CN107024124B - Corrugated plate bundle of single-side contactless straight-through runner - Google Patents
Corrugated plate bundle of single-side contactless straight-through runner Download PDFInfo
- Publication number
- CN107024124B CN107024124B CN201610065886.7A CN201610065886A CN107024124B CN 107024124 B CN107024124 B CN 107024124B CN 201610065886 A CN201610065886 A CN 201610065886A CN 107024124 B CN107024124 B CN 107024124B
- Authority
- CN
- China
- Prior art keywords
- waves
- plates
- plate
- heat transfer
- transfer surface
- 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.)
- Active
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
- F28D9/0031—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
- F28D9/0037—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 conduits for the other heat-exchange medium also being formed by paired plates touching each other
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F3/00—Plate-like or laminated elements; Assemblies of plate-like or laminated elements
- F28F3/02—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations
- F28F3/04—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations the means being integral with the element
- F28F3/042—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations the means being integral with the element in the form of local deformations of the element
- F28F3/046—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations the means being integral with the element in the form of local deformations of the element the deformations being linear, e.g. corrugations
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
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
The invention relates to the technical field of plate heat exchangers, in particular to a corrugated plate bundle of a single-side contactless straight-through runner, which comprises a plurality of plates, wherein the plates comprise a main heat transfer surface, turbulent flow waves uniformly distributed on the main heat transfer surface, pressure-bearing waves and branch-path waves extending from one end to the other end along the length direction of the plates.
Description
Technical Field
The invention relates to the technical field of plate heat exchangers, in particular to a corrugated plate bundle with a single-side contactless straight-through runner.
Background
As plate heat exchanger technology has evolved, the range of plate heat exchanger applications has been expanding. At present, researchers are trying to extend the plate heat exchanger to conditions that are prone to fouling and plugging.
For the easy scale deposit, easy jam application condition, current plate bundle structure mainly has:
1. a half-welded plate bundle structure. The plates are welded in pairs to form plate pairs, sealing is realized between the plate pairs through gaskets, and plate bundles can be disassembled into single plate pairs for cleaning when needed.
2. A wide flow channel plate bundle structure. The channel width is increased by increasing the plate spacing.
3. A plate bundle structure with a decontamination structure. By arranging the dirt removing structure between the plates, the dirt in the flow channels between the plates is removed.
The plate bundle structure only improves the problem of blockage or scaling, but does not substantially solve the problems of uniformity of the flow field and the contact points, so that the problem of blockage or scaling cannot be thoroughly solved.
Disclosure of Invention
Aiming at the medium containing particles or easy to scale which is easy to be blocked, the invention provides a corrugated plate bundle of a single-side contactless straight-through runner, which effectively solves the problems of inter-plate runner blocking, scale corrosion and the like and solves the problem of ubiquitous temperature cross heat exchange on the premise of not connecting a plurality of devices in series.
Based on the mechanism analysis of the flow channel blockage and scaling among plates, the invention creatively provides a single-side non-contact straight-through flow channel corrugated plate bundle structure, in the plate bundle, the flow channel on one side of the plate sheet is of a straight-through structure, and the flow channel basically keeps unchanged along the medium flowing direction, so that the flow field basically keeps consistent from the medium inlet to the medium outlet, the precondition of the particulate blockage and scaling is eliminated, and the problems of the particulate blockage and the scaling can be thoroughly solved.
The invention is realized by the following technical scheme:
the utility model provides a unilateral contactless straight-through runner's buckled plate bundle, includes a plurality of plates, the plate includes main heat transfer surface, evenly distributed in the vortex ripple of main heat transfer surface, pressure-bearing ripple and follow the sheet length direction by one end to the branch journey ripple of other end extension, its characterized in that: after a plurality of plates are stacked, longitudinal channels along the length direction of the plates and transverse channels along the width direction of the plates are formed on two sides of the plates, the height of the turbulence waves is smaller than 1/2 of the runner spacing of the transverse channels, the height of the pressure waves and the branching waves is equal to 1/2 of the runner spacing of the longitudinal channels, contacts are formed in the longitudinal channels by the opposite pressure waves and the pressure waves, contacts are formed in the opposite branching waves and the branching waves, and no contacts are formed in the transverse channels by the opposite turbulence waves and the turbulence waves.
The periphery of the plate is bent to form an inlet and an outlet, the plates are buckled in pairs to form plate pairs, and the corrugated plate bundles comprise a plurality of plate pairs which are mutually overlapped.
The periphery of the plate is in the same plane with the main heat transfer surface, and the plates are sequentially stacked into plate bundles through the inlaid strips arranged on the periphery of the plate.
The split-range corrugation is straight corrugation or approximately straight corrugation which is communicated along the length direction of the plate or is intermittent at one end, the intermittent part of the split-range corrugation is provided with folded-range corrugation which is arranged in a semicircular arc shape or a fold line shape, and the folded-range corrugation is continuous or intermittent corrugation and is concave corrugation relative to the main heat transfer surface.
The plate is provided with continuous or intermittent supporting waves or supporting strips at certain intervals along the width direction of the plate, the supporting waves are convex waves relative to the main heat transfer surface, the supporting strips are bosses relative to the main heat transfer surface, and the depth of the supporting waves and the height of the supporting strips are equal to 1/2 of the runner spacing of the transverse channel.
The corrugated plate bundle is characterized by comprising a plurality of plates, wherein each two pairs of plates are buckled to form plate pairs, each corrugated plate bundle comprises a plurality of plate pairs which are mutually overlapped, each plate comprises a main heat transfer surface, turbulent flow waves and pressure bearing waves which are uniformly distributed on the main heat transfer surface and branched path waves which are arranged at one end of the heat transfer surface and extend towards the other end, each pressure bearing wave is convex waves relative to the main heat transfer surface, each branched path wave is concave waves relative to the main heat transfer surface, after a plurality of plates are overlapped, longitudinal channels along the length direction of the plates and transverse channels along the width direction of the plates are formed at two sides of the plates, the height of each turbulent flow wave is smaller than 1/2 of the channel spacing of the longitudinal channels, the height of each pressure bearing wave is equal to 1/2 of the channel spacing of the longitudinal channels, each branched path wave is straight waves which are arranged on the plate and are arranged at a certain interval along the width direction of the plate, each supporting convex wave is a supporting strip or a supporting strip which is equal to the height of each supporting strip along the width direction of the plate, and the height of each supporting strip is equal to 1/2 of the supporting strip relative to the main heat transfer surface.
A corrugated sheet bundle of a single-sided contactless through runner, characterized by: the heat exchanger comprises a plurality of plates, wherein each plate comprises a main heat transfer surface, pressure-bearing waves uniformly distributed on the main heat transfer surface and branch-path waves which are arranged at one end of the heat transfer surface and extend towards the other end, the pressure-bearing waves and the branch-path waves are concave waves relative to the main heat transfer surface, after a plurality of plates are assembled, longitudinal channels along the length direction of the plates and transverse channels along the width direction of the plates are formed at two sides of the plates, the height of the pressure-bearing waves and the height of the branch-path waves are equal to 1/2 of the flow channel spacing of the longitudinal channels, the branch-path waves are straight waves penetrating along the length direction of the plates or with one end being intermittent, the plates are provided with continuous or intermittent support waves or support strips at certain intervals along the width direction of the plates, the support waves are convex waves relative to the main heat transfer surface, the depth of the support waves and the height of the support strips are equal to 1/2 of the flow channel spacing of the transverse channels, and the branch-path waves at the intermittent positions of the support waves are provided with semicircular or broken waves arranged in a fold shape, and the broken waves are continuous or intermittent waves relative to the main heat transfer surfaces.
The periphery of the plate is bent to form an inlet and an outlet, the plates are buckled in pairs to form plate pairs, and the corrugated plate bundles comprise a plurality of plate pairs which are mutually overlapped.
The periphery of the plate is in the same plane with the main heat transfer surface, and the plates are sequentially stacked into plate bundles through the inlaid strips arranged on the periphery of the plate.
The corrugated plate bundle is characterized by comprising a plurality of plates, wherein each two pairs of plates are buckled to form plate pairs, each corrugated plate bundle comprises a plurality of plate pairs which are mutually overlapped, each plate comprises a main heat transfer surface, pressure-bearing waves uniformly distributed on the main heat transfer surface and split-path waves which are arranged at one end of the heat transfer surface and extend towards the other end, each pressure-bearing wave is convex with respect to the main heat transfer surface, each split-path wave is concave with respect to the main heat transfer surface, after a plurality of plates are overlapped, longitudinal channels along the length direction of the plates and transverse channels along the width direction of the plates are formed at two sides of the plates, the height of each pressure-bearing wave is equal to 1/2 of the inter-plate channel spacing of the transverse channels, each split-path wave is a continuous or discontinuous supporting wave or a straight supporting wave which is arranged at a certain interval along the width direction of the plate, the supporting wave is equal to 1/2 of the inter-plate channel spacing, and the supporting wave is convex with respect to the main heat transfer surface.
The beneficial effects of the invention are as follows:
(1) After a plurality of plate pairs are stacked into plate bundles, a non-contact through flow passage is formed on one side of the plate, the cross section of the through flow passage basically keeps unchanged along the flow direction of a medium and has no contact, the flow field is quite uniform in the process of flowing the medium through the flow passage, and the flow passage is used as a passage for treating the medium containing particles or easy to scale, so that the problems of blockage and scale formation in the conventional plate heat exchanger are thoroughly solved.
(2) Because the longitudinal split-range ripple is arranged on the plate, after a plurality of plates are stacked, a longitudinal fold Cheng Liudao is formed on one side of the plate, and a medium A transversely passing through the plate and a medium B flowing along the longitudinal fold Cheng Liudao are subjected to heat exchange in a staggered countercurrent mode, so that the heat exchange of the medium with the temperature crossing is realized, and the problem that the temperature crossing can be solved only by connecting a plurality of plates in series in the conventional plate type heat exchanger is solved.
Drawings
Figure 1 is a schematic view of the structure of a plate constituting the present invention,
figure 2 is a C-C cross-sectional view of the panel of figure 1,
figure 3 is a D-D cross-sectional view of the panel of figure 1,
FIG. 4 is a schematic view of the structure of a plate constituting the present invention
FIG. 5 is a schematic view of the structure of the present invention
Figure 6 is a cross-sectional view of a bundle of plates of the present invention taken along the plate width transverse flow channels C-C,
figure 7 is a cross-sectional view of the inventive plate package along the long longitudinal flow path D-D,
figure 8 is a schematic view of the structure of a plate with folding path corrugation forming the invention,
figure 9 is a schematic view of a plate construction with support corrugations or support bars forming the present invention,
fig. 10 is a rear cross-sectional view of the plate pack plate bundle of fig. 9 taken along the plate width transverse flow channels E-E.
In the figure: 1. plate pairs, 2, plates, 201 primary heat transfer surfaces, 202, turbulence waves, 203, pressure waves, 204, separation waves, 205, bending waves, 206, support waves, 7, support bars, A, media A, B, media B.
Detailed Description
The present invention will be described in further detail below with reference to the drawings and preferred embodiments, so that those skilled in the art can better understand the technical solutions of the present invention.
Referring to fig. 1, the plate 2 constituting the present invention includes a main heat transfer surface 201, a turbulence wave 202, a pressure-bearing wave 203, and a branching wave 204. As shown in fig. 2 and 3, the turbulence wave 202 is a convex wave with respect to the main heat transfer surface 201, and the pressure wave 203 and the branching wave 204 are concave waves with respect to the main heat transfer surface.
Referring to fig. 4, the corrugated plate pair 2 is formed by buckling two plates, and the plates can be assembled and welded by bending the periphery of the plates, or the plates can be assembled and welded by adding sealing strips without bending the periphery of the plates, or the plates can be assembled and welded by adding sealing strips.
Referring to fig. 5 and fig. 6 and 7, a plurality of plate pairs are stacked together to form a plate bundle, the longitudinal flow passage along the length direction of the plate is divided into a plurality of folds Cheng Liudao along the width direction under the action of the split-range ripple, the medium B flowing through the folded-range flow passage and the medium a crossing the width direction of the plate form the wrong-flow heat exchange, and the problem of the temperature crossing of the medium a and the medium B can be solved without connecting a plurality of devices in series. In the longitudinal flow channel of the medium B at one side of the plate, the pressure-bearing corrugation 203 is opposite to the pressure-bearing corrugation 203, the branch corrugation 204 is opposite to the branch corrugation 204, when the height of the pressure-bearing corrugation 203 and the branch corrugation 204 is equal to 1/2 of the spacing of the side flow channel, the tops of the pressure-bearing corrugations 203 are contacted to form contacts, the pressure-bearing capacity of the plate pairs can be improved by welding the contacts, the contact surfaces of the branch corrugations are welded to prevent the fluid short circuit of the folded flow, in the transverse flow channel of the medium A at the other side of the plate, the turbulent flow corrugation 202 is opposite to the turbulent flow corrugation 202, the height of the turbulent flow corrugation 202 is less than 1/2 of the spacing of the side flow channel, and no contacts are formed after the plate pairs are assembled. In summary, the transverse flow channels along the width direction of the plate in the plate bundle are contactless through flow channels, and the longitudinal flow channels along the length direction of the plate are folded-over flow channels with contacts.
It is apparent that when the direction of the pressure-receiving corrugation 203 and the turbulence corrugation 202 with respect to the main heat transfer surface 201 is changed, that is, when the pressure-receiving corrugation 203 is adjusted to be a convex corrugation with respect to the main heat transfer surface 201 and the turbulence corrugation 202 is adjusted to be a concave corrugation with respect to the main heat transfer surface 201, and when the pressure-receiving corrugation 603 is 1/2 of the lateral flow path pitch, the branching corrugation 204 is 1/2 of the longitudinal flow path pitch, the turbulence corrugation is less than 1/2 of the longitudinal flow path pitch, the longitudinal flow path along the plate length direction becomes a contactless through flow path in the plate bundle, and the lateral flow path along the plate width direction becomes a lateral through flow path with a contact.
Referring to fig. 8, the sheet constituting the present invention is provided with a folding path corrugation 5 in the same direction as the folding path corrugation. When the number of the pass-dividing corrugations on the plate is m, and the number of the pass-dividing corrugations corresponds to the number of the longitudinal flow passes of the plate, namely m+1, the baffle corrugations are arranged at the outlet of the nth pass and the inlet of the n+1th pass, and the medium B can directly realize multi-pass baffle in the plate bundle without arranging a pass-dividing pipe box, so that the structural compactness of the plate bundle is greatly improved.
As shown in fig. 9 and 10, the supporting corrugation 6 or the supporting strip 7 is additionally arranged on the plate for forming the plate bundle of the invention, the transverse flow channel of the original medium A in the plate bundle is divided into a plurality of small transverse flow channels, the height and the original characteristics of the transverse flow channels are not affected, and the original uniform flow field is not affected.
Furthermore, the pressure-bearing wave, the turbulent wave, the branch wave and the folding wave can be replaced by structural members such as columns, ribs and the like, and the plate bundle formed by the plate sheets derived from the pressure-bearing wave, the turbulent wave, the branch wave and the folding wave has the same innovation and novelty as the invention and is also considered as the protection scope of the invention.
Furthermore, on the premise of keeping the corrugated form of the plates of the invention unchanged, by adding supporting pieces between the plates or adding supporting pieces around the plates, the plates do not need to be buckled into plate pairs in pairs, and a plurality of identical plates are directly stacked into a plate bundle, and the plate bundle has a corrugated plate bundle with the same flow channel structure and flow path combination as the invention, namely the plate bundle has the same innovation and novelty as the invention, and the structure is also considered as the protection scope of the invention.
The foregoing is merely a preferred embodiment of the present invention and it should be noted that modifications and adaptations to those skilled in the art may be made without departing from the principles of the present invention, which are intended to be comprehended within the scope of the present invention.
Claims (10)
1. A corrugated sheet bundle of a single-sided contactless through runner, characterized by: the heat exchanger comprises a plurality of plates, wherein the plates comprise a main heat transfer surface, turbulent flow waves uniformly distributed on the main heat transfer surface, pressure bearing waves and branch path waves extending from one end to the other end along the length direction of the plates, and the heat exchanger is characterized in that: after a plurality of plates are stacked, longitudinal channels along the length direction of the plates and transverse channels along the width direction of the plates are formed on two sides of the plates, the height of the turbulence waves is smaller than 1/2 of the runner spacing of the transverse channels, the height of the pressure waves and the branching waves is equal to 1/2 of the runner spacing of the longitudinal channels, contacts are formed in the longitudinal channels by the opposite pressure waves and the pressure waves, contacts are formed in the opposite branching waves and the branching waves, and no contacts are formed in the transverse channels by the opposite turbulence waves and the turbulence waves.
2. A corrugated plate bundle of a single-sided contactless through flow passage according to claim 1, characterized in that the plates are formed around by bending to form an inlet and an outlet, the plates are buckled in pairs to form plate pairs, and the corrugated plate bundle comprises a plurality of plate pairs stacked on each other.
3. A corrugated sheet bundle for a single-sided contactless through flow channel according to claim 1, characterized in that the periphery of the sheet is in the same plane as the main heat transfer surface, and that the sheet bundles are stacked in sequence by means of strips arranged around the sheet, in a sheet-strip-sheet sequence.
4. A corrugated sheet bundle of one-sided contactless through flow channels according to any one of claims 1 to 3, characterized in that the branched corrugations are straight corrugations or approximately straight corrugations penetrating in the sheet length direction or interrupted at one end, the interruption of the branched corrugations being provided with folded corrugations arranged in a semicircular arc or a zigzag shape, the folded corrugations being continuous or interrupted corrugations and being concave corrugations with respect to the main heat transfer surface.
5. A corrugated plate bundle of a single-sided contactless through flow passage according to claim 4, characterized in that the plate is provided with continuous or intermittent support corrugations or support strips at intervals in the width direction of the plate, the support corrugations being convex corrugations with respect to the main heat transfer surface, the support strips being bosses with respect to the main heat transfer surface, the depth of the support corrugations and the height of the support strips being equal to 1/2 of the flow passage spacing of the transverse passage.
6. The corrugated plate bundle is characterized by comprising a plurality of plates, wherein each two pairs of plates are buckled to form plate pairs, each corrugated plate bundle comprises a plurality of plate pairs which are mutually overlapped, each plate comprises a main heat transfer surface, turbulent flow waves and pressure bearing waves which are uniformly distributed on the main heat transfer surface and branched path waves which are arranged at one end of the heat transfer surface and extend towards the other end, each pressure bearing wave is convex waves relative to the main heat transfer surface, each branched path wave is concave waves relative to the main heat transfer surface, after a plurality of plates are overlapped, longitudinal channels along the length direction of the plates and transverse channels along the width direction of the plates are formed at two sides of the plates, the height of each turbulent flow wave is smaller than 1/2 of the channel spacing of the longitudinal channels, the height of each pressure bearing wave is equal to 1/2 of the channel spacing of the longitudinal channels, each branched path wave is straight waves which are arranged on the plate and are arranged at a certain interval along the width direction of the plate, each supporting convex wave is a supporting strip or a supporting strip which is equal to the height of each supporting strip along the width direction of the plate, and the height of each supporting strip is equal to 1/2 of the supporting strip relative to the main heat transfer surface.
7. A corrugated sheet bundle of a single-sided contactless through runner, characterized by: the heat exchanger comprises a plurality of plates, wherein each plate comprises a main heat transfer surface, pressure-bearing waves uniformly distributed on the main heat transfer surface and branch-path waves which are arranged at one end of the heat transfer surface and extend towards the other end, the pressure-bearing waves and the branch-path waves are concave waves relative to the main heat transfer surface, after a plurality of plates are assembled, longitudinal channels along the length direction of the plates and transverse channels along the width direction of the plates are formed at two sides of the plates, the height of the pressure-bearing waves and the height of the branch-path waves are equal to 1/2 of the flow channel spacing of the longitudinal channels, the branch-path waves are straight waves penetrating along the length direction of the plates or with one end being intermittent, the plates are provided with continuous or intermittent support waves or support strips at certain intervals along the width direction of the plates, the support waves are convex waves relative to the main heat transfer surface, the depth of the support waves and the height of the support strips are equal to 1/2 of the flow channel spacing of the transverse channels, and the branch-path waves at the intermittent positions of the support waves are provided with semicircular or broken waves arranged in a fold shape, and the broken waves are continuous or intermittent waves relative to the main heat transfer surfaces.
8. The corrugated plate bundle of a single-sided contactless through flow channel according to claim 7, wherein the plate sheet is formed around by bending to form an inlet and an outlet, the plate sheet is buckled in pairs to form plate pairs, and the corrugated plate bundle comprises a plurality of plate pairs stacked on each other.
9. A corrugated sheet bundle for a single-sided contactless through flow channel according to claim 7, wherein the periphery of the sheet is in the same plane as the main heat transfer surface, and the sheet bundles are stacked in sequence by means of strips provided around the sheet, and by means of a sheet-strip-sheet sequence.
10. The corrugated plate bundle is characterized by comprising a plurality of plates, wherein each two pairs of plates are buckled to form plate pairs, each corrugated plate bundle comprises a plurality of plate pairs which are mutually overlapped, each plate comprises a main heat transfer surface, pressure-bearing waves uniformly distributed on the main heat transfer surface and split-path waves which are arranged at one end of the heat transfer surface and extend towards the other end, each pressure-bearing wave is convex with respect to the main heat transfer surface, each split-path wave is concave with respect to the main heat transfer surface, after a plurality of plates are overlapped, longitudinal channels along the length direction of the plates and transverse channels along the width direction of the plates are formed at two sides of the plates, the height of each pressure-bearing wave is equal to 1/2 of the inter-plate channel spacing of the transverse channels, each split-path wave is a continuous or discontinuous supporting wave or a straight supporting wave which is arranged at a certain interval along the width direction of the plate, the supporting wave is equal to 1/2 of the inter-plate channel spacing, and the supporting wave is convex with respect to the main heat transfer surface.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610065886.7A CN107024124B (en) | 2016-02-01 | 2016-02-01 | Corrugated plate bundle of single-side contactless straight-through runner |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610065886.7A CN107024124B (en) | 2016-02-01 | 2016-02-01 | Corrugated plate bundle of single-side contactless straight-through runner |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN107024124A CN107024124A (en) | 2017-08-08 |
| CN107024124B true CN107024124B (en) | 2023-09-08 |
Family
ID=59524811
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610065886.7A Active CN107024124B (en) | 2016-02-01 | 2016-02-01 | Corrugated plate bundle of single-side contactless straight-through runner |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107024124B (en) |
Families Citing this family (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107875835A (en) * | 2017-12-07 | 2018-04-06 | 天津华赛尔传热设备有限公司 | A kind of flue gas of slurries cooling mixes wind and disappeared white system |
| CN108499334A (en) * | 2017-12-07 | 2018-09-07 | 天津华赛尔传热设备有限公司 | A kind of flue gas of tower condensed exterior mixes wind and disappears white system |
| CN107875800A (en) * | 2017-12-07 | 2018-04-06 | 天津华赛尔传热设备有限公司 | The flue gas to dehumidify outside a kind of tower disappears white system |
| CN107875818A (en) * | 2017-12-07 | 2018-04-06 | 天津华赛尔传热设备有限公司 | A kind of white desulfurizing tower that disappears of slurries cooling |
| CN108126482A (en) * | 2017-12-07 | 2018-06-08 | 天津华赛尔传热设备有限公司 | A kind of heating agent flue gas of tower condensed exterior disappears white system |
| CN107975817A (en) * | 2017-12-07 | 2018-05-01 | 天津华赛尔传热设备有限公司 | A kind of white absorption tower that disappears of flue gas heating |
| CN107940492A (en) * | 2017-12-07 | 2018-04-20 | 天津华赛尔传热设备有限公司 | A kind of white absorption tower that disappears of heating agent circulation |
| CN108662928A (en) * | 2018-06-14 | 2018-10-16 | 北京兴晟科技有限公司 | A kind of slurries heat-exchanger rig |
| FR3083597B1 (en) * | 2018-07-05 | 2021-01-22 | Nexson Group | PLATE FOR HEAT EXCHANGER AND HEAT EXCHANGER INCLUDING THE PLATE |
| CN109405604A (en) * | 2018-12-07 | 2019-03-01 | 山东北辰机电设备股份有限公司 | A kind of multi-functional full welded plate piece |
| CN109443055A (en) * | 2018-12-07 | 2019-03-08 | 山东北辰机电设备股份有限公司 | A kind of desulfurization slurry heat exchanger |
| CN110220400B (en) * | 2019-05-17 | 2024-03-29 | 天津华赛尔传热设备有限公司 | All-welded plate type gas-gas heat exchanger |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101806552A (en) * | 2010-05-20 | 2010-08-18 | 甘肃蓝科石化高新装备股份有限公司 | Corrugated sheet structure for welded plate type heat exchanger |
| CN205718592U (en) * | 2016-02-01 | 2016-11-23 | 天津华赛尔传热设备有限公司 | The corrugated board cluster of a kind of one side is contactless straight-through runner |
-
2016
- 2016-02-01 CN CN201610065886.7A patent/CN107024124B/en active Active
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101806552A (en) * | 2010-05-20 | 2010-08-18 | 甘肃蓝科石化高新装备股份有限公司 | Corrugated sheet structure for welded plate type heat exchanger |
| CN205718592U (en) * | 2016-02-01 | 2016-11-23 | 天津华赛尔传热设备有限公司 | The corrugated board cluster of a kind of one side is contactless straight-through runner |
Also Published As
| Publication number | Publication date |
|---|---|
| CN107024124A (en) | 2017-08-08 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN107024124B (en) | Corrugated plate bundle of single-side contactless straight-through runner | |
| AU2016201413B2 (en) | Heating element undulation patterns | |
| US4131159A (en) | Heat exchanger | |
| CN202267394U (en) | Primary surface heat exchanger for flue gas waste heat recovery | |
| US20020011331A1 (en) | Heat-exchange fin for a brazed-plate heat exchanger, and corresponding heat exchanger | |
| NL8200707A (en) | HEAT EXCHANGER WITH PERFORATED PLATES. | |
| GB1153403A (en) | Plate Type Heat Exchangers. | |
| CN107314699B (en) | High-performance heat exchange fin for heat exchanger and heat exchanger with high-performance heat exchange fin | |
| CN106979714B (en) | Rhombic fin tube bundle | |
| CN102954459A (en) | Novel plate type economizer | |
| CN215832532U (en) | Cross flow plate type heat exchange plate | |
| CN210321338U (en) | Plate-shell type heat exchanger based on circular micro-channel wavy-surface heat exchange plate | |
| CN203336568U (en) | Plate-type economizer | |
| CN107023817B (en) | Low-temperature economizer with straight-through structure | |
| CN212390622U (en) | Heat exchange device and water heater | |
| CN110360858B (en) | Heat exchanger plate bundle for phase change heat exchange | |
| CN107024133B (en) | Sheet of unilateral contactless straight-through runner | |
| CN207501760U (en) | Two-layer spiral heat exchanger | |
| JP2005195190A (en) | Multiplate heat exchanger | |
| CN203432434U (en) | Band fin cast plate-type air pre-heater | |
| US1751757A (en) | Heat exchanger | |
| CN212378563U (en) | Corrugated plate gas-gas heat exchanger | |
| CN211012600U (en) | Gas-liquid plate heat exchanger | |
| CN211012601U (en) | Gas-gas plate type heat exchanger | |
| CN203431917U (en) | Casting plate type air preheater with baffling fins |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant |