectional profile corresponding with above-mentioned barrier film (1) and being formed with the area (S that accounts for above-mentioned barrier film (1) 4) more than 70% and the reinforcement of a plurality of through holes (44) of 95% following scope with square tabular corrugated sheet parts (9) formation,
Above-mentioned corrugated sheet parts (9) upper wall surfaces (16), lower wall surface (17) and a plurality of fins (18) that are connected this upper wall surface (16) and lower wall surface (17) are shaped integratedly and constitute.
11. total-heat exchanger as claimed in claim 10, it is characterized in that, above-mentioned reinforcement is made of a plurality of tabular corrugated sheet parts (100) of cutting apart with square tabular corrugated sheet parts (9), and above-mentioned at least one that cut apart in the tabular corrugated sheet parts (100) is the comb shape shape.
12., it is characterized in that the fin (18) of above-mentioned corrugated sheet parts (9) forms the linearity or the continuous wave shape of above-below direction as claim 1,2,3,4,5,6,7,8,10 or 11 described total-heat exchangers.
The manufacture method of the total-heat exchanger of 13 1 kinds of positive AC types, described positive AC type total-heat exchanger with barrier film (1) and the stream that forms stream (7) form parts (2) alternately stacked on top of one another, via this barrier film (1) sensible heat and the latent heat of two kinds of gases is carried out heat exchange, this manufacture method is characterised in that
From upper wall surface (16), lower wall surface (17) is shaped integratedly with a plurality of fins (18) that are connected this upper wall surface (16) and lower wall surface (17) and the tabular corrugated sheet parts of 1 Zhang Ping (9) that constitute, cutting off and making the corrugated sheet parts (100) of cutting apart of two comb shape shapes is to mesh shape relatively, use this to cut apart corrugated sheet parts (100), formation has the reinforcement with a plurality of through holes (44) of the square shaped cross-sectional profile corresponding with above-mentioned barrier film (1) with square tabular corrugated sheet parts (9), utilizes this reinforcement to make above-mentioned stream with square tabular corrugated sheet parts (9) and forms parts (2).
CN2008100044752A 2007-03-14 2008-01-30 Total-heat exchanger and manufacturing method thereof Expired - Fee Related CN101266109B (en)

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Families Citing this family (15)

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Family Cites Families (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS54119153A (en) * 1978-03-08 1979-09-14 Mitsubishi Electric Corp Manufacture of heat exchange devices for air conditioning
JPH08291990A (en) * 1995-04-24 1996-11-05 Matsushita Seiko Co Ltd Heat-exchanger element
JP3577863B2 (en) * 1996-09-10 2004-10-20 三菱電機株式会社 Counter-flow heat exchanger
JPH11201683A (en) * 1998-01-13 1999-07-30 Daikin Ind Ltd Heat exchanging element
JP3404282B2 (en) * 1998-02-17 2003-05-06 三菱電機株式会社 Heat exchange element
JP4078709B2 (en) * 1998-03-20 2008-04-23 ダイキン工業株式会社 Heat exchange element with purification function
JP2003262487A (en) * 2002-01-07 2003-09-19 Daikin Ind Ltd Heat exchange element
JP3873795B2 (en) * 2002-04-01 2007-01-24 ダイキン工業株式会社 Air flow element
JP2005155996A (en) * 2003-11-25 2005-06-16 Nissan Motor Co Ltd Heat exchanger
JP4466156B2 (en) * 2004-03-29 2010-05-26 パナソニック株式会社 Heat exchanger
JP2006002982A (en) * 2004-06-16 2006-01-05 Nitta Ind Corp Heat exchanging element
JP2006029692A (en) * 2004-07-16 2006-02-02 Matsushita Electric Ind Co Ltd Heat exchanger
CN2755547Y (en) * 2004-12-07 2006-02-01 周登利 Heat recovery exchanger

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