CN105091630A - Heat exchanger and heat exchanging unit - Google Patents
Heat exchanger and heat exchanging unit Download PDFInfo
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- CN105091630A CN105091630A CN201510169406.7A CN201510169406A CN105091630A CN 105091630 A CN105091630 A CN 105091630A CN 201510169406 A CN201510169406 A CN 201510169406A CN 105091630 A CN105091630 A CN 105091630A
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- China
- Prior art keywords
- heat
- exchange tube
- sheet material
- junction surface
- flow path
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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Classifications
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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
- F28D9/0093—Multi-circuit heat-exchangers, e.g. integrating different heat exchange sections in the same unit or heat-exchangers for more than two fluids
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D1/00—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators
- F28D1/02—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid
- F28D1/03—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with plate-like or laminated conduits
- F28D1/0308—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with plate-like or laminated conduits the conduits being formed by paired plates touching each other
- F28D1/0325—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with plate-like or laminated conduits the conduits being formed by paired plates touching each other the plates having lateral openings therein for circulation of the heat-exchange medium from one conduit to another
- F28D1/0333—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with plate-like or laminated conduits the conduits being formed by paired plates touching each other the plates having lateral openings therein for circulation of the heat-exchange medium from one conduit to another the plates having integrated connecting members
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D1/00—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators
- F28D1/02—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid
- F28D1/04—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits
- F28D1/053—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits the conduits being straight
- F28D1/0535—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits the conduits being straight the conduits having a non-circular cross-section
- F28D1/05358—Assemblies of conduits connected side by side or with individual headers, e.g. section type radiators
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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)
- Details Of Heat-Exchange And Heat-Transfer (AREA)
Abstract
The invention provides a heat exchanger and heat exchanging unit. The heat exchanger has a plurality of heat exchanger tubes. Each heat exchanger tube has an internal flow path through which a first fluid flows. These heat exchanger tubes are arranged so that an external flow path, through which a second fluid that exchanges heat with the first fluid flows, is formed between each two adjacent heat exchanger tubes. Each two adjacent heat exchanger tubes are bonded together at the inlets and outlets of the internal flow paths in the two heat exchanger tubes. One of each two adjacent heat exchanger tubes is offset with respect to the other heat exchanger tube in a direction perpendicular to an arrangement direction in which these heat exchanger tubes are arranged.
Description
Technical field
The present invention relates to heat exchanger and heat exchange unit.
Background technology
As shown in figure 13, patent document 1 discloses a kind of heat exchanger 101 with multiple heat-exchange tube 102.Heat-exchange tube 102 is formed by carrying out bending machining to 1 sheet material, has central portion 102A, widening portion 102B and widening portion 102C.Central portion 102A is flat and be tubulose.Widening portion 102B and widening portion 102C at the two ends of heat-exchange tube 102 with the thickness opening of about 2 ~ 4 of central portion 102A times.Outside stream is formed between adjacent heat-exchange tube 102.Patent document 1 records: heat-exchange tube 102 can have sinuous refrigerant flow path, and sinuous refrigerant flow path can by spaced apart.
Prior art document
Patent document 1: Japanese Unexamined Patent Publication 2008-39322 publication
Summary of the invention
The invention provides a kind of technology of the performance for improving the heat exchanger be made up of heat-exchange tube.
That is, the present invention is a kind of heat exchanger, possesses:
Multiple flat heat-exchange tube, it has the internal flow path for the 1st fluid flowing respectively; With
Multiple outside stream, it is between adjacent described heat-exchange tube, supplies the 2nd fluid carrying out heat exchange with described 1st fluid to flow,
Described multiple heat-exchange tube is engaged with each other at the entrance and exit place of described internal flow path,
One side of heat-exchange tube described in adjacent 1 group relative to the opposing party at the direction upper offset vertical with the orientation of described multiple heat-exchange tube,
Described heat-exchange tube comprises the 1st sheet material and the 2nd sheet material of fitting each other,
When the outer surface of described 1st sheet material being defined as the 1st interarea, the outer surface of described 2nd sheet material being defined as the 2nd interarea,
Described 1st sheet material has the 1st entrance junction surface being positioned at described 1st interarea and exports junction surface as the part for being engaged with each other by adjacent described heat-exchange tube with the be positioned at described 1st interarea the 1st,
Described 2nd sheet material has the 2nd entrance junction surface being positioned at described 2nd interarea and exports junction surface as the part for being engaged with each other by adjacent described heat-exchange tube with the be positioned at described 2nd interarea the 2nd,
Described 1st entrance junction surface is in the position of the relative edge near described heat-exchange tube with described 1st outlet junction surface, and described 2nd entrance junction surface is in the position of the relative described edge away from described heat-exchange tube with described 2nd outlet junction surface.
According to above-mentioned technology, the performance of the heat exchanger be made up of heat-exchange tube can be improved.
Accompanying drawing explanation
Fig. 1 is the stereogram of the heat exchanger of the 1st embodiment of the present invention.
Fig. 2 A is the exploded perspective view of the heat-exchange tube that the heat exchanger of the 1st embodiment uses.
Fig. 2 B is the top view of the heat-exchange tube shown in Fig. 2 A.
Fig. 2 C is the sectional view of the heat exchanger of the 1st embodiment.
Fig. 3 A is the use of the structure chart of the heat exchange unit of heat exchanger in the past.
Fig. 3 B is the use of the structure chart of the heat exchange unit of the heat exchanger of the 1st embodiment.
Fig. 4 A is the sectional view of the heat exchanger of variation 1.
Fig. 4 B is the exploded perspective view of the 2nd heat-exchange tube.
Fig. 4 C is the sectional view of the 2nd heat-exchange tube.
Fig. 5 A is the sectional view of the heat exchanger of variation 2.
Fig. 5 B is the exploded perspective view of the heat-exchange tube that the heat exchanger of variation 2 uses.
Fig. 6 A is the sectional view of the heat exchanger of variation 3.
Fig. 6 B is the top view of the heat-exchange tube that the heat exchanger of variation 3 uses.
Fig. 7 A is the sectional view of the heat exchanger of variation 4.
Fig. 7 B is the sectional view of the heat exchanger of variation 5.
Fig. 8 is the sectional view of the heat exchanger of the 2nd embodiment of the present invention.
Fig. 9 is the stereogram of the heat exchanger of the 3rd embodiment of the present invention.
Figure 10 A is the stereogram of the heat-exchange tube that the heat exchanger of the 3rd embodiment uses.
Figure 10 B is the sectional view of the heat exchanger of the 3rd embodiment.
Figure 10 C is the sectional view of the coupling member that the heat exchanger of the 3rd embodiment uses.
Figure 10 D is the use of the partial sectional view of the heat exchanger of the duplexer of coupling member.
Figure 10 E is the use of the partial sectional view of the heat exchanger of multiple coupling members with configurations differing from one.
Figure 11 A is the stereogram of the heat-exchange tube that the heat exchanger of variation 6 uses.
Figure 11 B is the sectional view of the heat exchanger of variation 6.
Figure 11 C is the sectional view of the coupling member that the heat exchanger of variation 6 uses.
Figure 12 is the use of the structure chart of the heat exchange unit of the heat exchanger of the 3rd embodiment.
Figure 13 is the stereogram of heat exchanger in the past.
Label declaration
1,1A, 1C, 1D, 1E, 1F, 1G, 1H, 1J heat exchanger
2,2C, 2D, 2E, 2F, 2G, 2H heat-exchange tube
2A the 1st heat-exchange tube
2B the 2nd heat-exchange tube
2f leading edge
3 internal flow paths
3a entrance
3b exports
4 ~ 7,24 ~ 27 junction surfaces
8 outside streams
8a intake section
8b exit portion
11,41 the 1st sheet materials
11p the 1st interarea
12,42 the 2nd sheet materials
12p the 2nd interarea
14 inlet faces
16 pressure fan
17 the 3rd sheet materials
17p the 3rd interarea
18 the 4th sheet materials
18p the 4th interarea
29 protuberances
44,45 thinner wall section
44h, 45h through hole
46 ~ 48 stream forming portions
51 ~ 57 sections
71 sheet materials
71p, 71q link surface
70,72,73 coupling members
73s body
73t protuberance
200,202 heat exchange units
Detailed description of the invention
In patent document 1, when supplying to give air from incline direction heat exchanger 101, in the stripping of the intake section generation air stream of outside stream, can produce and contributive heat-transfer area do not had to heat exchange.In addition, the flow of the air in outside stream reduces because of the increase of kinetic pressure losses.Its result, causes the decline of the ability of heat exchanger 101 and the increase wanting demanded driving force of pressure fan.And then, if the angle that the inflow direction of the air direction parallel relative to the central portion 102A with flat is exceedes about 40 degree, then can produce the wind noise caused by the stripping of air stream.In the purposes such as conditioner, also there is the performance of forcing to sacrifice heat exchanger and the flow velocity and carrying out reducing air situation about operating.Such problem is easily subject to producing when strictly limiting at the position relationship of pressure fan and heat exchanger as ceiling cell type indoor set.Based on above-mentioned opinion, the present inventor contemplates the invention of each technical scheme of following explanation.
The heat exchanger of the 1st technical scheme of the present invention, possesses:
Multiple flat heat-exchange tube, it has the internal flow path for the 1st fluid flowing respectively; With
Multiple outside stream, it is between adjacent described heat-exchange tube, supplies the 2nd fluid carrying out heat exchange with described 1st fluid to flow,
Described multiple heat-exchange tube is engaged with each other at the entrance and exit place of described internal flow path,
One side of heat-exchange tube described in adjacent 1 group relative to the opposing party at the direction upper offset vertical with the orientation of described multiple heat-exchange tube,
Described heat-exchange tube comprises the 1st sheet material and the 2nd sheet material of fitting each other,
When the outer surface of described 1st sheet material being defined as the 1st interarea, the outer surface of described 2nd sheet material being defined as the 2nd interarea,
As the part for being engaged with each other by adjacent described heat-exchange tube, described 1st sheet material has the 1st entrance junction surface being positioned at described 1st interarea and the 1st outlet junction surface being positioned at described 1st interarea,
As the part for being engaged with each other by adjacent described heat-exchange tube, described 2nd sheet material has the 2nd entrance junction surface being positioned at described 2nd interarea and the 2nd outlet junction surface being positioned at described 2nd interarea,
Described 1st entrance junction surface is in the position of the relative edge near described heat-exchange tube with described 1st outlet junction surface, and described 2nd entrance junction surface is in the position of the relative described edge away from described heat-exchange tube with described 2nd outlet junction surface.
According to the 1st technical scheme, the angle that the inflow direction of the 2nd fluid is consistent with the flow direction of the 2nd fluid in outside stream or both reducing be can be made.In the front and back of the inlet face of heat exchanger, the flow direction of the 2nd fluid changes hardly.In this case, the stripping of the 2nd fluid stream can be suppressed, also be not easy to produce the large pressure loss.Therefore, the performance of heat exchanger can be given full play to.
In addition, according to the 1st technical scheme, described heat-exchange tube comprises the 1st sheet material and the 2nd sheet material of fitting each other.Therefore, it is possible to realize the thin-walled property of heat-exchange tube, be conducive to the miniaturization of heat exchanger.
And then, according to the 1st technical scheme, described 1st sheet material has the 1st entrance junction surface being positioned at described 1st interarea and exports junction surface as the part for being engaged with each other by adjacent described heat-exchange tube with the be positioned at described 1st interarea the 1st, described 2nd sheet material has the 2nd entrance junction surface being positioned at described 2nd interarea and exports junction surface as the part for being engaged with each other by adjacent described heat-exchange tube with the be positioned at described 2nd interarea the 2nd, described 1st entrance junction surface is in the position of the relative edge near described heat-exchange tube with described 1st outlet junction surface, described 2nd entrance junction surface is in the position of the relative described edge away from described heat-exchange tube with described 2nd outlet junction surface.According to such structure, the biased configuration of multiple heat-exchange tube can not only be formed, the broad degree of outside stream can also be specified by structure.
In the 2nd technical scheme, such as, described multiple heat-exchange tube of the heat exchanger of the 1st technical scheme can comprise multiple 1st heat-exchange tube and multiple 2nd heat-exchange tube, the structure of described 1st heat-exchange tube can be different from the structure of described 2nd heat-exchange tube, and described 1st heat-exchange tube and described 2nd heat-exchange tube can be adjacent in described orientation.If the 1st heat-exchange tube and the 2nd heat-exchange tube are combinationally used, even if then when the restriction of the broad degree equidimension of amount of bias, outside stream is strict, also the easy angle of inclination by the inlet face of heat exchanger is adjusted to best angle.That is, according to this variation, the free degree of the design of heat exchanger uprises.
In the 3rd technical scheme, such as, described 1st heat-exchange tube of the heat exchanger of the 2nd technical scheme can comprise the 1st sheet material and the 2nd sheet material of fitting each other, the outer surface of described 1st sheet material is being defined as the 1st interarea, when the outer surface of described 2nd sheet material is defined as the 2nd interarea, described 1st sheet material can have the 1st entrance junction surface being positioned at described 1st interarea and export junction surface as the part for being engaged with each other by adjacent described heat-exchange tube with the be positioned at described 1st interarea the 1st, described 2nd sheet material can have the 2nd entrance junction surface being positioned at described 2nd interarea and export junction surface as the part for being engaged with each other by adjacent described heat-exchange tube with the be positioned at described 2nd interarea the 2nd, described 1st entrance junction surface can be in the position of the relative edge near described 1st heat-exchange tube with described 1st outlet junction surface, described 2nd entrance junction surface can be in the position of the relative described edge away from described 1st heat-exchange tube with described 2nd outlet junction surface, described 2nd heat-exchange tube can comprise the 3rd sheet material and the 4th sheet material of fitting each other, the outer surface of described 3rd sheet material is being defined as the 3rd interarea, when the outer surface of described 4th sheet material is defined as the 4th interarea, described 3rd sheet material can have the 3rd entrance junction surface being positioned at described 3rd interarea and export junction surface as the part for being engaged with each other by adjacent described heat-exchange tube with the be positioned at described 3rd interarea the 3rd, described 4th sheet material can have the 4th entrance junction surface being positioned at described 4th interarea and export junction surface as the part for being engaged with each other by adjacent described heat-exchange tube with the be positioned at described 4th interarea the 4th, in the face vertical with the described orientation of described multiple heat-exchange tube, the position at described 3rd entrance junction surface and the position at described 3rd outlet junction surface can export the position consistency at junction surface with the position and the described 4th at described 4th entrance junction surface respectively.According to such structure, the biased configuration of multiple heat-exchange tube can not only be formed, the broad degree of outside stream can also be specified.
In the 4th technical scheme, such as, described 3rd sheet material of the heat exchanger of the 1st technical scheme can be the component with the shape identical with described 4th sheet material.According to the 4th technical scheme, the reduction of the cost realized by the reduction of number of components can be expected.
In the 5th technical scheme, such as, can be the component with the shape identical with described 1st sheet material or described 2nd sheet material from described 3rd sheet material of the heat exchanger of the 3rd technical scheme or the 4th technical scheme with at least 1 side that described 4th sheet material is selected.According to the 5th technical scheme, the reduction of the cost realized by the reduction of number of components can be expected.
In the 6th technical scheme, such as, in 1st technical scheme ~ the 5th technical scheme, the described internal flow path of the heat exchanger of arbitrary technical scheme can have multiple sections that extend on the specific column direction of described heat-exchange tube, described heat-exchange tube can also have: (i) multiple flow path portion, its both sides to the thickness direction of described heat-exchange tube are outstanding, respectively provide described section of described internal flow path, (ii) thinner wall section, its on the width vertical with described column direction between adjacent described flow path portion and described flow path portion, spaced with described section by described section of described internal flow path along described column direction, in the cross section vertical with described column direction, the described flow path portion of the described heat-exchange tube of the side selected from heat-exchange tube described in adjacent 1 group can be relative with the described thinner wall section of the described heat-exchange tube of the opposing party across described outside stream, and the described flow path portion of the described heat-exchange tube of the opposing party can be relative with the described thinner wall section of the described heat-exchange tube of a side across described outside stream, described multiple flow path portion of described multiple flow path portion of the described heat-exchange tube of one side and the described heat-exchange tube of the opposing party can be arranged in staggered on described width.According to such structure, the broad degree of the outside stream on the thickness direction of heat-exchange tube is roughly certain in the upper maintenance of the width (flow direction of the 2nd fluid) of heat-exchange tube.Its result, can reduce the pressure loss of the 2nd fluid in outside stream.In addition, the stacked spacing of heat-exchange tube can be reduced and expand the heat transfer area of per unit volume.And then, the stripping of the 2nd fluid stream of the surface of heat-exchange tube can be suppressed and expand effective heat transfer area.
The heat exchange unit of the 7th technical scheme of the present invention possesses: pressure fan, it impeller possessing rotating shaft and be fixed on described rotating shaft; With the heat exchanger in the 1st technical scheme ~ the 6th technical scheme described in arbitrary technical scheme, its with the face of described rotational axis vertical in be configured in around described pressure fan, by the rotation of described impeller, the circumferencial direction towards described rotating shaft sends described 2nd fluid to described pressure fan, in described multiple outside stream, when observing from described rotating shaft, the downstream of described outside stream lays respectively at upstream side than described outside stream by the front in the direction of rotation of described rotating shaft.According to the 7th technical scheme, the configuration optimization of heat-exchange tube can be made relative to the swirling flow from centrifugal blower.Thus, the pressure loss reduces, and heat exchanger effectiveness improves.7th technical scheme is especially applicable to ceiling cell type indoor set.
The heat exchanger of the 8th technical scheme of the present invention possesses: multiple flat heat-exchange tube, and it has the internal flow path for the 1st fluid flowing respectively; with multiple outside stream, it is between adjacent described heat-exchange tube, the 2nd fluid carrying out heat exchange with described 1st fluid is supplied to flow, described multiple heat-exchange tube is engaged with each other at the entrance and exit place of described internal flow path, one side of heat-exchange tube described in adjacent 1 group relative to the opposing party at the direction upper offset vertical with the orientation of described multiple heat-exchange tube, described heat-exchange tube comprises the 1st sheet material and the 2nd sheet material of fitting each other, the outer surface of described 1st sheet material is being defined as the 1st interarea, when the outer surface of described 2nd sheet material is defined as the 2nd interarea, described 1st sheet material has at the 1st junction surface of described 1st interarea setting as the part for being engaged with each other by adjacent described heat-exchange tube, described 2nd sheet material has at the 2nd junction surface of described 2nd interarea setting as the part for being engaged with each other by adjacent described heat-exchange tube, the composition surface that described 1st junction surface engages with described 2nd junction surface tilts relative to the direction vertical with the described orientation of described multiple heat-exchange tube, the axle at described 1st junction surface and the axle at described 2nd junction surface tilt relative to the described orientation of described multiple heat-exchange tube.
According to the 8th technical scheme, can make the inflow direction of the 2nd fluid consistent with the flow direction of the 2nd fluid in outside stream or reduce both be angle.In the front and back of the inlet face of heat exchanger, the flow direction of the 2nd fluid changes hardly.In this case, the stripping of the flowing of the 2nd fluid can be suppressed, also be not easy to produce the large pressure loss.Therefore, it is possible to give full play to the performance of heat exchanger.
In addition, according to the 8th technical scheme, described heat-exchange tube comprises the 1st sheet material and the 2nd sheet material of fitting each other.Therefore, it is possible to realize the thin-walled property of heat-exchange tube, be conducive to the miniaturization of heat exchanger.
And then, according to the 8th technical scheme, the outer surface of described 1st sheet material is being defined as the 1st interarea, when the outer surface of described 2nd sheet material is defined as the 2nd interarea, described 1st sheet material have be arranged at described 1st interarea the 1st junction surface as the part for adjacent described heat-exchange tube is engaged with each other, described 2nd sheet material have be arranged at described 2nd interarea the 2nd junction surface as the part for adjacent described heat-exchange tube is engaged with each other, the composition surface that described 1st junction surface engages with described 2nd junction surface tilts relative to the direction vertical with the described orientation of described multiple heat-exchange tube, the axle at described 1st junction surface and the axle at described 2nd junction surface tilt relative to the described orientation of described multiple heat-exchange tube.Therefore, it is possible to make multiple heat-exchange tube offset with respect to each in the direction of the width.
In the 9th technical scheme, such as, the described internal flow path of the heat exchanger of the 8th technical scheme can have multiple sections that extend on the specific column direction of described heat-exchange tube, described heat-exchange tube can also have: (i) multiple flow path portion, its both sides to the thickness direction of described heat-exchange tube are outstanding, respectively provide described section of described internal flow path, (ii) thinner wall section, its on the width vertical with described column direction between adjacent described flow path portion and described flow path portion, spaced with described section by described section of described internal flow path along described column direction, in the cross section vertical with described column direction, the described flow path portion of the described heat-exchange tube of the side selected from heat-exchange tube described in adjacent 1 group can be relative with the described thinner wall section of the described heat-exchange tube of the opposing party across described outside stream, and the described flow path portion of the described heat-exchange tube of the opposing party can be relative with the described thinner wall section of the described heat-exchange tube of a side across described outside stream, described multiple flow path portion of described multiple flow path portion of the described heat-exchange tube of one side and the described heat-exchange tube of the opposing party can be arranged in staggered on described width.According to such structure, the broad degree of the outside stream on the thickness direction of heat-exchange tube is roughly certain in the upper maintenance of the width (flow direction of the 2nd fluid) of heat-exchange tube.Its result, can reduce the pressure loss of the 2nd fluid in outside stream.In addition, the stacked spacing of heat-exchange tube can be reduced and expand the heat transfer area of per unit volume.And then, the stripping of the flowing of the 2nd fluid in the surface of heat-exchange tube can be suppressed and expand effective heat transfer area.
The heat exchange unit of the 10th technical scheme of the present invention possesses: pressure fan, it impeller possessing rotating shaft and be fixed on described rotating shaft; With the heat exchanger described in the 8th technical scheme or the 9th technical scheme, its with the face of described rotational axis vertical in be configured in around described pressure fan, by the rotation of described impeller, the circumferencial direction towards described rotating shaft sends described 2nd fluid to described pressure fan, in described multiple outside stream, when observing from described rotating shaft, the downstream of described outside stream lays respectively at upstream side than described outside stream by the front in the direction of rotation of described rotating shaft.According to the 10th technical scheme, the configuration optimization of heat-exchange tube can be made relative to the swirling flow from centrifugal blower.Thus, reduce the pressure loss, and heat exchanger effectiveness improves.10th technical scheme is especially applicable to ceiling cell type indoor set.
The heat exchanger of the 11st technical scheme of the present invention possesses: multiple flat heat-exchange tube, and it has the internal flow path for the 1st fluid flowing respectively; With multiple outside stream, it is between adjacent described heat-exchange tube, the 2nd fluid carrying out heat exchange with described 1st fluid is supplied to flow, described multiple heat-exchange tube is engaged with each other at the entrance and exit place of described internal flow path, one side of heat-exchange tube described in adjacent 1 group relative to the opposing party at the direction upper offset vertical with the orientation of described multiple heat-exchange tube, described multiple heat-exchange tube arranges into fan-shaped, and described multiple outside stream radially extends.
According to the 11st technical scheme, the angle that the inflow direction of the 2nd fluid is consistent with the flow direction of the 2nd fluid in outside stream or both reducing be can be made.In the front and back of the inlet face of heat exchanger, the flow direction of the 2nd fluid changes hardly.In this case, the stripping of the flowing of the 2nd fluid can be suppressed, also be not easy to produce the large pressure loss.Therefore, it is possible to give full play to the performance of heat exchanger.
In addition, according to the 11st technical scheme, described multiple heat-exchange tube arranges into fan-shaped, and described multiple outside stream radially extends.Such as, by outside stream towards when certain heat exchanger arrangement is around pressure fan (centrifugal blower), between adjacent heat exchanger, there is space.Can by the heat exchanger arrangement of the 11st technical scheme in such space.Because outside stream radially extends, so easily flow into outside stream from the 2nd fluid of pressure fan ejection.Thereby, it is possible to reduce the pressure loss of the 2nd fluid.In addition, the stripping of the 2nd fluid stream can be suppressed, so effectively heat transfer area expands.
In the 12nd technical scheme, such as, the described heat-exchange tube of the heat exchanger of the 11st technical scheme can comprise 1 group of sheet material of fitting each other, the entrance and exit of described internal flow path can be offered at the interarea of described sheet material, in order to adjacent described heat-exchange tube being engaged at the described entrance of described internal flow path or described exit, described heat exchanger also can possess the coupling member configured between the described entrance of the described internal flow path of adjacent described heat-exchange tube or between described outlet, described coupling member can be the component of flat ring-type, from the upstream side of described outside stream towards downstream, the thickness of described coupling member can increase continuously.If use coupling member, then easily can construct the heat exchanger of the 11st technical scheme.
In the 13rd technical scheme, such as, the described coupling member of the heat exchanger of the 12nd technical scheme can be the component in the cross section with wedge shape.If use the coupling member of such shape, then easily can construct the heat exchanger of the 11st technical scheme.
In the 14th technical scheme, such as, link surface between a side and described coupling member of heat-exchange tube described in adjacent 1 group of the heat exchanger by the 12nd technical scheme or the 13rd technical scheme is defined as the 1st link surface, when the link surface between the opposing party of heat-exchange tube described in adjacent 1 group and described coupling member is defined as the 2nd link surface, described 1st link surface can tilt relative to described 2nd link surface.By coupling member, the angle that the 1st link surface and the 2nd link surface are can be specified.That is, by coupling member, the broad degree of outside stream can be adjusted.
In the 15th technical scheme, in the 12nd technical scheme ~ the 14th technical scheme, the described coupling member of the heat exchanger of arbitrary technical scheme can have the protuberance of the tabular of giving prominence to towards the downstream of described outside stream.According to such coupling member, protuberance plays function as the separator of the outside stream of segmentation.The flowing of the 2nd fluid is flowed by the surface of correcting into along heat-exchange tube, so effectively heat transfer area expands.In addition, protuberance self plays function as fin and contributes to expanding heat-transfer area, so heat exchange performance improves further.
In the 16th technical scheme, such as, the duplexer of multiple described coupling member can be configured with between the adjacent described heat-exchange tube of the heat exchanger of the 12nd technical scheme ~ the 15th technical scheme.By increasing the quantity of coupling member, the broad degree of outside stream can be increased.That is, the free degree of the design of heat exchanger uprises.
In the 17th technical scheme, such as, when the described coupling member of the heat exchanger by the 12nd technical scheme ~ the 15th technical scheme is defined as the 1st coupling member, described heat exchanger also can possess the 2nd coupling member had with the variform shape of described 1st coupling member.According to the 17th technical scheme, the broad degree of outside stream freely can be adjusted.
In the 18th technical scheme, such as, the described internal flow path of the heat exchanger of the 1st technical scheme ~ the 17th technical scheme can be have multiple sections and the flow direction of described 1st fluid extending on the specific column direction of described heat-exchange tube at the sinuous stream reverse to the midway of described outlet from described entrance.According to the internal flow path wriggled, swim over to downstream from outside stream, occur thermograde on the surface of heat-exchange tube.Thereby, it is possible to make the flowing of the 1st fluid and the flowing of the 2nd fluid doubtfully relative, so the raising that the temperature efficiency of heat exchanger can be expected and the raising of heat exchanger effectiveness of accompanying therewith.
In the 19th technical scheme, such as, the described heat-exchange tube of the heat exchanger of the 1st technical scheme ~ the 18th technical scheme also can have and is arranged between adjacent described section, hinders the obstruction of the heat movement between adjacent described section to construct.According to the 19th technical scheme, on the flow direction of the 2nd fluid, the thermograde on the surface of heat-exchange tube becomes large, and temperature efficiency and the heat exchanger effectiveness of heat exchanger improve further.
The heat exchange unit of the 20th technical scheme of the present invention possesses: the heat exchanger in the 11st technical scheme ~ the 19th technical scheme described in arbitrary technical scheme, its with the face of described rotational axis vertical in be configured in around described pressure fan; And pressure fan, it impeller possessing rotating shaft and be fixed on described rotating shaft, by the rotation of described impeller, the circumferencial direction towards described rotating shaft sends described 2nd fluid, in described multiple outside stream, when observing from described rotating shaft, the downstream of described outside stream lays respectively at upstream side than described outside stream by the front in the direction of rotation of described rotating shaft.According to the 20th technical scheme, the configuration optimization of heat-exchange tube can be made relative to the swirling flow from centrifugal blower.Thus, the pressure loss reduces, and heat exchanger effectiveness improves.20th technical scheme is especially applicable to ceiling cell type indoor set.
The heat exchanger of the 21st technical scheme of the present invention is the heat exchanger used in following heat exchange unit, described heat exchange unit possesses: pressure fan, it impeller possessing rotating shaft and be fixed on described rotating shaft, by the rotation of described impeller, the circumferencial direction towards described rotating shaft sends described 2nd fluid; And heat exchanger, its with the face of described rotational axis vertical in be configured in around described pressure fan,
Described heat exchanger possesses:
Multiple flat heat-exchange tube, it has the internal flow path for the 1st fluid flowing respectively; With
Multiple outside stream, it is between adjacent described heat-exchange tube, supplies the 2nd fluid carrying out heat exchange with described 1st fluid to flow,
Described heat-exchange tube comprises the 1st sheet material and the 2nd sheet material of fitting each other,
When the outer surface of described 1st sheet material being defined as the 1st interarea, the outer surface of described 2nd sheet material being defined as the 2nd interarea,
Described 1st sheet material have be positioned at described 1st interarea, as the entrance of described internal flow path the 1st entrance junction surface and be positioned at described 1st interarea, as described internal flow path outlet the 1st outlet junction surface,
Described 2nd sheet material have be positioned at described 2nd interarea, as the entrance of described internal flow path the 2nd entrance junction surface and be positioned at described 2nd interarea, as described internal flow path outlet the 2nd outlet junction surface,
Engaged by the described 1st entrance junction surface of a side and the described 2nd entrance junction surface of the opposing party, and the described 2nd outlet junction surface of the described 1st outlet junction surface of a side and the opposing party engages, thus described in adjacent 1 group, heat-exchange tube is engaged with each other,
In described multiple outside stream, when observing from described rotating shaft, the downstream of described outside stream lays respectively at upstream side than described outside stream by the front in the direction of rotation of described rotating shaft,
When observing from the thickness direction of described heat-exchange tube, described 1st entrance junction in than the upstream side of described 2nd entrance junction surface by described outside stream,
When observing from the thickness direction of described heat-exchange tube, described 1st outlet junction is in the upstream side leaning on described outside stream than described 2nd outlet junction surface.
The heat exchanger of the 22nd technical scheme of the present invention is the heat exchanger used in following heat exchange unit, described heat exchange unit possesses: pressure fan, it impeller possessing rotating shaft and be fixed on described rotating shaft, by the rotation of described impeller, the circumferencial direction towards described rotating shaft sends described 2nd fluid; And heat exchanger, its with the face of described rotational axis vertical in be configured in around described pressure fan,
Described heat exchanger possesses:
Multiple flat heat-exchange tube, it has the internal flow path for the 1st fluid flowing respectively; With
Multiple outside stream, it is between adjacent described heat-exchange tube, supplies the 2nd fluid carrying out heat exchange with described 1st fluid to flow,
Described heat-exchange tube comprises the 1st sheet material and the 2nd sheet material of fitting each other,
When the outer surface of described 1st sheet material being defined as the 1st interarea, the outer surface of described 2nd sheet material being defined as the 2nd interarea,
Described 1st sheet material have be positioned at described 1st interarea, as the entrance of described internal flow path the 1st entrance junction surface and be positioned at described 1st interarea, as described internal flow path outlet the 1st outlet junction surface,
Described 2nd sheet material have be positioned at described 2nd interarea, as the entrance of described internal flow path the 2nd entrance junction surface and be positioned at described 2nd interarea, as described internal flow path outlet the 2nd outlet junction surface,
Engaged by the described 1st entrance junction surface of a side and the described 2nd entrance junction surface of the opposing party, and the described 2nd outlet junction surface of the described 1st outlet junction surface of a side and the opposing party engages, thus described in adjacent 1 group, heat-exchange tube is engaged with each other,
In described multiple outside stream, when observing from described rotating shaft, the downstream of described outside stream lays respectively at upstream side than described outside stream by the front in the direction of rotation of described rotating shaft,
The composition surface that described 1st entrance junction surface and described 2nd entrance junction surface engage relative to the face tilt residing for described heat-exchange tube,
Described 1st outlet junction surface and described 2nd composition surface that engages, outlet junction surface relative to the face tilt residing for described heat-exchange tube,
The axle at described 1st entrance junction surface and the axle at described 2nd entrance junction surface tilt relative to the thickness direction of described multiple heat-exchange tube,
The axle at described 1st outlet junction surface and the axle at described 2nd outlet junction surface tilt relative to the thickness direction of described multiple heat-exchange tube.
The heat exchanger of the 23rd technical scheme of the present invention is the heat exchanger used in following heat exchange unit, described heat exchange unit possesses: pressure fan, it impeller possessing rotating shaft and be fixed on described rotating shaft, by the rotation of described impeller, the circumferencial direction towards described rotating shaft sends described 2nd fluid; And heat exchanger, its with the face of described rotational axis vertical in be configured in around described pressure fan,
Described heat exchanger possesses:
Multiple flat heat-exchange tube, it has the internal flow path for the 1st fluid flowing respectively; With
Multiple outside stream, it is between adjacent described heat-exchange tube, supplies the 2nd fluid carrying out heat exchange with described 1st fluid to flow,
Described heat-exchange tube comprises the 1st sheet material and the 2nd sheet material of fitting each other,
When the outer surface of described 1st sheet material being defined as the 1st interarea, the outer surface of described 2nd sheet material being defined as the 2nd interarea,
Described 1st sheet material have be positioned at described 1st interarea, as the entrance of described internal flow path the 1st entrance junction surface and be positioned at described 1st interarea, as described internal flow path outlet the 1st outlet junction surface,
Described 2nd sheet material have be positioned at described 2nd interarea, as the entrance of described internal flow path the 2nd entrance junction surface and be positioned at described 2nd interarea, as described internal flow path outlet the 2nd outlet junction surface,
Engaged by the described 1st entrance junction surface of a side and the described 2nd entrance junction surface of the opposing party, and the described 2nd outlet junction surface of the described 1st outlet junction surface of a side and the opposing party engages, thus described in adjacent 1 group, heat-exchange tube is engaged with each other,
Described multiple outside stream radially extends.
In the 24th technical scheme, in described multiple outside streams of the heat exchanger of the 23rd technical scheme, when observing from described rotating shaft, the downstream of described outside stream can lay respectively at upstream side than described outside stream by the front in the direction of rotation of described rotating shaft, and described multiple heat-exchange tube can be arranged in fan-shaped when observing from described axial rotary.
Below, with reference to accompanying drawing, embodiments of the present invention are described.The invention is not restricted to following embodiment.
(the 1st embodiment)
As shown in Figure 1, the heat exchanger 1 of the 1st embodiment of the present invention possesses multiple flat heat-exchange tube 2, inlet header 10A and outlet header 10B.Multiple heat-exchange tube 2 has the shape of rectangle respectively under overlooking.1st fluid (such as, cold-producing medium) is in the internal flow of multiple heat-exchange tube 2.Multiple heat-exchange tube 2 is arranged in outside and forms the stream carrying out the 2nd fluid (such as, air) of heat exchange with the 1st fluid.Specifically, the stream of the 2nd fluid is formed between adjacent heat-exchange tube 2.Inlet header 10A and outlet header 10B is assemblied in the heat-exchange tube 2 of the end face of the heat exchanger 1 in the orientation forming heat-exchange tube 2.
As shown in Fig. 2 A ~ Fig. 2 C, heat-exchange tube 2 has the internal flow path 3 for the 1st fluid flowing.Inlet header 10A is the pipe supplying the 1st fluid for the entrance 3a of internally stream 3.Outlet header 10B is the pipe for discharging the 1st fluid from the outlet 3b of internal flow path 3.Inlet header 10A can be connected with external equipment (not shown) respectively with outlet header 10B.
As shown in arrow A in Fig. 1, the 1st fluid is supplied to the internal flow path 3 of heat-exchange tube 2 from inlet header 10A.As indicated by arrow b of figure, equipment is discharged to the outside with the 1st fluid that the 2nd fluid has carried out heat exchange from outlet header 10B by internal flow path 3.As indicated by arrow c of figure 1, the 2nd fluid, on the direction parallel with the width of heat-exchange tube 2, is being formed at flowing in the space between adjacent heat-exchange tube 2 (multiple outside stream 8).The width of heat-exchange tube 2 is directions vertical with the both sides of the length direction of heat-exchange tube 2 with the orientation of multiple heat-exchange tube 2.
In FIG, the length direction of the width of heat-exchange tube 2, the orientation of multiple heat-exchange tube 2 and heat-exchange tube 2 corresponds respectively to X-direction, Y-direction and Z-direction.In this manual, the orientation (stacked direction) of heat-exchange tube 2 is parallel with the thickness direction of heat-exchange tube 2.2nd fluid flows abreast with the width (X-direction) of heat-exchange tube 2 substantially.
Heat-exchange tube 2 is made up of 1 group of sheet material 11,12 of fitting each other.At least one party selected from 1 group of sheet material 11,12 has the recess forming internal flow path 3.Specifically, heat-exchange tube 2 is made up of the 1st sheet material 11 and the 2nd sheet material 12.1st sheet material 11 and the 2nd sheet material 12 have the recess forming internal flow path 3 respectively.Internal flow path 3 is formed by the 1st sheet material 11 and the 2nd sheet material laminating 12 laminating.According to such structure, the thin-walled property of heat-exchange tube 2 can be realized, be conducive to the miniaturization of heat exchanger 1.In addition, owing to forming heat-exchange tube 2 by the laminating of the 1st sheet material 11 and the 2nd sheet material 12, so use fixture than being easier to and/or carrying out soldering.
Sheet material 11,12 is made up of metals such as aluminium, aluminium alloy, stainless steels.By carrying out punch process to metallic plate to give the shape expected, thus obtain sheet material 11,12.Sheet material 11,12 is such as fitted by soldering.As the raw material of sheet material 11,12, the covering material with core and at least 1 solder layer can be used.
Except collector 10A, 10B, the heat exchanger 1 of present embodiment is only made up of multiple heat-exchange tube 2.Heat-exchange tube 2 is the simple parts be made up of 1 group of sheet material 11,12.Punch process for obtaining sheet material 11,12 is also easy.Compared with finned tube heat exchanger, heat exchanger 1 has easy manufacture, the advantages such as dew are not easily detained in surface.
As shown in Fig. 2 A ~ Fig. 2 C, multiple heat-exchange tube 2 is engaged with each other with outlet 3b place at the entrance 3a of internal flow path 3.One side of 1 group of adjacent heat-exchange tube 2 relative to the opposing party at direction (X-direction) upper offset vertical with the orientation of multiple heat-exchange tube 2.Specifically, multiple heat-exchange tube 2 offsets with respect to each in the direction of the width.Thus, stair-stepping structure is formed from the end side the orientation (Y-direction) of multiple heat-exchange tube 2 towards another side.
As shown in Figure 2 C, the inlet face 14 of heat exchanger 1 tilts relative to the orientation (Y-direction) of heat-exchange tube 2.Inlet face 14 is the faces of the leading edge 2f comprising multiple heat-exchange tube 2.When overlooking heat exchanger 1 from the direction (Z-direction) parallel with the length direction of heat-exchange tube 2, the profile of heat exchanger 1 is parallelogram.According to the heat exchanger 1 with such structure, can obtain in the following benefit be described.The leading edge 2f of heat-exchange tube 2 refers to the edge being arranged in the upstream side of the flow direction of the 2nd fluid of outside stream 8 of heat-exchange tube 2.
As shown in Figure 3A, heat exchange unit 104 in the past possesses multiple heat exchanger 101 (with reference to Figure 13) and pressure fan 16.Multiple heat exchanger 101 is configured in pressure fan 16 around.But the major part of the 2nd fluid is supplied to the inlet face 102 of heat exchanger 101 from incline direction.2nd fluid flow into the outside stream of heat exchanger 101 while significantly changing flow direction.In this case, easily cause the stripping of the 2nd fluid stream, and easily produce the large pressure loss.As a result, heat exchanger 101 cannot give full play to its performance.Consider the space being supplied to heat exchange unit 104, the ability etc. required heat exchange unit 104, the position, size, posture etc. of changing heat exchanger 101 are very difficult.
As shown in Figure 3 B, the heat exchange unit 200 of present embodiment possesses multiple heat exchanger 1 and pressure fan 16.Pressure fan 16 is such as centrifugal blower.Pressure fan 16 possesses rotating shaft and is fixed on the impeller of rotating shaft, sends the 2nd fluid by the rotation of impeller towards the circumferencial direction of rotating shaft.In other words, when the rotation of the end on observation impeller from rotating shaft, pressure fan sends the 2nd fluid towards the circumferencial direction of the imaginary circle connected with the outer rim of impeller.In the face of the rotational axis vertical with pressure fan, multiple heat exchanger 1 is configured in pressure fan 16 around.The outside stream 8 (being represented by oblique line) of heat exchanger 1 extends on the direction that the inlet face 14 relative to heat exchanger 1 tilts.In multiple outside stream, when observing from the rotating shaft of pressure fan, the downstream of outside stream lays respectively at upstream side than outside stream more by the front in the direction of rotation of rotating shaft.The flow direction of the 2nd fluid in the outside stream 8 of heat exchanger 1 is parallel or almost parallel with the inflow direction of the 2nd fluid heat exchanger 1.That is, according to heat exchanger 1, the angle that the inflow direction of the 2nd fluid is consistent with the flow direction of the 2nd fluid in outside stream 8 or both reducing be can be made.In the front and back of the inlet face 14 of heat exchanger 1, the flow direction of the 2nd fluid changes hardly.In this case, compared with the heat exchange unit 104 of the heat exchanger 101 employed in the past, the stripping of the 2nd fluid stream can be suppressed, also be not easy to produce the large pressure loss.Therefore, it is possible to give full play to the performance of heat exchanger 1.The significantly design alteration of the housing for stationary heat exchangers 1 is not required yet.
Specifically, heat exchanger 1 has the structure of following explanation.
As shown in Fig. 2 A ~ Fig. 2 C, the outer surface of the 1st sheet material 11 is defined as the 1st interarea 11p, the outer surface of the 2nd sheet material 12 is defined as the 2nd interarea 12p.The entrance 3a of internal flow path 3 and outlet 3b is at both sides' opening of the 1st interarea 11p and the 2nd interarea 12p.Entrance 3a and outlet 3b lays respectively at end side and another side of the length direction of heat-exchange tube 2.1st sheet material 11 has the 1st entrance junction surface 4 and the 1st outlet junction surface 5.1st entrance junction surface 4 and the 1st outlet junction surface 5, as the part for being engaged with each other by adjacent heat-exchange tube 2 at entrance 3a and the outlet 3b place of internal flow path 3, are formed at the 1st interarea 11p.2nd sheet material 12 has the 2nd entrance junction surface 6 and the 2nd outlet junction surface 7.2nd entrance junction surface 6 and the 2nd outlet junction surface 7, as the part for being engaged with each other by adjacent heat-exchange tube 2 at entrance 3a and the outlet 3b place of internal flow path 3, are formed at the 2nd interarea 12p.Because heat-exchange tube 2 is engaged with each other, so do not need special attachment by the junction surface 4 ~ 7 by being formed at sheet material 11 and 12.The parts manufactured needed for heat exchanger 1 are only sheet material 11,12.Therefore, it is possible to expect the reduction of cost that realized by the reduction of number of components and the simplification of manufacturing process.
Entrance junction surface 4,6 is the protuberances of the ring-type of giving prominence to a little along the thickness direction of heat-exchange tube 2 around the entrance 3a of internal flow path 3.Outlet junction surface 5,7 is the protuberances of the ring-type of giving prominence to a little along the thickness direction of heat-exchange tube 2 around the outlet 3b of internal flow path 3.1st entrance junction surface 4 is in the position of the relative leading edge 2f near heat-exchange tube 2 with the 1st outlet junction surface 5.2nd entrance junction surface 6 is in the position of the relative leading edge 2f away from heat-exchange tube 2 with the 2nd outlet junction surface 7.1st entrance junction surface 4 engages with the 2nd entrance junction surface 6 of adjacent heat-exchange tube 2.1st outlet junction surface 5 exports junction surface 7 with the 2nd of adjacent heat-exchange tube 2 and engages.Thereby, it is possible to make multiple heat-exchange tube 2 offset with respect to each in the direction of the width.According to junction surface 4 ~ 7, the biased configuration of multiple heat-exchange tube 2 can not only be formed, the broad degree of outside stream 8 can also be specified.
In the present embodiment, the 1st entrance junction surface 4 directly engages with the 2nd entrance junction surface 6 of adjacent heat-exchange tube 2, and the 1st outlet junction surface 5 exports junction surface 7 with the 2nd of adjacent heat-exchange tube 2 and directly engages.Thus, the internal flow path 3 of adjacent heat-exchange tube 2 is communicated with.But, also as aftermentioned 3rd embodiment, coupling member can be set between junction surface 4 and junction surface 6, both are engaged indirectly.When using such coupling member, the broad degree of the outside stream 8 of regulation can be carried out by coupling member, so junction surface 4,6 can be omitted.This is also applicable to junction surface 5,7.
Amount of bias between adjacent heat-exchange tube 2 equals the amount of bias between the 1st entrance junction surface 4 and the 2nd entrance junction surface 6.By adjustment amount of bias, the angle of inclination of inlet face 14 relative to the width of heat-exchange tube 2 of heat exchanger 1 can be adjusted.In addition, in the present embodiment, amount of bias is certain.But amount of bias is not must be certain.Such as, the amount of bias between 1 group of heat-exchange tube 2 also can be different from the amount of bias between another 1 group of heat-exchange tube 2.In addition, in the present embodiment, all heat-exchange tubes 2 have identical structure.Therefore, all heat-exchange tubes 2 are biased in the direction of the width relative to adjacent heat-exchange tube 2.But, also as aftermentioned variation 5, not biased structure can be comprised partly.
1st sheet material 11 can be the component with the shape identical with the 2nd sheet material 12.When formation junction surface, position 4,5 at misalignment in the width direction, the heat-exchange tube 2 shown in construction drawing 2A ~ Fig. 2 C can be carried out by 2 the 1st sheet materials 11 of fitting.Its result, can expect the reduction of the cost realized by the reduction of number of components.
Below, some variation of heat exchanger are described.For key element common in the heat exchanger 1 shown in Fig. 2 A ~ Fig. 2 C and each variation, enclose identical Reference numeral, the description thereof will be omitted sometimes.That is, as long as not contradiction technically, the explanation relevant to heat exchanger 1 also can be applied to following variation.
(variation 1)
As shown in Figure 4 A, in the heat exchanger 1A of variation 1, multiple heat-exchange tube comprises multiple 1st heat-exchange tube 2A and multiple 2nd heat-exchange tube 2B.The structure of the 1st heat-exchange tube 2A is different from the structure of the 2nd heat-exchange tube 2B.1st heat-exchange tube 2A is adjacent in orientation with the 2nd heat-exchange tube 2B.Specifically, the 1st heat-exchange tube 2A and the 2nd heat-exchange tube 2B alternately configuration in orientation.If combinationally used by the 1st heat-exchange tube 2A and the 2nd heat-exchange tube 2B, even if then when the restriction of the broad degree equidimension of amount of bias, outside stream 8 is strict, also the easy angle of inclination by the inlet face 14 of heat exchanger 1A is adjusted to best angle.That is, according to this variation, the free degree of the design of heat exchanger 1A uprises.
1st heat-exchange tube 2A is the heat-exchange tube 2 illustrated with reference to Fig. 2 A ~ Fig. 2 C.Therefore, the explanation of the 1st heat-exchange tube 2A is omitted.
As shown in figs. 4 b and 4 c, the 2nd heat-exchange tube 2B comprises the 3rd sheet material 17 and the 4th sheet material 18 of fitting each other.The outer surface of the 3rd sheet material 17 is defined as the 3rd interarea 17p, the outer surface of the 4th sheet material 18 is defined as the 4th interarea 18p.The entrance 3a of internal flow path 3 and outlet 3b is at both sides' opening of the 3rd interarea 17p and the 4th interarea 18p.3rd sheet material 17 has the 3rd entrance junction surface 24 and the 3rd outlet junction surface 25.3rd entrance junction surface 24 and the 3rd outlet junction surface 25, as the part for being engaged with each other by adjacent heat-exchange tube 2 (the 1st heat-exchange tube 2A and the 2nd heat-exchange tube 2B), are formed at the 3rd interarea 17p.4th sheet material 18 has the 4th entrance junction surface 26 and the 4th outlet junction surface 27.4th entrance junction surface 26 and the 4th outlet junction surface 27, as the part be engaged with each other by adjacent heat-exchange tube 2 (the 1st heat-exchange tube 2A and the 2nd heat-exchange tube 2B), are formed at the 4th interarea 18p.
Entrance junction surface 24,26 is the protuberances of the ring-type of giving prominence to a little along the thickness direction of heat-exchange tube 22B around the entrance 3a of internal flow path 3.Outlet junction surface 25,27 is the protuberances of the ring-type of giving prominence to a little along the thickness direction of heat-exchange tube 2B around the outlet 3b of internal flow path 3.In the face that the orientation (Y-direction) with multiple heat-exchange tube 2A, 2B is vertical, the position at the position at the 3rd entrance junction surface 24 and the 3rd outlet junction surface 25 exports the position consistency at junction surface 27 with the position and the 4th at the 4th entrance junction surface 26 respectively.In other words, when junction surface 24 ~ 27 is projected to the plane vertical with the thickness direction of heat-exchange tube 2B, the projection image at the 3rd entrance junction surface 24 is consistent with the projection image that the projection image and the 4th at the 4th entrance junction surface 26 exports junction surface 27 respectively with the projection image at the 3rd outlet junction surface 25.According to junction surface 24 ~ 27, the biased configuration of multiple heat-exchange tube 2A, 2B can not only be formed, the broad degree of outside stream 8 can also be specified.
In this variation, the 3rd sheet material 17 is the components with the shape identical with the 4th sheet material 18.When make the 3rd sheet material 17 inside and outside to timing, the 3rd sheet material 17 and the 4th sheet material 18 completely the same.In this case, the reduction of the cost realized by the reduction of number of components can be expected.
In addition, when the 1st sheet material 11 and the 2nd sheet material 12 have different shapes, also can be the component with the shape identical with the 1st sheet material 11 or the 2nd sheet material 12 from the 3rd sheet material 17 with at least 1 side that the 4th sheet material 18 is selected.In this case, the reduction of the cost realized by the reduction of number of components can also be expected.
(variation 2)
As fig. 5 a and fig. 5b, the heat exchanger 1C of variation 2 is made up of multiple heat-exchange tube 2C.Heat-exchange tube 2C comprises the 1st sheet material 21 and the 2nd sheet material 22 of fitting each other.The outer surface of the 1st sheet material 21 is defined as the 1st interarea 21p, the outer surface of the 2nd sheet material 22 is defined as the 2nd interarea 22p.1st sheet material 21 has the 1st entrance junction surface 34 and the 1st outlet junction surface 35.1st entrance junction surface 34 and the 1st outlet junction surface 35, as the part for being engaged with each other by adjacent heat-exchange tube 2C, are formed at the 1st interarea 21p.2nd sheet material 22 has the 2nd entrance junction surface 36 and the 2nd outlet junction surface 37.2nd entrance junction surface 36 and the 2nd outlet junction surface 37, as the part for being engaged with each other by adjacent heat-exchange tube 2C, are formed at the 2nd interarea 22p.
Entrance junction surface 34,36 is the protuberances of the ring-type of giving prominence to a little along the thickness direction of heat-exchange tube 2C around the entrance 3a of internal flow path 3.Outlet junction surface 35,37 is the protuberances of the ring-type of giving prominence to a little along the thickness direction of heat-exchange tube 2C around the outlet 3b of internal flow path 3.But the projecting height at junction surface 34 ~ 37 increases continuously or reduces on the width of heat-exchange tube 2C.Composition surface 38 is formed between the 1st entrance junction surface 34 and the 2nd entrance junction surface 36 of adjacent heat-exchange tube 2C.Export between junction surface 37 at the 1st outlet junction surface 35 and the 2nd of adjacent heat-exchange tube 2C and be formed with composition surface 39.The direction vertical relative to the orientation (Y-direction) with multiple heat-exchange tube 2C, composition surface 38,39 tilts.Specifically, composition surface 38,39 is ring-type under overlooking, and tilts relative to the width (X-direction) of heat-exchange tube 2C.In addition, composition surface 38,39 tilts relative to the orientation (Y-direction) of heat-exchange tube 2C.The angle of inclination on composition surface 38 equals the angle of inclination on composition surface 39.And then the axle C1 at the 1st outlet junction surface 35 is vertical with composition surface 39 with the axle C2 at the 2nd outlet junction surface 37.Equally, the axle at the 1st entrance junction surface 34 is vertical with composition surface 38 with the axle at the 2nd entrance junction surface 36.That is, the axle at each junction surface tilts relative to the orientation (Y-direction) of multiple heat-exchange tube 2C.In addition, the axle at each junction surface tilts relative to the width (X-direction) of heat-exchange tube 2C." axle at junction surface " is the axle at the center at each junction surface by having cylindric side.By junction surface 34 ~ 37, multiple heat-exchange tube 2C can be made to offset with respect to each in the direction of the width.The effect of the effect of the biased configuration forming multiple heat-exchange tube 2C and the broad degree of the outside stream 8 of regulation is born at junction surface 34 ~ 37.By adjusting the projecting height at junction surface 34 ~ 37, the angle of inclination of inlet face 14 relative to the width (X-direction) of heat-exchange tube 2C of heat exchanger 1C can be adjusted.In addition, according to this variation, can not by the angle of inclination of the restriction ground adjustment inlet face 14 of the stacked spacing, amount of bias etc. of heat-exchange tube 2C.
In this variation, the 1st sheet material 21 also can be have the component with the 2nd sheet material 22 same shape.
(variation 3)
As shown in Figure 6 A and 6 B, the heat-exchange tube 2D of the heat exchanger 1D of variation 3 has sinuous internal flow path 3.In the heat-exchange tube 2 illustrated before, 2A, 2B and 2C, internal flow path 3 also can wriggle.
In this variation, heat-exchange tube 2D is made up of the 1st sheet material 41 and the 2nd sheet material 42 of fitting to be formed internal flow path 3 each other.Internal flow path 3 is that the flow direction of the 1st fluid is at the sinuous stream reverse to the midway of outlet 3b from entrance 3a.In this variation, the flow direction of the 1st fluid repeatedly (2 times) is reverse.Internal flow path 3 has the part of the odd number extended on the column direction parallel with the length direction of heat-exchange tube 2D.In this variation, internal flow path 3 comprises 3 parts parallel to each other.According to such structure, the internal diameter of inlet header 10A and outlet header 10B can be increased, so the pressure loss of the inside of inlet header 10A and outlet header 10B can be reduced.And then, can the length of width of shortening heat exchanging tube 2D, so heat exchanger 1D can be made miniaturized.
As shown in Figure 6 A and 6 B, internal flow path 3 has multiple sections that extend on the specific column direction of heat-exchange tube 2D.Specifically, internal flow path 3 has the 1st section of 51, the 2nd sections 52, the 3rd sections the 53, the 1st bending sections 54, the 2nd bending section 55, most upstream section 56 and most downstream sections 57.Heat-exchange tube 2D has outstanding to the both sides of the thickness direction of heat-exchange tube 2D, to form the section 51,52,53 of internal flow path 3 respectively multiple stream forming portions 46,47,48.Multiple stream forming portion 46,47,48 comprises the 1st stream forming portion 46, the 2nd stream forming portion 47 and the 3rd stream forming portion 48.Extend from entrance 3a along the length direction of heat-exchange tube 2D for 1st section 51.2nd section of 52 mode flowed on the direction contrary with the flow direction of the 1st fluid in the 1st section 51 with the 1st fluid extends.3rd section of 53 mode flowed on the direction contrary with the flow direction of the 1st fluid in the 2nd section 52 with the 1st fluid extends.1st section 51 is connected with the 2nd section 52 by the 1st bending section 54.2nd section 52 is connected with the 3rd section 53 by the 2nd bending section 55.Most upstream section 56 is formed in leans on upstream side and the part of the surrounding of entrance 3a than the 1st section 51.Most downstream section 57 is formed in than the 3rd section of 53 downstreams and exports the part of the surrounding of 3b.1st fluid according to entrance 3a, most upstream section 56, the 1st section 51, the 1st bending section 54, the 2nd section 52, the 2nd bending section 55, the 3rd section 53, most downstream section 57 and outlet 3b order, wriggle while flow.
In addition, heat-exchange tube 2D has the 1st thinner wall section 44 and the 2nd thinner wall section 45.1st thinner wall section 44 on the width of heat-exchange tube 2D between the 1st adjacent stream forming portion 46 and the 2nd stream forming portion 47,52 spaced by the 1st section 51 and the 2nd sections along column direction.2nd thinner wall section 45 on the width of heat-exchange tube 2D between the 2nd adjacent stream forming portion 47 and the 3rd stream forming portion 48,53 spaced by the 2nd section 52 and the 3rd sections along column direction.1st thinner wall section 44 and the 2nd thinner wall section 45 are the junction surface between the 1st sheet material 41 and the 2nd sheet material 42 respectively.
As shown in Figure 6A, in the cross section that the length direction (column direction) with heat-exchange tube 2D is vertical, the stream forming portion 46,47 of the heat-exchange tube 2D of the side selected from adjacent 1 group of heat-exchange tube 2D is across the thinner wall section 44,45 relative of outside stream 8 and the heat-exchange tube 2D of the opposing party.In addition, from thinner wall section 44,45 relative across outside stream 8 and the heat-exchange tube 2D of a side of the stream forming portion 47,48 of the heat-exchange tube 2D of adjacent 1 group of the opposing party that heat-exchange tube 2D selects.That is, multiple stream forming portions 46 ~ 48 of multiple stream forming portion 46 ~ 48 of the heat-exchange tube 2D of a side and the heat-exchange tube 2D of the opposing party are arranged in staggered on width (X-direction).According to such structure, the broad degree of the outside stream 8 on the thickness direction of heat-exchange tube 2D is roughly certain in the upper maintenance of the width (flow direction of the 2nd fluid) of heat-exchange tube 2D.Its result, can reduce the pressure loss of the 2nd fluid in outside stream 8.In addition, the stacked spacing of heat-exchange tube 2D can be reduced and expand the heat transfer area of per unit volume.And then, the stripping of the 2nd fluid stream of the surface of heat-exchange tube 2D can be suppressed and expand effective heat transfer area.
In addition, heat-exchange tube 2D also has obstruction structure, and this obstruction structure installation, between adjacent section, hinders the heat between adjacent section to move (heat between the 1st fluid specifically, flowed in each section moves).Specifically, multiple 1st through hole 44h is formed with in the 1st thinner wall section 44.Multiple 2nd through hole 45h is formed in the 2nd thinner wall section 45.1st through hole 44h constructs as the obstruction of the heat movement between obstruction the 1st section 51 and the 2nd sections 52 and plays function.2nd through hole 45h constructs as the obstruction of the heat movement between obstruction the 2nd section 52 and the 3rd sections 53 and plays function.
According to the internal flow path 3 wriggled, swim over to downstream from outside stream 8, occur thermograde on the surface of heat-exchange tube 2D.Thereby, it is possible to make the 1st fluid stream relative approx with the 2nd fluid stream, so the raising that the temperature efficiency of heat exchanger 1D can be expected and the raising of heat exchanger effectiveness of accompanying therewith.And then construct according to above-mentioned obstruction, on the width (flow direction of the 2nd fluid) of heat-exchange tube 2D, the thermograde on the surface of heat-exchange tube 2D becomes large, and temperature efficiency and the heat exchanger effectiveness of heat exchanger 1D improve further.When hindering structure to be through hole 44h, 45h, adjacent section is by spaced apart.Therefore, it is possible to reliably hinder above-mentioned heat mobile.
In this variation, the 1st through hole 44h is the through hole (specifically, slit) of through 1st thinner wall section 44 on the thickness direction of the 1st sheet material 41 and the 2nd sheet material 42.1st through hole 44h is formed in the central portion of the width of the 1st thinner wall section 44, has the shape of rectangle under overlooking.2nd through hole 45h is the through hole (specifically, slit) of through 2nd thinner wall section 45 on the thickness direction of the 1st sheet material 41 and the 2nd sheet material 42.2nd through hole 45h is formed in the central portion of the width of the 2nd thinner wall section 45, has the shape of rectangle under overlooking.Multiple 1st through hole 44h configures at predetermined spaced intervals along the length direction of the 1st thinner wall section 44.Multiple 2nd through hole 45h configures at predetermined spaced intervals along the length direction of the 2nd thinner wall section 45.
In the arbitrary cross section vertical with the thickness direction of the 2nd sheet material 42 with the 1st sheet material 41, the sectional area (total sectional area) of the 1st through hole 44h is than sectional area 1/2 large of the 1st thinner wall section 44.Interval L2 between the length L1 ratio of the length direction of the 1st through hole 44h and the 1st adjacent through hole 44h is long.In the arbitrary cross section vertical with the thickness direction of the 2nd sheet material 42 with the 1st sheet material 41, the sectional area of sectional area ratio the 2nd thinner wall section 45 of the 2nd through hole 45h 1/2 large.Interval L4 between the length L3 ratio of the length direction of the 2nd through hole 45h and the 2nd adjacent through hole 45h is long.The length L3 of the length direction of the 2nd through hole 45h is equal with the length L1 of the length direction of the 1st through hole 44h.Interval L2 between interval L4 between the 2nd adjacent through hole 45h and the 1st adjacent through hole 44h is equal.According to such structure, the heat between the 1st fluid of the 1st fluid of flowing in the 1st section 51 and flowing in the 2nd section 52 can effectively and be reliably hindered to move.Heat between effectively and reliably can hindering the 2nd section 52 and the 3rd sections 53 moves.
The shape, configuration, number, sectional area etc. of through hole 44h, 45h are not particularly limited.Such as, the shape of the 1st through hole 44h can be also other shapes such as circle, polygon, ellipse under overlooking.Also 1 the 1st through hole 44h can be only formed with in the 1st thinner wall section 44.But, when forming multiple 1st through hole 44h in the 1st thinner wall section 44 at predetermined intervals as this variation, the decline of the intensity of the 1st thinner wall section 44 can be suppressed, can effectively hinder again the heat between the 1st section 51 and the 2nd sections 52 to move.This is also applicable to the 2nd through hole 45h.
In addition, heat-exchange tube 2D also has the most upstream thinner wall section 63 the 2nd bending section 55 and most upstream section 56 separated and the 3rd through hole 63h being formed at most upstream thinner wall section 63.Most upstream thinner wall section 63 is in the thinner wall section of the 1st sheet material 41 and the 2nd sheet material 42 having been carried out being formed when fitting.3rd through hole 63h hinders to construct as the upstream side of the heat movement between obstruction the 2nd bending section 55 and most upstream section 56 and plays function.3rd through hole 63h is formed in the part near entrance 3a in most upstream thinner wall section 63.3rd through hole 63h is the through hole (specifically, slit) of through most upstream thinner wall section 63 on the thickness direction of the 1st sheet material 41 and the 2nd sheet material 42.3rd through hole 63h is formed in the central portion of most upstream thinner wall section 63, has the shape of rectangle under overlooking.According to such structure, can effectively and reliably the heat between the 2nd bending section 55 and most upstream section 56 be hindered to move.
In addition, heat-exchange tube 2D also has the most downstream thinner wall section 65 the 1st bending section 54 and most downstream section 57 separated and the 4th through hole 65h being formed at most downstream thinner wall section 65.Most downstream thinner wall section 65 is in the thinner wall section of the 1st sheet material 41 and the 2nd sheet material 42 having been carried out being formed when fitting.4th through hole 65h hinders to construct as the downstream of the heat movement between obstruction the 1st bending section 54 and most downstream section 57 and plays function.4th through hole 65h is formed in the part near outlet 3b in most downstream thinner wall section 65.4th through hole 65h is the through hole (specifically, slit) of through most downstream thinner wall section 65 on the thickness direction of the 1st sheet material 41 and the 2nd sheet material 42.4th through hole 65h is formed in the central portion of most downstream thinner wall section 65, has the shape of rectangle under overlooking.According to such structure, can effectively and reliably the heat between the 1st bending section 54 and most downstream section 57 be hindered to move.Same with the 1st through hole 44h, the shape, configuration, number, sectional area etc. of the 3rd through hole 63h and the 4th through hole 65h are not particularly limited.
The obstruction structure of heat movement is hindered to be not limited to through hole.As the obstruction structure hindering heat movement, also can with there is the material of relatively low pyroconductivity (such as, resin) make thinner wall section 44,45,63,65, the part beyond thinner wall section 44,45,63,65 is made with the material (such as, metal) with relatively high pyroconductivity.
As shown in Figure 6A, in the cross section vertical with column direction, the part (or whole) on the surface of stream forming portion 46 ~ 48 extends towards the direction that thickness direction and this both direction of width relative to heat-exchange tube 2D tilts from thinner wall section 44,45.According to such structure, when the 2nd fluid flows in outside stream 8, the stripping of the 2nd fluid of the surface of stream forming portion 46 ~ 48 can be suppressed.Therefore, the heat exchanger effectiveness of heat exchanger 1D improves further.
In this variation, only used a kind of heat-exchange tube 2D.Thereby, it is possible to expect the reduction of cost and the simplification of manufacturing process.But, also can use the heat-exchange tube of multiple kinds with structure different from each other.
(variation 4)
The quantity forming the section of internal flow path 3 is not limited to 3.As shown in Figure 7 A, the heat-exchange tube 2E that the heat exchanger 1E of variation 4 uses is having in 5 the section this point forming internal flow path 3, different from the heat-exchange tube 2D that the heat exchanger 1D of variation 3 uses.
(variation 5)
Not every heat-exchange tube all must be biased relative to adjacent heat-exchange tube in the direction of the width.As shown in Figure 7 B, the heat exchanger 1F of variation 5 is made up of multiple heat exchange nest of tubes 20.Adjacent heat exchange nest of tubes 20 is at width (X-direction) upper offset.Heat exchange nest of tubes 20 is made up of multiple heat-exchange tube 2D, 2F.Specifically, heat exchange nest of tubes 20 comprises heat-exchange tube 2D and heat-exchange tube 2F.Heat-exchange tube 2D is the heat-exchange tube that the heat exchanger 1D of variation 3 uses.Heat-exchange tube 2F is the variation of heat-exchange tube 2D.In heat-exchange tube 2F, be not biased relative to the entrance junction surface formed at the 2nd sheet material and outlet junction surface respectively at the entrance junction surface that the 1st sheet material is formed and outlet junction surface.In heat exchange nest of tubes 20, heat-exchange tube 2D is not biased relative to heat-exchange tube 2F.Like this, by by the heat-exchange tube with multiple junction surfaces biased in the direction of the width and the heat-exchange tube combination had at the not biased multiple junction surfaces of width, the angle of inclination (the inflow angle of the 2nd fluid heat exchanger) of inlet face 14 suitably can be adjusted.
(other structures)
The cross section of internal flow path 3 also can be the curve shape such as streamline shape, wing-like.In addition, all bights of comprising, the cross section of internal flow path 3 or a part of bight also can have R shape or curve shape.According to such structure, the pressure loss of the 2nd fluid can be reduced, and suppress the stripping of the 2nd fluid stream.
In addition, also can at least one end of heat-exchange tube in the direction of the width be provided with from the stream forming portion forming internal flow path 3 along the outstanding plate-like portion of width.The flow direction of such plate-like portion restriction the 2nd fluid, suppresses the stripping of the 2nd fluid stream.Thus, effective heat transfer area of heat-exchange tube increases.In addition, plate-like portion self bears the effect of fin, and the surface of plate-like portion is added as heat-transfer area.Therefore, by arranging plate-like portion at heat-exchange tube, the miniaturization of heat exchanger can be realized.
Below, the heat exchanger of other embodiments is described.For key element common in the heat exchanger of the heat exchanger illustrated in the 1st embodiment and other embodiments, enclose identical Reference numeral, the description thereof will be omitted sometimes.That is, as long as not contradiction technically, the explanation of the 1st embodiment also can be applicable to following embodiment.
(the 2nd embodiment)
As shown in Figure 8, the heat exchanger 1G of present embodiment is made up of multiple heat-exchange tube 2G respectively with internal flow path 3.Multiple heat-exchange tube 2G is arranged in the outside stream 8 being formed between adjacent heat-exchange tube 2G and flow for the 2nd fluid.But in the present embodiment, multiple heat-exchange tube 2G does not offset with respect to each.The position of multiple heat-exchange tube 2G is consistent with each other on length direction (Z-direction) and width (X-direction).Present embodiment is different from the 1st embodiment in this.In other, be common in present embodiment and the 1st embodiment.
Heat-exchange tube 2G has the protuberance 29 of tabular at the two ends of width (flow direction of the 2nd fluid).Protuberance 29 forms intake section 8a and the exit portion 8b of outside stream 8.Protuberance 29 contributes to the heat transfer area expanding heat-exchange tube 2G.
The intake section 8a of outside stream 8 extends on the direction that the inlet face 14 relative to heat exchanger 1G tilts, to make the flow direction of the 2nd fluid at the intake section 8a place of outside stream 8 close to the direction parallel from the direction that pressure fan (with reference to Fig. 3 B) heat exchanger 1G flows into the 2nd fluid.According to the present embodiment, can consider that the inflow angle of the 2nd fluid externally intake section 8a of stream 8 is to adjust the angle of protuberance 29.Thereby, it is possible to reduce the pressure loss of the 2nd fluid, and the stripping of the 2nd fluid stream can be suppressed.
In the present embodiment, protuberance 29 is exterior regions (or hinder marginal part) of heat-exchange tube 2G, relative to orientation (Y-direction) and width (X-direction) inclination of multiple heat-exchange tube 2G.According to such structure, the angle that the inflow direction not carrying out the direction and the 2nd fluid that significantly design alteration just can reduce the intake section 8a of outside stream 8 is.Its result, can provide a kind of heat exchanger 1G that inhibit cost, have again excellent properties.
Protuberance 29 can be formed by the bend at end of the sheet material by forming heat-exchange tube 2G.The tilt angle alpha (angle of inclination relative to width) of protuberance 29 is upper certain in the orientation (Y-direction) of heat-exchange tube 2G.But tilt angle alpha is not must be certain.Such as, when the inflow angle of the 2nd fluid heat exchanger changes in the orientation of heat-exchange tube, the inflow angle of the 2nd fluid can be coordinated and tilt angle alpha is changed.That is, in heat exchanger 1G, the protuberance 29 with various tilt angle alpha also can be formed with.
(the 3rd embodiment)
As shown in Figure 9, the heat exchanger 1H of present embodiment is made up of multiple heat-exchange tube 2H respectively with internal flow path 3.Multiple heat-exchange tube 2H is arranged in fan-shaped, to make to form outside stream 8 between adjacent heat-exchange tube 2H.The width of heat-exchange tube 2H is consistent with the radial direction of fan.Multiple outside stream 8 radially extends.2nd fluid moves from inner circumferential side towards periphery effluent.
As shown in figure 12, when by being configured at around pressure fan 16 (centrifugal blower) towards certain heat exchanger 204 of outside stream, between adjacent heat exchanger 204, there is space.The heat exchanger 1H of present embodiment can be configured at such space.Because outside stream 8 radially extends, so easily flow into outside stream 8 from the 2nd fluid of pressure fan 16 ejection.Thereby, it is possible to reduce the pressure loss of the 2nd fluid.In addition, the stripping of the 2nd fluid stream can be suppressed, so effectively heat transfer area expands.
As outside stream towards certain heat exchanger 204, both can use heat exchanger in the past, also can be used in the heat exchanger illustrated in the 1st embodiment or the 2nd embodiment.
As shown in Figure 10 A ~ Figure 10 C, heat exchanger 1H also possesses multiple coupling member 70.In the present embodiment, between adjacent heat-exchange tube 2H, 2 coupling members 70 are configured with.Heat-exchange tube 2H comprises 1 group of sheet material 71 of fitting each other.Entrance 3a and the outlet 3b of internal flow path 3 is offered at the interarea of sheet material 71.In order to adjacent heat-exchange tube 2H engages by the entrance 3a place at internal flow path 3, a side of 2 coupling members 70 is configured between the entrance 3a of adjacent heat-exchange tube 2H.In order to adjacent heat-exchange tube 2H engages by the outlet 3b place at internal flow path 3, the opposing party of 2 coupling members 70 is configured between the outlet 3b of adjacent heat-exchange tube 2H.The internal flow path 3 of adjacent heat-exchange tube 2H is communicated with via coupling member 70.Coupling member 70 is components of flat ring-type.The internal diameter of coupling member 70 is equal with the opening diameter exporting 3b with the entrance 3a of internal flow path 3.From the upstream side of outside stream 8 towards downstream, the thickness of coupling member 70 increases continuously.If use coupling member 70, then easily can construct the heat exchanger 1H of the structure shown in Fig. 9.
As shown in Figure 10 B, the link surface between a side of the heat-exchange tube 2H of adjacent 1 group and coupling member 70 is defined as the 1st link surface 71p, the link surface between the opposing party of the heat-exchange tube 2H of adjacent 1 group and coupling member 70 is defined as the 2nd link surface 71q.Now, the 1st link surface 71p tilts relative to the 2nd link surface 71q.By coupling member 70, the angle that the 1st link surface 71p and the 2nd link surface 71q is can be specified.That is, by coupling member 70, the broad degree of outside stream 8 can be adjusted.
As illustrated in figure 10 c, coupling member 70 is components of the ring-type in the cross section with wedge shape.If use the coupling member 70 of such shape, then easily can construct the heat exchanger 1H of the structure shown in Fig. 9.In addition, owing to can be carried out the broad degree of the outside stream 8 of regulation by coupling member 70, so also entrance junction surface and outlet junction surface can be omitted from heat-exchange tube 2H.Certainly, heat-exchange tube 2H also can have entrance junction surface illustrated in the 1st embodiment and the 2nd embodiment and outlet junction surface.
As shown in Figure 10 D, the duplexer 170 of multiple coupling member 70 also can be configured with between adjacent heat-exchange tube 2H.Such as, the duplexer 170 of 2 coupling members 70 can be configured between heat-exchange tube 2H.By increasing the quantity of coupling member 70, the broad degree of outside stream 8 can be increased.That is, the free degree of the design of heat exchanger 1H uprises.
As shown in figure 10e, also multiple coupling members 70,72 with configurations differing from one can be used in heat exchanger 1H.When the coupling member 70 illustrated with reference to Figure 10 C is defined as the 1st coupling member 70, heat exchanger 1H also can possess the 2nd coupling member 72 had with the variform shape of the 1st coupling member 70.In the example of Figure 10 E, the 1st coupling member 70 and the 2nd coupling member 72 circumferentially alternately configure.According to such structure, the broad degree of outside stream 8 freely can be adjusted.In addition, as illustrated with reference to Figure 10 D, the duplexer of the 1st coupling member 70 and the 2nd coupling member 72 can be also configured with between adjacent heat-exchange tube 2H.
In addition, in the heat exchanger of the 3rd embodiment, a side of 1 group of adjacent heat-exchange tube also can relative to the opposing party at the direction upper offset vertical with the orientation of multiple heat-exchange tube.
(variation 6)
As shown in Figure 11 A ~ Figure 11 C, the heat exchanger 1J of variation 6 possesses the coupling member 73 of the protuberance 73t with tabular.Protuberance 73t towards the outside stream 8 downstream give prominence to.In other words, protuberance 73t is towards radial direction protruding outside of heat exchanger 1J.Except the different this point of shape of coupling member 73, the heat exchanger 1J of variation 6 has the structure identical with the heat exchanger 1H of variation 5.
Specifically, coupling member 73 is made up of the body 73s of ring-type and the protuberance 73t of tabular.Body 73s has the shape identical with the coupling member 70 illustrated in variation 5, between the entrance 3a (or outlet 3b) being configured in the internal flow path 3 of heat-exchange tube 2H.Protuberance 73t is installed on the outer peripheral face of body 73s, has the shape of rectangle under overlooking.Specifically, protuberance 73t be have heat-exchange tube 2H about 1/4 the part of tabular of size.According to such coupling member 73, protuberance 73t plays function as the separator of the outside stream 8 of segmentation.The flowing of the 2nd fluid is flowed by the surface of correcting into along heat-exchange tube 2J, so effectively heat transfer area expands.In addition, protuberance 73t self plays function as fin and contributes to expanding heat-transfer area, so heat exchange performance improves further.
In this variation, only used a kind of coupling member 73.But, also circumferentially alternately can configure the coupling member 70 in variation 5 and the coupling member 73 in this variation.
Technology disclosed in this description is useful for the cooling device, household electrical appliances etc. of conditioner, computer.
Claims (20)
1. a heat exchanger, possesses:
Multiple flat heat-exchange tube, it has the internal flow path for the 1st fluid flowing respectively; With
Multiple outside stream, it is between adjacent described heat-exchange tube, supplies the 2nd fluid carrying out heat exchange with described 1st fluid to flow,
Described multiple heat-exchange tube is engaged with each other at the entrance and exit place of described internal flow path,
One side of heat-exchange tube described in adjacent 1 group relative to the opposing party at the direction upper offset vertical with the orientation of described multiple heat-exchange tube,
Described heat-exchange tube comprises the 1st sheet material and the 2nd sheet material of fitting each other,
When the outer surface of described 1st sheet material being defined as the 1st interarea, the outer surface of described 2nd sheet material being defined as the 2nd interarea,
Described 1st sheet material has the 1st entrance junction surface being positioned at described 1st interarea and exports junction surface as the part for being engaged with each other by adjacent described heat-exchange tube with the be positioned at described 1st interarea the 1st,
Described 2nd sheet material has the 2nd entrance junction surface being positioned at described 2nd interarea and exports junction surface as the part for being engaged with each other by adjacent described heat-exchange tube with the be positioned at described 2nd interarea the 2nd,
Described 1st entrance junction surface is in the position of the relative edge near described heat-exchange tube with described 1st outlet junction surface, and described 2nd entrance junction surface is in the position of the relative described edge away from described heat-exchange tube with described 2nd outlet junction surface.
2. heat exchanger according to claim 1,
Described multiple heat-exchange tube comprises multiple 1st heat-exchange tube and multiple 2nd heat-exchange tube,
The structure of described 1st heat-exchange tube is different from the structure of described 2nd heat-exchange tube,
Described 1st heat-exchange tube is adjacent in described orientation with described 2nd heat-exchange tube.
3. heat exchanger according to claim 2,
Described 1st heat-exchange tube comprises the 1st sheet material and the 2nd sheet material of fitting each other,
When the outer surface of described 1st sheet material being defined as the 1st interarea, the outer surface of described 2nd sheet material being defined as the 2nd interarea,
Described 1st sheet material has the 1st entrance junction surface being positioned at described 1st interarea and exports junction surface as the part for being engaged with each other by adjacent described heat-exchange tube with the be positioned at described 1st interarea the 1st,
Described 2nd sheet material has the 2nd entrance junction surface being positioned at described 2nd interarea and exports junction surface as the part for being engaged with each other by adjacent described heat-exchange tube with the be positioned at described 2nd interarea the 2nd,
Described 1st entrance junction surface is in the position of the relative edge near described 1st heat-exchange tube with described 1st outlet junction surface, and described 2nd entrance junction surface is in the position of the relative described edge away from described 1st heat-exchange tube with described 2nd outlet junction surface,
Described 2nd heat-exchange tube comprises the 3rd sheet material and the 4th sheet material of fitting each other,
When the outer surface of described 3rd sheet material being defined as the 3rd interarea, the outer surface of described 4th sheet material being defined as the 4th interarea,
Described 3rd sheet material has the 3rd entrance junction surface being positioned at described 3rd interarea and exports junction surface as the part for being engaged with each other by adjacent described heat-exchange tube with the be positioned at described 3rd interarea the 3rd,
Described 4th sheet material has the 4th entrance junction surface being positioned at described 4th interarea and exports junction surface as the part for being engaged with each other by adjacent described heat-exchange tube with the be positioned at described 4th interarea the 4th,
In the face vertical with the described orientation of described multiple heat-exchange tube, the position at described 3rd entrance junction surface and the position at described 3rd outlet junction surface export the position consistency at junction surface with the position and the described 4th at described 4th entrance junction surface respectively.
4. heat exchanger according to claim 3,
Described 3rd sheet material is the component with the shape identical with described 4th sheet material.
5. heat exchanger according to claim 3,
At least 1 side selected from described 3rd sheet material and described 4th sheet material is the component with the shape identical with described 1st sheet material or described 2nd sheet material.
6. heat exchanger according to claim 1,
Described internal flow path has multiple sections that extend on the specific column direction of described heat-exchange tube,
Described heat-exchange tube also has: (i) multiple flow path portion, and its both sides to the thickness direction of described heat-exchange tube are outstanding, respectively provides described section of described internal flow path; (ii) thinner wall section, its on the width vertical with described column direction between adjacent described flow path portion and described flow path portion, along described column direction by described section of described internal flow path and described section spaced,
In the cross section vertical with described column direction, the described flow path portion of the described heat-exchange tube of the side selected from heat-exchange tube described in adjacent 1 group is relative with the described thinner wall section of the described heat-exchange tube of the opposing party across described outside stream, and the described flow path portion of the described heat-exchange tube of the opposing party is relative with the described thinner wall section of the described heat-exchange tube of a side across described outside stream
Described multiple flow path portion of described multiple flow path portion of the described heat-exchange tube of one side and the described heat-exchange tube of the opposing party is arranged in staggered on described width.
7. a heat exchange unit, possesses:
Pressure fan, it impeller possessing rotating shaft and be fixed on described rotating shaft; With
Heat exchanger according to claim 1, its with the face of described rotational axis vertical in be configured in around described pressure fan,
By the rotation of described impeller, the circumferencial direction towards described rotating shaft sends described 2nd fluid to described pressure fan,
In described multiple outside stream, when observing from described rotating shaft, the downstream of described outside stream lays respectively at upstream side than described outside stream by the front in the direction of rotation of described rotating shaft.
8. a heat exchanger, possesses:
Multiple flat heat-exchange tube, it has the internal flow path for the 1st fluid flowing respectively; With
Multiple outside stream, it is between adjacent described heat-exchange tube, supplies the 2nd fluid carrying out heat exchange with described 1st fluid to flow,
Described multiple heat-exchange tube is engaged with each other at the entrance and exit place of described internal flow path,
One side of heat-exchange tube described in adjacent 1 group relative to the opposing party at the direction upper offset vertical with the orientation of described multiple heat-exchange tube,
Described heat-exchange tube comprises the 1st sheet material and the 2nd sheet material of fitting each other,
When the outer surface of described 1st sheet material being defined as the 1st interarea, the outer surface of described 2nd sheet material being defined as the 2nd interarea,
Described 1st sheet material has at the 1st junction surface of described 1st interarea setting as the part for being engaged with each other by adjacent described heat-exchange tube,
Described 2nd sheet material has at the 2nd junction surface of described 2nd interarea setting as the part for being engaged with each other by adjacent described heat-exchange tube,
The composition surface that described 1st junction surface engages with described 2nd junction surface tilts relative to the direction vertical with the described orientation of described multiple heat-exchange tube,
The axle at described 1st junction surface and the axle at described 2nd junction surface tilt relative to the described orientation of described multiple heat-exchange tube.
9. heat exchanger according to claim 8,
Described internal flow path has multiple sections that extend on the specific column direction of described heat-exchange tube,
Described heat-exchange tube also has: (i) multiple flow path portion, and its both sides to the thickness direction of described heat-exchange tube are outstanding, respectively provides described section of described internal flow path; (ii) thinner wall section, its on the width vertical with described column direction between adjacent described flow path portion and described flow path portion, along described column direction by described section of described internal flow path and described section spaced,
In the cross section vertical with described column direction, the described flow path portion of the described heat-exchange tube of the side selected from heat-exchange tube described in adjacent 1 group is relative with the described thinner wall section of the described heat-exchange tube of the opposing party across described outside stream, and the described flow path portion of the described heat-exchange tube of the opposing party is relative with the described thinner wall section of the described heat-exchange tube of a side across described outside stream
Described multiple flow path portion of described multiple flow path portion of the described heat-exchange tube of one side and the described heat-exchange tube of the opposing party is arranged in staggered on described width.
10. a heat exchange unit, possesses:
Pressure fan, it impeller possessing rotating shaft and be fixed on described rotating shaft; With
Heat exchanger according to claim 8, its with the face of described rotational axis vertical in be configured in around described pressure fan,
By the rotation of described impeller, the circumferencial direction towards described rotating shaft sends described 2nd fluid to described pressure fan,
In described multiple outside stream, when observing from described rotating shaft, the downstream of described outside stream lays respectively at upstream side than described outside stream by the front in the direction of rotation of described rotating shaft.
11. 1 kinds of heat exchangers, possess:
Multiple flat heat-exchange tube, it has the internal flow path for the 1st fluid flowing respectively; With
Multiple outside stream, it is between adjacent described heat-exchange tube, supplies the 2nd fluid carrying out heat exchange with described 1st fluid to flow,
Described multiple heat-exchange tube is engaged with each other at the entrance and exit place of described internal flow path,
One side of heat-exchange tube described in adjacent 1 group relative to the opposing party at the direction upper offset vertical with the orientation of described multiple heat-exchange tube,
Described multiple heat-exchange tube arranges into fan-shaped,
Described multiple outside stream radially extends.
12. heat exchangers according to claim 11,
Described heat-exchange tube comprises 1 group of sheet material of fitting each other,
The entrance and exit of described internal flow path is offered at the interarea of described sheet material,
In order to adjacent described heat-exchange tube being engaged at the described entrance of described internal flow path or described exit, described heat exchanger also possesses the coupling member configured between the described entrance of the described internal flow path of adjacent described heat-exchange tube or between described outlet
Described coupling member is the component of flat ring-type,
From the upstream side of described outside stream towards downstream, the thickness of described coupling member increases continuously.
13. heat exchangers according to claim 12,
Described coupling member is the component in the cross section with wedge shape.
14. heat exchangers according to claim 12,
When the link surface between a side of heat-exchange tube described in adjacent 1 group and described coupling member being defined as the 1st link surface, the link surface between the opposing party of heat-exchange tube described in adjacent 1 group and described coupling member being defined as the 2nd link surface,
Described 1st link surface tilts relative to described 2nd link surface.
15. heat exchangers according to claim 12,
Described coupling member has the protuberance of the tabular of giving prominence to towards the downstream of described outside stream.
16. heat exchangers according to claim 12,
The duplexer of multiple described coupling member is configured with between adjacent described heat-exchange tube.
17. heat exchangers according to claim 12,
When described coupling member is defined as the 1st coupling member,
Described heat exchanger also possesses the 2nd coupling member had with the variform shape of described 1st coupling member.
18. heat exchangers according to claim 1,
Described internal flow path has multiple sections and the flow direction of described 1st fluid extending on the specific column direction of described heat-exchange tube at the sinuous stream reverse to the midway of described outlet from described entrance.
19. heat exchangers according to claim 1,
Described heat-exchange tube also has and is arranged between adjacent described section, hinders the obstruction of the heat movement between adjacent described section to construct.
20. 1 kinds of heat exchange units, possess:
Pressure fan, it impeller possessing rotating shaft and be fixed on described rotating shaft; With
Heat exchanger according to any one of claim 11 ~ 19, its with the face of described rotational axis vertical in be configured in around described pressure fan,
By the rotation of described impeller, the circumferencial direction towards described rotating shaft sends described 2nd fluid to described pressure fan,
In described multiple outside stream, when observing from described rotating shaft, the downstream of described outside stream lays respectively at upstream side than described outside stream by the front in the direction of rotation of described rotating shaft.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2014102391 | 2014-05-16 | ||
| JP2014-102391 | 2014-05-16 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN105091630A true CN105091630A (en) | 2015-11-25 |
Family
ID=53177252
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510169406.7A Pending CN105091630A (en) | 2014-05-16 | 2015-04-10 | Heat exchanger and heat exchanging unit |
Country Status (4)
| Country | Link |
|---|---|
| US (1) | US20150330713A1 (en) |
| EP (1) | EP2977697A3 (en) |
| JP (1) | JP2015232435A (en) |
| CN (1) | CN105091630A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106196742A (en) * | 2016-08-15 | 2016-12-07 | 安徽天祥空调科技有限公司 | A kind of Wind-cooling type vaporizer |
| CN114270115A (en) * | 2019-08-08 | 2022-04-01 | 株式会社电装 | Heat exchanger |
| CN115342041A (en) * | 2022-09-14 | 2022-11-15 | 广东鑫钻节能科技股份有限公司 | Intelligent energy-saving air compression station |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109564071B (en) * | 2016-10-21 | 2020-09-15 | 松下知识产权经营株式会社 | Heat exchanger and refrigeration system using the same |
| JP2022070491A (en) * | 2020-10-27 | 2022-05-13 | 有限会社和氣製作所 | Heat exchanger |
| CN114543578A (en) * | 2020-11-25 | 2022-05-27 | 广州华凌制冷设备有限公司 | Heat exchanger, fins thereof, heat exchange equipment and air conditioner |
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- 2015-04-28 JP JP2015091712A patent/JP2015232435A/en not_active Withdrawn
- 2015-05-01 US US14/702,214 patent/US20150330713A1/en not_active Abandoned
- 2015-05-15 EP EP15167869.5A patent/EP2977697A3/en not_active Withdrawn
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Also Published As
| Publication number | Publication date |
|---|---|
| US20150330713A1 (en) | 2015-11-19 |
| JP2015232435A (en) | 2015-12-24 |
| EP2977697A2 (en) | 2016-01-27 |
| EP2977697A3 (en) | 2016-04-27 |
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