CN104279894A - Stacked heat exchanger - Google Patents
Stacked heat exchanger Download PDFInfo
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- CN104279894A CN104279894A CN201410491310.8A CN201410491310A CN104279894A CN 104279894 A CN104279894 A CN 104279894A CN 201410491310 A CN201410491310 A CN 201410491310A CN 104279894 A CN104279894 A CN 104279894A
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Abstract
The invention discloses a stacked heat exchanger which comprises core veneers. Pore passages are chiseled in each core veneer, and two ends of each pore passage are communicated. Equivalent spacing between every two adjacent pore passages is not more than 3mm. The spacing between each pore passage and the lower surface of each core veneer is not more than 2mm; the core veneers are similar in structure. The core veneers are stacked together, and the projection directions of the pore passages between layers form a 90-degree included angle. After the two layers of core veneers are stacked, edge gaps between the two layers are required to be sealed. The periphery of a stacked core is sealed with a casing and the edge of each pore passage surface. A fluid medium 1 flows into the heat exchange core from an inlet of the casing and flows out from an outlet. Another fluid medium flows into the heat exchange core from an inlet and flows out from an outlet. The stacked heat exchanger has the advantages that the heat exchanger as a whole is compact in structure, high in heat exchange efficiency, convenient to mount and simple in structure.
Description
Technical field
The invention belongs to fluid heat transfer and augmentation of heat transfer field, relate to and a kind of there is the stacked heat exchanger device that structure is simple, heat exchange efficiency is high, can be widely used in various heat transfer process.In this core body, direction, different core layer duct is vertical, mutually completely cuts off between central layer.
Background technology
Heat exchanger can be widely applied in industrial production.Traditional heat exchanger mostly is pipe heat exchanger, and a kind of fluid is at Bottomhole pressure, and another fluid is in the outer flowing of pipe, and the temperature difference between fluid is by the form transmission of heat conduction.But tube wall heat exchange or general passage interlayer heat exchange, because heat exchange area is little, the restriction of the conditions such as pipe thickness, is difficult to realize high efficient heat exchanging.Need to develop a kind of heat exchanger, there is structure simple, the advantages such as heat exchange efficiency is high, and heat exchange reference area is large.For this reason, Many researchers develops the heat exchanger apparatus with different structure.
Application number is disclose a kind of heat exchanger in the patent of 200580032906.0, it implants bending fan-folded metallic plate in heat exchange core body, replace formation first and second runner in a thickness direction, each first flow two ends are blocked by a pair comb member, and fin is arranged in the second runner.This heat exchanger effectively can realize heat exchange, but complex structure, first flow is platy structure, and heat exchange efficiency has to be strengthened.Application number is disclose a kind of heat exchanger in the patent of 201410006129.3, this heat exchanger comprises the first header and second header of spaced apart preset distance, and multiple flat tube to be spaced apart and arranged between the first header and the second header and to be communicated with the first header and the second header.Inside and outside tube wall, form flowing by the mode in alter direction, thus reach the object of heat exchange.
Summary of the invention
The invention provides a kind of high efficient heat exchanging, structure is simple, workable stacked heat exchanger device.
Technical scheme of the present invention is as follows:
A kind of stacked heat exchanger device, comprises,
First central layer: in this central layer, carve the duct being carved with different size and shape, two ends, duct are penetrating; With layer duct parallel arranged, the equivalent spacing between adjoining cell channels is not more than 3mm, and the combination of each duct and central layer can be groove structure, also can be tunnel structure.Spacing between duct and the lower surface of central layer is not more than 2mm.
Second central layer: similar to the first core plate structure, the equivalent spacing between duct is changeable compared with the first central layer, and between duct, wall thickness also can be different from wall thickness between the first central layer.First central layer is stacked on the second central layer.Direction, duct on second central layer and the duct projecting direction of the first central layer are 90 degree of angles.First central layer and the second central layer pile the edge slot that poststack needs between sealing two layers.After sealing, the first central layer and the stacking formation one of the second central layer, continue stacking with the 3rd central layer.3rd central layer is identical with the structure of the first central layer.The direction, duct of the 3rd central layer and the duct projecting direction of the second central layer are 90 degree of angles.Equally, seal the 3rd central layer and the second central layer pile poststack two-layer between gap.The central layer number of plies is not limited to 3 layers, can be multilayer, for multilayer orifice plate stacking according to the method described above.
Heap poststack, forms Integral heat-exchange core body.The face, alternate layer by layer duct that this core body is 90 degree of angles by two projecting directions forms.The edge seal in the periphery of this core body and casing and face, each duct.
Fluid media (medium) A flows into heat exchange core body by first import of described casing, flows out through the first outlet.Fluid media (medium) B flows into heat exchange core body via second import, flows out through second outlet.There is temperature difference between fluid media (medium) A and fluid media (medium) B, after flowing through heat exchange core body, complete heat transfer process.
Described stacked heat exchanger device, the cross section in duct can be square, circular or other shapes.The hydraulic diameter size in duct is between 1-5mm.
Described stacked heat exchanger device, the spacing between two ducts is not more than 3mm.
Described stacked heat exchanger device, the material of central layer can be metal material, also can be plastics, ceramic nonmetallic.
The present invention has following obvious advantage and outstanding effect: heat exchanger integrally, utilize the thin layer heat conduction of wall to realize heat exchange, compact overall structure, the fluid media (medium) heat exchange from combustion high temperature flue gas to lower temperature can be realized, heat-exchange temperature scope is large, and efficiency is high.Whole heat exchanger simple installation, structure is simple.
Accompanying drawing explanation
Fig. 1 is the stacking decomposing schematic representation of central layer.
Fig. 2 is overall heat exchange core and the fluid media (medium) flowing schematic diagram of heap poststack.
Fig. 3 is a complete stacked heat exchanger device outside drawing.
Fig. 4 is a complete stacked heat exchanger device top view figure.
In figure: 1 first central layer; 2 second central layers; 3 the 3rd central layers; 4 Integral heat-exchange core bodys; 5 casings; 6 first imports; 7 first outlets; 2; 8 second imports; 9 second outlets; 10 ducts; 11 fluid media (medium) A; 12 fluid media (medium) B.
Detailed description of the invention
Below by embodiment and accompanying drawing, technical scheme of the present invention is described in further detail.
For implementing the decomposing schematic representation of stacking heat exchanger shown in Fig. 1 according to the present invention.As shown in Figure 1, in the first central layer of heat exchanger, carve the duct (10) being carved with different size and shape, duct (10) two ends are penetrating; With layer duct parallel arranged, the equivalent spacing between adjoining cell channels is not more than 3mm, and the combination of each duct and central layer can be groove structure, also can be tunnel structure.Spacing between duct and the lower surface of central layer is not more than 2mm;
Second central layer is identical with the first core plate structure.First central layer is stacked on the second central layer.Direction, duct on second central layer and the duct projecting direction of the first central layer are 90 degree of angles.First central layer and the second central layer pile the edge slot that poststack needs between sealing two layers.After sealing, the first central layer and the stacking formation one of the second central layer, continue stacking with the 3rd central layer.3rd central layer is identical with the structure of the first central layer, the second central layer.The direction, duct of the 3rd central layer and the duct projecting direction of the second central layer are 90 degree of angles.Equally, seal the 3rd central layer and the second central layer pile poststack two-layer between gap.The central layer number of plies is not limited to 3 layers, can be multilayer, for multilayer orifice plate stacking according to the method described above.
Heap poststack, forms Integral heat-exchange core body (4), as shown in Figure 2.In the overall heat exchange core of heap poststack, the face, alternate layer by layer duct that this core body is 90 degree of angles by both direction forms.Fluid media (medium) flows respectively in the mutually different duct of same layer, and two kinds of fluid media (medium)s circulate respectively between adjacent core layer, do not mix mutually.As shown in Figure 3 and Figure 4, the edge seal in the periphery of this heat exchange core body and casing (5) and face, each duct, realizes the independence of the fluid media (medium) flowing of both direction.Fluid media (medium) A flows into heat exchange core body (4) by first import (6) of described casing (5), flows out through the first outlet (7).Fluid media (medium) B flows into heat exchange core body (4) via second import (8), flows out through second outlet (9).There is temperature difference between fluid media (medium) A and fluid media (medium) B, after flowing through heat exchange core body, complete heat transfer process.
Described stacked heat exchanger device, the cross section of duct (10) can be square, circular or other shapes.The hydraulic diameter size in duct (10) is between 1-5mm.
Described stacked heat exchanger device, the spacing between two ducts is not more than 3mm.
Described stacked heat exchanger device, the material of central layer can be metal material, also can be plastics, ceramic nonmetallic.
Claims (9)
1. a stacked heat exchanger device, its feature is as follows, and this stacked heat exchanger device comprises,
First central layer: in this central layer, carve the duct (10) being carved with different size and shape, duct (10) two ends are penetrating; With layer duct parallel arranged, the equivalent spacing between adjoining cell channels is not more than 3mm; Spacing between the lower surface of duct and the first central layer is not more than 2mm;
Second central layer: similar to the first core plate structure, also equivalent spacing between duct that equivalent spacing between the duct being carved with duct (10) second central layer of different size and shape is different from the first central layer is carved, wall thickness between wall thickness identical or different and the first central layer between the second central layer duct; First central layer is stacked on the second central layer; Direction, duct on second central layer and the duct projecting direction of the first central layer are 90 degree of angles; First central layer and the second central layer pile the edge slot that poststack needs between sealing two layers;
First central layer and the stacking formation one of the second central layer, continue stacking with the 3rd central layer; 3rd central layer is identical with the structure of the first central layer; The direction, duct of the 3rd central layer and the duct projecting direction of the second central layer are 90 degree of angles; Equally, the 3rd central layer of sealing and the second central layer pile poststack two-layer between gap;
The edge seal in the periphery of this Integral heat-exchange core body (4) and casing (5) and face, each duct; Fluid media (medium) A (11) flows into heat exchange core body (4) by first import (6) of described casing (5), flows out through the first outlet (7); Fluid media (medium) B (12) flows into heat exchange core body (4) via second import (8), flows out through second outlet (9); There is temperature difference between fluid media (medium) A (11) and fluid media (medium) B (12), after flowing through heat exchange core body, complete heat transfer process.
2. a kind of stacked heat exchanger device according to claim 1, its feature is as follows, and each duct (10) are combined as groove structure or tunnel structure with central layer.
3. a kind of stacked heat exchanger device according to claim 1 and 2, its feature is as follows, the cross section of duct (10) be square or, circular.
4. a kind of stacked heat exchanger device according to claim 3, its feature is as follows, and the hydraulic diameter size of duct (10) is 1-5mm.
5. a kind of stacked heat exchanger device according to claim 1,2 or 4, its feature is as follows, and the material of central layer is metal material, plastics or pottery.
6. a kind of stacked heat exchanger device according to claim 3, its feature is as follows, and the material of central layer is metal material, plastics or pottery.
7. a kind of stacked heat exchanger device according to claim 1,2,4 or 6, its feature is as follows, and the central layer number of plies is multilayer, presses the mode of three layers of central layer for multilayer orifice plate stacking.
8. a kind of stacked heat exchanger device according to claim 3, its feature is as follows, and the central layer number of plies is multilayer, presses the mode of three layers of central layer for multilayer orifice plate stacking.
9. a kind of stacked heat exchanger device according to claim 5, its feature is as follows, and the central layer number of plies is multilayer, presses the mode of three layers of central layer for multilayer orifice plate stacking.
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CN201410491310.8A CN104279894A (en) | 2014-09-23 | 2014-09-23 | Stacked heat exchanger |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108180773A (en) * | 2018-01-29 | 2018-06-19 | 西安热工研究院有限公司 | A kind of interruption fin structure printed circuit board heat exchanger core body |
CN108180776A (en) * | 2018-01-19 | 2018-06-19 | 上海凯泉泵业(集团)有限公司 | A kind of entirety dividing wall type heat exchanger |
CN110319729A (en) * | 2019-07-10 | 2019-10-11 | 陕西益信伟创智能科技有限公司 | Heat exchanger core body and heat exchanger based on bionical stacking 3-d modelling |
CN112071453A (en) * | 2019-05-25 | 2020-12-11 | 孟想 | Design scheme of direct-current countercurrent pore channel type heat exchanger/evaporator |
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FR2469684A1 (en) * | 1979-11-13 | 1981-05-22 | Thermo Electronique France Sa | Heat exchanger for two fluids - has modular construction of stacked flat plastics sheets with interposed partitions to form passages |
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CN202083255U (en) * | 2011-04-17 | 2011-12-21 | 江苏新金达机械制造有限公司 | Heat exchanger for catalytic combustion |
EP2426453A1 (en) * | 2009-04-28 | 2012-03-07 | Mitsubishi Electric Corporation | Total heat exchange element |
CN102449421A (en) * | 2009-05-28 | 2012-05-09 | 贝洱两合公司 | Layer heat exchange for high temperatures |
CN204128414U (en) * | 2014-09-23 | 2015-01-28 | 大连理工大学 | A kind of stacked heat exchanger device |
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2014
- 2014-09-23 CN CN201410491310.8A patent/CN104279894A/en active Pending
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
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FR2469684A1 (en) * | 1979-11-13 | 1981-05-22 | Thermo Electronique France Sa | Heat exchanger for two fluids - has modular construction of stacked flat plastics sheets with interposed partitions to form passages |
JPS5974496A (en) * | 1982-10-21 | 1984-04-26 | Matsushita Electric Ind Co Ltd | Plate-type heat exchanger |
DD235322A1 (en) * | 1985-03-13 | 1986-04-30 | Zi D Ministeriums F Bezirksgel | PLATE WATER HEATER IN A QUADRUPT, REMOVABLE FRAME, MADE OF LEVEL GLASS PLATES |
EP2426453A1 (en) * | 2009-04-28 | 2012-03-07 | Mitsubishi Electric Corporation | Total heat exchange element |
CN102449421A (en) * | 2009-05-28 | 2012-05-09 | 贝洱两合公司 | Layer heat exchange for high temperatures |
CN202083255U (en) * | 2011-04-17 | 2011-12-21 | 江苏新金达机械制造有限公司 | Heat exchanger for catalytic combustion |
CN204128414U (en) * | 2014-09-23 | 2015-01-28 | 大连理工大学 | A kind of stacked heat exchanger device |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108180776A (en) * | 2018-01-19 | 2018-06-19 | 上海凯泉泵业(集团)有限公司 | A kind of entirety dividing wall type heat exchanger |
CN108180776B (en) * | 2018-01-19 | 2023-08-01 | 上海凯泉泵业(集团)有限公司 | Integral dividing wall type heat exchanger |
CN108180773A (en) * | 2018-01-29 | 2018-06-19 | 西安热工研究院有限公司 | A kind of interruption fin structure printed circuit board heat exchanger core body |
CN112071453A (en) * | 2019-05-25 | 2020-12-11 | 孟想 | Design scheme of direct-current countercurrent pore channel type heat exchanger/evaporator |
CN110319729A (en) * | 2019-07-10 | 2019-10-11 | 陕西益信伟创智能科技有限公司 | Heat exchanger core body and heat exchanger based on bionical stacking 3-d modelling |
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Application publication date: 20150114 |