CN103946663A - Plate heat exchanger - Google Patents
Plate heat exchanger Download PDFInfo
- Publication number
- CN103946663A CN103946663A CN201280048896.XA CN201280048896A CN103946663A CN 103946663 A CN103946663 A CN 103946663A CN 201280048896 A CN201280048896 A CN 201280048896A CN 103946663 A CN103946663 A CN 103946663A
- Authority
- CN
- China
- Prior art keywords
- pad
- heat transfer
- plate
- access
- stream
- 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.)
- Granted
Links
Classifications
-
- 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
- F28D9/0062—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by spaced plates with inserted elements
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F3/00—Plate-like or laminated elements; Assemblies of plate-like or laminated elements
- F28F3/08—Elements constructed for building-up into stacks, e.g. capable of being taken apart for cleaning
- F28F3/10—Arrangements for sealing the margins
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D9/00—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D9/0031—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other
- F28D9/0043—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other the plates having openings therein for circulation of at least one heat-exchange medium from one conduit to another
- F28D9/005—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other the plates having openings therein for circulation of at least one heat-exchange medium from one conduit to another the plates having openings therein for both heat-exchange media
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F3/00—Plate-like or laminated elements; Assemblies of plate-like or laminated elements
- F28F3/08—Elements constructed for building-up into stacks, e.g. capable of being taken apart for cleaning
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F3/00—Plate-like or laminated elements; Assemblies of plate-like or laminated elements
- F28F3/08—Elements constructed for building-up into stacks, e.g. capable of being taken apart for cleaning
- F28F3/083—Elements constructed for building-up into stacks, e.g. capable of being taken apart for cleaning capable of being taken apart
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F2275/00—Fastening; Joining
- F28F2275/20—Fastening; Joining with threaded elements
- F28F2275/205—Fastening; Joining with threaded elements with of tie-rods
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F3/00—Plate-like or laminated elements; Assemblies of plate-like or laminated elements
- F28F3/02—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations
- F28F3/04—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations the means being integral with the element
- F28F3/042—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations the means being integral with the element in the form of local deformations of the element
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
In the present invention, a plurality of heat transfer plates are stacked, said heat transfer plates having a plurality of through holes formed therein. Flow-path forming gaskets are interposed between the outer peripheral sections of the adjacent heat transfer plates, whereby the heat transfer plates are used as boundaries to alternately form first flow paths for circulating high-temperature fluid, second flow paths for circulating low-temperature fluid, and connecting paths for the inflow and outflow of fluid to and from the first flow paths and second flow paths. Connection-path forming gaskets which surround the through holes are interposed between adjacent heat transfer plates, whereby connection paths for the inflow and outflow of fluid to and from the first flow paths and connection paths for the inflow and outflow of fluid to and from the second flow paths are formed. The connection-path forming gaskets are formed having inner gasket members that surround the through holes and, overlapping the inner gasket members, outer gasket members that surround the inner gasket members.
Description
The cross reference of association request
The application advocates the priority of No. 2011-233098, Japan's Patent, and its content is combined in the record of present specification by reference.
Technical field
The present invention relates to the heat-exchangers of the plate type that makes high temperature fluid and cryogen carry out heat exchange, particularly, thus the present invention relates to alternately form between each heat transfer plate by plug-in mounting pads such as stacked multiple heat transfer plates the peripheral parts between each heat transfer plate the stream of circulation high temperature fluid and the heat-exchangers of the plate type of stream of circulation cryogen.
Background technology
As shown in Figure 8, heat-exchangers of the plate type the tabular fixed frame 11 of the rectangle of vertical posture and vertically between the tabular movable frame 12 of the rectangle of posture with stacked multiple the OBL heat transfer plates 20 of vertical posture, 20, as shown in Figure 9, between this heat transfer plate 20 and heat transfer plate 20, alternately form the first stream 1 and the second stream 2, by the high temperature fluid H that circulates at the first stream 1, at the second stream 2 cryogen C that circulates, high temperature fluid H and cryogen C are carried out to heat exchange.
And, at four jiaos of via hole 11a～11d that are provided with as the gateway of fluid H, C of fixed frame 11, on movable frame 12, be not provided with via hole.In addition, overlapping respectively on fixed frame 11 and movable frame 12 have special plate (below, to be called " D plate ", " E plate ".）31、32。On four angles of D plate 31, be provided with via hole (unnumbered), the pad that surrounds this via hole (is called " D pad " below.) 140 be plugged between D plate 31 and fixed frame 11.In addition, on E plate 32, be not provided with via hole.
In addition, at four jiaos of via holes 21～24 that are provided with as the gateway of fluid H, C of heat transfer plate 20, be provided with heat transfer part (without numbering) at pars intermedia, at 20,20 plug-in mounting pads 130 of each heat transfer plate, make to be for example communicated with the upper and lower via hole 23,24 of the upper and lower via hole 21,22 in left side and heat transfer part and right side not to heat transfer part opening, or in contrast.
Pad 130 allosomes or the not shown stream that forms the peripheral part (along the inner side of outer peripheral edges) that surrounds each heat transfer plate 20 form the access formation pad 132 with the surrounding of pad 131 and encirclement via hole 21～24.
And, heat-exchangers of the plate type is provided with the access 3,3 that the via hole upper and lower with left side 21,22 and the first stream 1 cut off by the upper and lower access in right side is formed with pad 132, the 132 upper and lower via holes 23,24 in encirclement right side, and, by making the upper and lower via hole 21,22 in stream formation pad 131 encirclement left sides and heat transfer part be provided with the first stream 1 of circulation high temperature fluid H.
In addition, heat-exchangers of the plate type is provided with by upper and lower via holes 21,22 on the left of the upper and lower access in left side being formed surround with pad 132,132 access 3,3 that the via hole upper and lower with right side 23,24 and the second stream 2 cut off, and, form by making stream formation pad 131 surround the upper and lower access in right side the second stream 2 that is provided with circulation cryogen C with pad 132,132 and heat transfer part.
Therefore, in Fig. 9, high temperature fluid H flows through downwards in the first stream 1 and discharges from the via hole 22 of lower-left from the via hole 21 of upper left, and cryogen C upwards flows through in the second stream 2 and discharges from the via hole 23 of upper right from the via hole 24 of bottom right, thereby two fluid H, C carry out heat exchange.
In addition, though not shown, but record maqting type heat-exchangers of the plate type in patent documentation 1 grade, its with vertical posture stacked multiple by by laser weld, soldering etc. permanent engagement the boxlike plate of peripheral part etc. of two heat transfer plates, and at the peripheral part plug-in mounting pad of boxlike plate, thereby in boxlike plate, form the first stream or the second stream, between boxlike plate and boxlike plate, form the second stream or the first stream.
In addition, in patent documentation 2, record heat-exchangers of the plate type, its plug-in mounting stream between heat transfer plate forms with pad and the access formation integrated pad forming of pad, has the formation of plug-in mounting stream a part and the access of pad arranged side by side form bilayer (two) pad forming by a part for pad at the boundary member of heat transfer part and via hole.This heat-exchangers of the plate type is characterised in that, double-deck pad does not use bonding agent to be fixed to heat transfer plate, and the pad of other parts uses bonding agent to bond to heat transfer plate.
And double-deck pad is inserted between stacked heat transfer plate every one (replacing), thus be formed with without double-deck pad be communicated with the stream of heat transfer part and via hole.The heat transfer plate of the part of this bilayer pad of plug-in mounting is not easily because interior pressure is out of shape, but because double-deck pad does not bond to heat transfer plate by bonding agent, therefore the resistance to pressure of heat-exchangers of the plate type is improved.
Formerly technical literature
Patent documentation
Patent documentation 1: Japanese Patent Laid-Open 2005-106412 communique
Patent documentation 2: Japanese patent laid-open 9-72686 communique
But, in the existing heat-exchangers of the plate type shown in above-mentioned Fig. 8 and Fig. 9, there is following problem.
As shown in Figure 9, in heat-exchangers of the plate type, the high temperature fluid H that flows into the first stream 1 is forming by the access that surrounds via hole 21 the interior circulation of access 3 forming with pad 132.As shown in figure 10, access at the access 3 that forms this high temperature fluid H circulation forms with in pad 132, the inner side (liquid contact side) contacting with high temperature fluid H under hygrothermal environment, thereby because long use can cause solidifying or softeningly wait hot deteriorated deterioration.
In addition, this access formation is macromolecule (RH) by the principal component of pad 132, so heated and react with oxygen (O2) by high temperature fluid H, generates alkyl (R-).And stream forms uses the outside (on-liquid contact side) of pad 131 to contact with atmosphere, alkyl (R-) generates peroxy radical (ROO-) with oxygen reaction.This peroxy radical (ROO-) reacts with macromolecule (RH) and generates peroxide (ROOH).(ROOH) is unstable for this peroxide, is easily decomposed into alkoxyl (RO-) and hydroxyl (OH-).
In a word, the access that forms the access 3 of high temperature fluid H circulation forms uses the liquid contact side of pad 132 to contact with high temperature fluid H, and on-liquid contact side contacts with atmosphere.Therefore, as the macromolecule of principal component, because of oxidative degradation reaction avalanche, group number increases, and impels cut-out, the cross-linking reaction of strand.And, thus, lose the original elasticity of rubber, and structurally, because access forms with pad 132 under compression environment, therefore the fracture that the development of the contact deficiency that the development of generation compression set causes, crackle causes.And this fracture often makes high temperature fluid H leak in the second stream and mix with cryogen C from access 3.
In addition, in the heat-exchangers of the plate type of recording at patent documentation 2, be fitted with double-deck pad in inside.But the access formation pad 132 that forms the access 3 of high temperature fluid H circulation is not set as bilayer, thereby oxidative degradation occurs, high temperature fluid H can leak to outside sometimes.
And, be dangerous liquid at high temperature fluid H, once the high temperature fluid H leaking from heat-exchangers of the plate type flows out to outside, there is sometimes secondary disaster.If not there is not secondary disaster and change ahead of time pad, operating cost rises.In addition, also considered the whole heat-exchangers of the plate type of the coverings such as the sheet material high by air-tightness or inserted rubber etc. to the gap of the periphery edge between stacked heat transfer plate and suppress oxidative degradation and avoid high temperature fluid H to flow out to outside method, but such method is adopted because of cost aspect or quality aspect existing problems.
Summary of the invention
The problem that invention will solve
So problem of the present invention is to provide a kind of access formation pad of the access that forms high temperature fluid circulation that deteriorated heat-exchangers of the plate type can not occur.
Solve the means of problem
In heat-exchangers of the plate type involved in the present invention, be laminated with the heat transfer plate that multiple are formed with multiple via holes, by plug-in mounting stream formation pad between the peripheral part of the each heat transfer plate adjacent, thereby described heat-exchangers of the plate type is alternately formed with the first stream that makes high temperature fluid circulation and the second fluid that makes cryogen circulation taking heat transfer plate as boundary, by the access formation pad that surrounds described via hole is plugged between adjacent heat transfer plate, thereby described heat-exchangers of the plate type is formed with and makes the access of fluid inflow and outflow the first stream and the access of inflow and outflow the second stream, described access formation is formed as bilayer with the inboard washer parts that pad has the described via hole of encirclement with surrounding the outside gasket part of this inboard washer.
Here,, as a mode of heat-exchangers of the plate type involved in the present invention, described access formation also can only be provided with side by side bilayer with pad between the heat transfer plate of access that forms described high temperature fluid circulation.
In addition, from above-mentioned different heat-exchangers of the plate type involved in the present invention, be laminated with the boxlike plate that multiple peripheral parts that are forever connected to form two heat transfer plates of multiple via holes form, between the peripheral part of adjacent each boxlike plate, be fitted with stream formation pad, and between adjacent heat transfer plate, be fitted with and surround the access formation pad of described via hole, thereby described heat-exchangers of the plate type is alternately formed with the first stream that makes high temperature fluid circulation or the second stream that makes cryogen circulation in boxlike plate and between boxlike plate, described access formation is formed as bilayer with the inboard washer parts that pad has the described via hole of encirclement with surrounding the outside gasket part of this inboard washer.
In addition,, as a mode of described each heat-exchangers of the plate type involved in the present invention, can adopt at described access and form by the formation that is formed with outage on the heat transfer plate between inboard washer parts and the outside gasket part of pad.
In addition, as a mode of described each heat-exchangers of the plate type involved in the present invention, can adopt the formation of the following stated:, form with being formed with to pore on the heat transfer plate between inboard washer parts and outside gasket part between pad at described access, in the confined space being surrounded by inside and outside gasket part and heat transfer plate, be filled with inert gas.
Brief description of the drawings
Fig. 1 is the summary exploded perspective view that the first and second embodiment of heat-exchangers of the plate type involved in the present invention is shown.
Fig. 2 is the summary exploded perspective view that the major part of the first and second embodiment of heat-exchangers of the plate type involved in the present invention is shown.
Fig. 3 is the summary exploded perspective view that the major part of the variation of the first and second embodiment of heat-exchangers of the plate type involved in the present invention is shown.
Fig. 4 is the stereogram that the second embodiment of heat-exchangers of the plate type involved in the present invention is shown.
Fig. 5 is that the major part that the second embodiment of heat-exchangers of the plate type involved in the present invention is shown is amplified exploded perspective view.
Fig. 6 illustrates the second embodiment of heat-exchangers of the plate type involved in the present invention, is the major part amplification sectional view along the V-V line of Fig. 5.
Fig. 7 is the major part amplification sectional view that the 3rd embodiment of heat-exchangers of the plate type involved in the present invention is shown.
Fig. 8 is the approximate three-dimensional map that existing heat-exchangers of the plate type is shown.
Fig. 9 is the summary exploded perspective view that existing heat-exchangers of the plate type is shown.
Figure 10 is the major part amplification sectional view that the major part of existing heat-exchangers of the plate type is shown.
Detailed description of the invention
Referring to figs. 1 through Fig. 3, the first embodiment of heat-exchangers of the plate type involved in the present invention is described.But, part same as the prior art is marked to identical symbol and describes.In addition, waiting up and down of narrating in the following description is an example of each embodiment, in actual occupation mode, is different positions sometimes certainly.
As shown in Figure 1 to Figure 3, the heat-exchangers of the plate type of the first embodiment is same with prior art, between heat transfer plate 20 and heat transfer plate 20, alternately to form the first stream 1 and the second stream 2, circulate high temperature fluid H and at the circulate device of cryogen C of the second stream 2, utilize the pad 30 being inserted between heat transfer plate 20 and heat transfer plate 20 that the first stream 1 and the second stream 2 are set at the first stream 1.
Pad 30 stream that (shown in Fig. 1 and Fig. 2) or allosome ground (shown in Fig. 3) is formed with the peripheral part that surrounds heat transfer plate 20 integratedly forms and forms with pad 32 with pad 31 and the access that surrounds the surrounding of via hole 21～24.As shown in Figure 2, form stream formation pad 31 and access and form with in the pad 30 of pad 32, the boundary member of heat transfer part and via hole 21～24 is shared.
And, in the heat-exchangers of the plate type of the first embodiment, as shown in Figure 2, the access that the access 3 of high temperature fluid H circulation is set forms and is formed as inboard washer parts 32a and outside gasket part 32b bilayer with pad (following, to be called " dual pad ") 32.Therefore,, on heat transfer plate 20, be formed with accordingly double-deck groove with inboard washer parts 32a and the outside gasket part 32b of dual pad 32.
In addition, inboard washer parts 32a is formed as circular in the mode of surrounding via hole 21,22.And outside gasket part 32b is formed as being out of shape trapezoidal shape, form boundary member shared with pad 31 and the second stream 2 with stream.
In addition, as shown in Figure 3, the formation of allosome formation stream is formed with the circular inboard washer parts 32a that surrounds via hole 21,22 and the circular outside gasket part 32b bilayer that surrounds these inboard washer parts 32a with the dual pad 32 of pad 31 and access formation pad 32 side by side in concentric mode.Therefore, gasket part 32b in outside does not form the part shared with pad 31 with stream.
And, surround the upper and lower via hole 21,22 in left side by dual pad 32, thereby be provided with the access 3 mobile for high temperature fluid H.In addition, although (below, be called " substance pad " by the general pad using in prior art.) 130 access forms and surround the upper and lower via hole in right side 23,24 with pad 132 and be provided for the mobile access of cryogen C 3, still also can surround the upper and lower via hole in right side 23,24 by dual pad 32 is provided for the mobile access of cryogen C 3.
And, the access formation of substance pad 130 cuts off the upper and lower via hole in right side 23,24 with pad 132, stream formation is inserted between two heat transfer plates 20,20 to surround the upper and lower via hole 21,22 in left side and the mode of heat transfer part with pad 131, thereby is provided for the first stream 1 of high temperature fluid H circulation.
In addition,, although do not illustrate, also can be formed with side by side inboard washer parts and outside gasket part bilayer for the stream formation pad 131 that the first stream 1 is set.Thus, can be used in the pad that the first stream 1 is set and can not produce oxidative degradation.And, also can be formed with side by side inboard washer parts and outside gasket part bilayer for the stream formation pad 131 that the second stream 2 is set.Thus, can assemble without distinguishing the first stream 1 and the second stream 2.
And, pad 30, substance pad 130 are alternately inserted between adjacent heat transfer plate 20,20, thus, high temperature fluid H flows through in the first stream 1 and discharges from the via hole 22 of bottom, left side from the via hole 21 of left upper portion, on the other hand, cryogen C flows through in the second stream 2 and discharges from the via hole 23 of right upper portion from the via hole 24 of lower right side, thereby high temperature fluid H and cryogen C carry out heat exchange.
Now, high temperature fluid H is in the interior circulation of access 3 of left upper portion and flow in the first stream 1.High temperature fluid H in this access 3 contacts with the inboard washer parts 32a of dual pad 32, still, because the surrounding of these inboard washer parts 32a is surrounded by outside gasket part 32b, therefore, can not contact with atmosphere, is difficult to occur oxidative degradation reaction.
In addition, lower the temperature with cryogen C heat exchange at the high temperature fluid H of the access 3 interior circulations of bottom, left side, therefore, the pad 32 that is used to form the access 3 of bottom, left side can not be also bilayer but individual layer.In addition, even if for the access 3 that the upper and lower via hole in right side 23,24 is communicated with is arranged by the access formation pad 132 of substance pad 130, also be at the interior circulation cryogen of this access 3 C, access forms the high temperature that can not become generation oxidative degradation degree with pad 132.
Therefore, this heat-exchangers of the plate type is that dual pad 32 can not crack and high temperature fluid H can be from the heat exchanger of access 3 internal leakages.
Below, with reference to Fig. 2 to Fig. 6, the second embodiment of heat-exchangers of the plate type involved in the present invention is described.In the second embodiment, it is characterized in that, on the heat transfer plate 20 of the part clipping at inboard washer parts 32a and the outside gasket part 32b of dual pad 32, be provided with outage 25 and to both or one only in pore 26.
In order to discharge the high temperature fluid H leaking from the inboard washer parts 32a of dual pad 32, the pad 33 of plug-in mounting ring-type between the heat transfer plate 20,20 for the first stream 1 is set, thus can make outage 25 continuously by this pad 33.
And as shown in Figure 4, the nozzle 13 continuous with outage 25 is installed in fixed frame 11, as shown in Figure 6, if high temperature fluid H leaks from this nozzle 13, can detect as inboard washer parts 32a is because leakage has occurred crackle etc.
In addition, Fig. 5 and Fig. 6 also show the state that the dual pad 32 shown in Fig. 2 is plugged between heat transfer plate 20, is inserted into double-deck D pad 41, the 42 encirclement intercommunicating pores 21 between fixed frame 11 and D plate 20d, but, even if the dual pad 32 shown in heat-exchangers of the plate type Fig. 3 of the second embodiment also can be implemented.
No matter which kind of situation, forms to pore 26 for inboard washer parts 32a is difficult for oxidative degradation reaction further occurs., in the confined space of surrounding to pore 26 to the inboard washer parts 32a by dual pad 32 and outside gasket part 32b and two heat transfer plates 20, supply with the inert gases such as nitrogen, inboard washer parts 32a is not contacted completely with oxygen.
And, because this confined space is adjacent with the first stream 1 across heat transfer plate 20, therefore, by the pad 33 of the ring-type continuous with giving pore 26 of plug-in mounting between the heat transfer plate 20,20 for the first stream 1 is set, thereby this confined space is communicated with this pad 33, supplies with inert gas from the nozzle 14 that is installed on frame 11 in confined space.As shown in Figure 4, be installed on fixed frame 11 for the nozzle 14 of supplying with this inert gas.
In addition, can be only the access 3 of left upper portion to the circulation of high temperature fluid H high temperature outage 25 is set and to pore 26, but, also can outage 25 be set and to pore 26 to the dual pad 32 of the access 3 of the bottom, left side for high temperature fluid H after cooling circulation is set, thereby can assemble with spinning upside down.Therefore, the outage 25 in this situation and give that pore 26 is formed on while turning upside down, outage 25 is on the position that is outage 25 to pore 26, to pore 26.
Below, with reference to Fig. 7, the 3rd embodiment of heat-exchangers of the plate type involved in the present invention is described.The 3rd embodiment is characterized in that, be laminated with vertical posture multiple boxlike plate 200 and boxlike plate 200 between the dual pad 32 of plug-in mounting.
Boxlike plate 200 is to form by the peripheral part of two heat transfer plates 20,20 forever being connected to (representing with stain in Fig. 7) with laser weld or soldering etc., is provided with the first stream 1 of circulation high temperature fluid H or the second stream 2 of circulation cryogen C in inside.
And stacked multiple boxlike plates 200 are provided with the second stream 2 of circulation cryogen C or the first stream 1 of circulation high temperature fluid H between boxlike plate 200 and boxlike plate 200.The dual pad 30 of peripheral part plug-in mounting at this stacked boxlike plate 200 with boxlike plate 200.
The stream formation that pad 30 combinations are plugged in the peripheral part of the permanent connection of boxlike plate 200 forms with pad (not shown) with for the dual pad 32 that access 3 is set.Dual pad 32 is provided with the circular inboard washer parts 32a that surrounds via hole 21,22 and the outside gasket part 32b that surrounds these inboard washer parts 32a side by side in concentric mode.Outside gasket part 31b is plugged in the inner side of permanent connection in illustrated mode.
Or, although diagram not,, outside gasket part 32b is plugged between the part of permanent connection 201, and inboard washer parts 31a is plugged in the inner side (in Fig. 7 for being plugged in the outline line (line) of outside gasket part 31b) of permanent connection.
In order to make the first stream 1 interior circulation of high temperature fluid H in boxlike plate 200, high temperature fluid H is also in the interior circulation of access 3.Access 3 forms by the dual pad 32 that surrounds via hole 21,22.Although the inboard washer parts 32a of dual pad 32 contacts with high temperature fluid H,, suppressed with the reacting of oxygen in atmosphere, oxidative degradation is suppressed.
Therefore, the dual pad 32 of the heat-exchangers of the plate type that assembled box type plate 200 forms also makes crackle, the deteriorated permanent deformation causing is suppressed year in year out, and high temperature fluid H can not leak prematurely.In addition, even if this heat-exchangers of the plate type make cryogen C in the interior circulation of boxlike plate 200, high temperature fluid H is circulated between boxlike plate 200 and boxlike plate 200, high temperature fluid H also can not leak.
Above, in the related heat-exchangers of the plate type of present embodiment, be laminated with multiple and be formed with multiple via holes 21, 22, 23, 24 heat transfer plate 20, form with pad 31 by plug-in mounting stream between the peripheral part of the each heat transfer plate 20 adjacent, thereby be alternately formed with the first stream 1 that makes high temperature fluid H circulation and the second fluid 2 that makes cryogen C circulation taking heat transfer plate 20 as boundary, by surrounding described via hole 21, 22, 23, 24 access forms with pad 32, 32 are plugged between adjacent heat transfer plate 20, make fluid H thereby be formed with, the access 3 of the access 3 of C inflow and outflow the first stream 1 and inflow and outflow the second stream 2, described access formation has with pad 32 the described via hole 21 of encirclement, 22, 23, 24 inboard washer parts 32a is formed as bilayer with surrounding the outside gasket part 32b of this inboard washer 32a.Therefore, access formation is surrounded via hole 21 with pad 32 with inboard washer parts 32a and outside gasket part 32b bilayer, 22, 23, 24 and form access 3, although thereby inboard washer parts 32a contacts with high temperature fluid H, but with oxygen in atmosphere react suppressed, therefore, the inboard washer parts 32a that maintains sealing can not make oxidative degradation react the molecule chain break causing, cross-linking reaction is developed, development and the crackle of compression set are inhibited, be difficult for leaking at the high temperature fluid H that forms the access 3 interior circulations that form with pad 32 by access.
In addition, the heat-exchangers of the plate type related according to present embodiment, described access formation is only provided with side by side bilayer with pad 32 between the heat transfer plate 20 of access 3 that forms described high temperature fluid H circulation.Thus, in view of the access of the access 3 that forms high temperature fluid H circulation forms with pad 32 deteriorated because pad easily occurs in oxidative degradation reaction, thereby be only that this access formation pad 32 is formed as bilayer, the access formation pad 32 that is used to form the stream of cryogen C circulation is formed as individual layer.
In addition, in the related heat-exchangers of the plate type of present embodiment, be laminated with multiple and be forever connected to form multiple via holes 21, 22, 23, two heat transfer plates 20 of 24, the boxlike plate 200 that 20 peripheral part forms, at adjacent each boxlike plate 200, between 200 peripheral part, being fitted with stream forms with pad 31, and be fitted with and surround described via hole 21 200 of adjacent heat transfer plates, 22, 23, 24 access forms with pad 32, thereby in boxlike plate 200 and between boxlike plate 200, be alternately formed with the first stream 1 that makes high temperature fluid H circulation or the second stream 2 that makes cryogen C circulation, described access formation is formed as bilayer with the inboard washer parts 32a that pad 32 has the described via hole of encirclement with surrounding the outside gasket part 32b of this inboard washer 32a.Therefore, the access formation pad 32 being plugged between boxlike plate 200 and boxlike plate 200 is formed as inboard washer parts 32a and outside gasket part 32b bilayer, thereby in the case of interior the first stream 1 that high temperature fluid H circulation is set of boxlike plate 200, access forms with the reaction of the difficult generation oxidative degradation of pad 32, can suppress the deteriorated development of pad, high temperature fluid H is difficult for leaking from access 3.
In addition, the heat-exchangers of the plate type related according to present embodiment, forms with being formed with outage 25 on the heat transfer plate 20 between inboard washer parts 32a and the outside gasket part 32b of pad 32 at described access.Therefore, owing to being formed with outage 25 on the heat transfer plate 20 between inboard washer parts 32a and outside gasket part 32b, thereby can discharge because of high temperature fluid H deteriorated with the heat of inboard washer, that the deteriorated permanent deformation accompanying is leaked from inboard washer parts 32a year in year out from the outage 25 in the gasket part 32b of outside.
In addition, the heat-exchangers of the plate type related according to present embodiment, form with being formed with to pore 26 on the heat transfer plate 20 between inboard washer parts 32a and the outside gasket part 32b of 32, pad at described access, in the confined space being surrounded by inside and outside gasket part and heat transfer plate 20, be filled with inert gas.Thus, owing to being filled with inert gas in the confined space being surrounded by inboard washer parts 32a, outside gasket part 32b and heat transfer plate 20, thereby can be present in the oxidative degradation reaction that air in this confined space suppresses inboard washer parts 32a with doing one's utmost by removal.
The present invention is not limited to the described first to the 3rd embodiment, can carry out various changes.For example, in the heat-exchangers of the plate type that is laminated with boxlike plate 200 illustrating in described the 3rd embodiment, also can possess the steam vent that illustrates in the second embodiment, to pore 26, in addition, also can be as illustrated in the first embodiment, only at the upstream side of the first stream 1, access is formed to be formed as bilayer with pad 32.In addition, with the continuous nozzle 13 of outage 25 and with giving pore 26 continuous nozzle 14 also can not be located at fixed frame 11, and be located at movable frame 12.
Description of reference numerals
1 first stream 2 second streams
3 access 20 heat transfer plates
21,22,23,24 via holes
25 outages 26 are given pore
30 pad 31 stream formation pads
32 access form with pad (dual pad)
Gasket part outside 32a inboard washer parts 32b
200 boxlike plate C cryogens
H high temperature fluid
Claims (5)
1. a heat-exchangers of the plate type, wherein,
Be laminated with the heat transfer plate that multiple are formed with multiple via holes,
By plug-in mounting stream formation pad between the peripheral part of the each heat transfer plate adjacent, thereby described heat-exchangers of the plate type is alternately formed with the first stream that makes high temperature fluid circulation and the second fluid that makes cryogen circulation taking heat transfer plate as boundary,
By the access that surrounds described via hole is formed and is plugged between adjacent heat transfer plate with pad, thereby described heat-exchangers of the plate type is formed with and makes the access of fluid inflow and outflow the first stream and the access of inflow and outflow the second stream,
Described access formation is formed as bilayer with the inboard washer parts that pad has the described via hole of encirclement with surrounding the outside gasket part of this inboard washer.
2. heat-exchangers of the plate type according to claim 1, wherein,
Described access formation is only provided with side by side bilayer with pad between the heat transfer plate of access that forms described high temperature fluid circulation.
3. a heat-exchangers of the plate type, wherein,
Be laminated with the boxlike plate that multiple peripheral parts that are forever connected to form two heat transfer plates of multiple via holes form,
Between the peripheral part of adjacent each boxlike plate, be fitted with stream formation pad,
And between adjacent heat transfer plate, be fitted with and surround the access formation pad of described via hole,
Thereby described heat-exchangers of the plate type is alternately formed with the first stream that makes high temperature fluid circulation or the second stream that makes cryogen circulation in boxlike plate and between boxlike plate,
Described access formation is formed as bilayer with the inboard washer parts that pad has the described via hole of encirclement with surrounding the outside gasket part of this inboard washer.
4. according to the heat-exchangers of the plate type described in any one in claims 1 to 3, wherein,
Form with being formed with outage on the heat transfer plate between inboard washer parts and the outside gasket part of pad at described access.
5. according to the heat-exchangers of the plate type described in any one in claim 1 to 4, wherein,
Form with being formed with to pore on the heat transfer plate between inboard washer parts and outside gasket part between pad at described access, in the confined space being surrounded by inside and outside gasket part and heat transfer plate, be filled with inert gas.
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2011-233098 | 2011-10-24 | ||
| JP2011233098 | 2011-10-24 | ||
| PCT/JP2012/077362 WO2013061966A1 (en) | 2011-10-24 | 2012-10-23 | Plate heat exchanger |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN103946663A true CN103946663A (en) | 2014-07-23 |
| CN103946663B CN103946663B (en) | 2016-06-29 |
Family
ID=48167796
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201280048896.XA Active CN103946663B (en) | 2011-10-24 | 2012-10-23 | Heat-exchangers of the plate type |
Country Status (5)
| Country | Link |
|---|---|
| US (1) | US20140338870A1 (en) |
| EP (1) | EP2772718B1 (en) |
| JP (1) | JP6097696B2 (en) |
| CN (1) | CN103946663B (en) |
| WO (1) | WO2013061966A1 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104359337A (en) * | 2014-12-04 | 2015-02-18 | 胡甜甜 | Multi-medium plate heat exchanger |
| CN107478078A (en) * | 2017-08-17 | 2017-12-15 | 佛山禅能换热器有限公司 | Mix application method and plate type heat exchanger of the sealing gasket in plate type heat exchanger |
Families Citing this family (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP6097697B2 (en) * | 2011-11-11 | 2017-03-15 | 株式会社日阪製作所 | Plate heat exchanger |
| DE102013222130A1 (en) * | 2013-10-30 | 2015-04-30 | MAHLE Behr GmbH & Co. KG | Heat exchanger |
| CN104101237B (en) * | 2014-06-25 | 2016-06-15 | 无锡溥汇机械科技有限公司 | A kind of plate type heat exchanger |
| CN104121791B (en) * | 2014-07-18 | 2015-12-16 | 无锡溥汇机械科技有限公司 | A kind of plate type heat exchanger |
| US20170089644A1 (en) * | 2015-09-30 | 2017-03-30 | Spx Flow, Inc. | Port Connection for a Heat Exchanger |
| US10458718B2 (en) * | 2017-11-29 | 2019-10-29 | Asia Vital Components Co., Ltd. | Airtight penetration structure for heat dissipation device |
| CN114636331A (en) * | 2020-12-16 | 2022-06-17 | 丹佛斯有限公司 | Gasket unit insert for heat exchanger |
| DE102022112039A1 (en) | 2022-05-13 | 2023-11-16 | Akg Verwaltungsgesellschaft Mbh | Safety heat exchanger |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS55145873A (en) * | 1979-04-26 | 1980-11-13 | Power Reactor & Nuclear Fuel Dev Corp | Bellows seal valve |
| JPH0579786A (en) * | 1991-09-25 | 1993-03-30 | Hisaka Works Ltd | Plate type heat exchanger |
| JPH05264192A (en) * | 1992-03-21 | 1993-10-12 | Hisaka Works Ltd | Plate type heat exchanger |
| WO1997029336A1 (en) * | 1996-02-09 | 1997-08-14 | Swep International Ab | An endless plate heat exchanger rubber-gasket |
| JP2000283687A (en) * | 1999-03-31 | 2000-10-13 | Hisaka Works Ltd | Plate type heat exchanger |
| CN2575590Y (en) * | 2002-10-28 | 2003-09-24 | 刘雲生 | Archery type stable tail discarding armor-piercing projectile |
Family Cites Families (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3099520A (en) * | 1960-02-10 | 1963-07-30 | Separator Ab | Method and apparatus for preventing infection of heat exchange chambers |
| JPH02192598A (en) * | 1989-01-18 | 1990-07-30 | Hisaka Works Ltd | Fluid leakage detecting device for plate type heat exchanger |
| AT395354B (en) * | 1991-03-12 | 1992-12-10 | Widschwendter Arnulf | PLATE HEAT EXCHANGER |
| JP3665391B2 (en) | 1995-09-05 | 2005-06-29 | 株式会社日阪製作所 | Plate type heat exchanger gasket mounting structure |
| SE524751C2 (en) * | 2002-07-29 | 2004-09-28 | Alfa Laval Corp Ab | Heat exchanger plate, plate heat exchanger and method of manufacturing a heat exchanger plate |
| SE524783C2 (en) * | 2003-02-11 | 2004-10-05 | Alfa Laval Corp Ab | Plate package, plate heat exchanger and plate module |
| DE10312788A1 (en) * | 2003-03-21 | 2004-09-30 | Behr Gmbh & Co. Kg | Exhaust gas heat exchanger and sealing device for exhaust gas heat exchanger |
| JP4519437B2 (en) | 2003-09-30 | 2010-08-04 | 株式会社日阪製作所 | Joined plate heat exchanger |
| JP4351185B2 (en) * | 2005-04-22 | 2009-10-28 | 三菱電機株式会社 | Semiconductor module cooling device |
| JP2008051390A (en) * | 2006-08-24 | 2008-03-06 | Fuiisa Kk | Heat exchanger |
| US20100300651A1 (en) * | 2009-05-28 | 2010-12-02 | Spx Apv Danmark A/S | Double-walled plate heat exchanger |
-
2012
- 2012-10-23 EP EP12843569.0A patent/EP2772718B1/en active Active
- 2012-10-23 JP JP2013540787A patent/JP6097696B2/en active Active
- 2012-10-23 WO PCT/JP2012/077362 patent/WO2013061966A1/en active Application Filing
- 2012-10-23 US US14/354,120 patent/US20140338870A1/en not_active Abandoned
- 2012-10-23 CN CN201280048896.XA patent/CN103946663B/en active Active
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS55145873A (en) * | 1979-04-26 | 1980-11-13 | Power Reactor & Nuclear Fuel Dev Corp | Bellows seal valve |
| JPH0579786A (en) * | 1991-09-25 | 1993-03-30 | Hisaka Works Ltd | Plate type heat exchanger |
| JPH05264192A (en) * | 1992-03-21 | 1993-10-12 | Hisaka Works Ltd | Plate type heat exchanger |
| WO1997029336A1 (en) * | 1996-02-09 | 1997-08-14 | Swep International Ab | An endless plate heat exchanger rubber-gasket |
| JP2000283687A (en) * | 1999-03-31 | 2000-10-13 | Hisaka Works Ltd | Plate type heat exchanger |
| CN2575590Y (en) * | 2002-10-28 | 2003-09-24 | 刘雲生 | Archery type stable tail discarding armor-piercing projectile |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104359337A (en) * | 2014-12-04 | 2015-02-18 | 胡甜甜 | Multi-medium plate heat exchanger |
| CN107478078A (en) * | 2017-08-17 | 2017-12-15 | 佛山禅能换热器有限公司 | Mix application method and plate type heat exchanger of the sealing gasket in plate type heat exchanger |
Also Published As
| Publication number | Publication date |
|---|---|
| EP2772718A1 (en) | 2014-09-03 |
| EP2772718A4 (en) | 2015-07-29 |
| CN103946663B (en) | 2016-06-29 |
| JPWO2013061966A1 (en) | 2015-04-02 |
| US20140338870A1 (en) | 2014-11-20 |
| JP6097696B2 (en) | 2017-03-15 |
| WO2013061966A1 (en) | 2013-05-02 |
| EP2772718B1 (en) | 2019-05-15 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103946663A (en) | Plate heat exchanger | |
| CN103842761A (en) | Plate heat exchanger | |
| CN103917843A (en) | Plate type heat exchanger | |
| WO2014122890A1 (en) | Heat exchanger | |
| JP2007532852A (en) | Plate heat exchanger | |
| JP2013045781A (en) | Cooler and manufacturing method of the same | |
| JP2016148491A (en) | Plate-type heat exchanger | |
| TWM658064U (en) | Cooling assembly, press head mechanism and sorting and testing equipment | |
| US8955406B2 (en) | Workpiece transfer apparatus | |
| JP5085723B2 (en) | Plate heat exchanger | |
| JP2001099590A (en) | Plate type heat exchanger | |
| JP2018510315A (en) | Block heat exchanger, method of using the heat exchanger, and heat exchange block belonging to the exchanger | |
| CN213208729U (en) | Plate bundle of plate heat exchanger and plate heat exchanger | |
| US11933547B2 (en) | Double plate heat exchanger | |
| JP5855467B2 (en) | Heat exchanger | |
| JP2019133874A (en) | Leak inspection device for fuel cell | |
| KR102403967B1 (en) | Printed circuit board type heat exchanger with partition | |
| JP3184020U (en) | Structure of heat exchanger with leak detection function | |
| JP2002107088A (en) | Plate-type heat exchanger | |
| EP4400796A1 (en) | Microchannel heat exchanger | |
| JP2009064805A (en) | Cooling device | |
| CN105458447A (en) | Spot welding system | |
| JP2007292394A (en) | Laminated heat exchanger | |
| JP2004028357A (en) | Heat exchanger |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |