CN204438866U - A kind of Novel plate heat exchanger - Google Patents
A kind of Novel plate heat exchanger Download PDFInfo
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- CN204438866U CN204438866U CN201420851293.XU CN201420851293U CN204438866U CN 204438866 U CN204438866 U CN 204438866U CN 201420851293 U CN201420851293 U CN 201420851293U CN 204438866 U CN204438866 U CN 204438866U
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- heat exchanger
- distributor
- wave card
- fin
- plate heat
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Abstract
The utility model provides a kind of Novel plate heat exchanger, plate type heat exchanger is provided with corrugated plate group, corrugated plate group comprises first wave card and the Second Wave card of the stacked setting in interval, a corner apertures of first wave card is other is provided with the first distributor, and the sidewall of a corner apertures of Second Wave card is provided with the second distributor; The medium that first distributor of multiple coaxial setting and the second distributor form plate type heat exchanger distributes passage.First distributor comprises fin and outer fin in annular, and the height of outer fin, higher than the height of interior fin, forms fluid cavity between interior fin and outer fin; Second distributor comprises two the axial dispensing orifices be connected with Second Wave card corner apertures, is also provided with arc distribution plate between dispensing orifice.A kind of Novel plate heat exchanger provided by the utility model, by improving sheet structure and dispensing arrangement, while further increasing the heat exchanger effectiveness of plate type heat exchanger, also has fluid chemical field abundant, and fluid flowing is even, the advantage that flow resistance is low.
Description
Technical field
The utility model relates to plate type heat exchanger and manufactures field, is specially a kind of plate type heat exchanger with Novel sheet bar and distributor.
Background technology
Plate type heat exchanger can play its advantage under the operating mode of single-phase heat exchange, but in two-phase heat-exchanging state, because the difference such as physical property, fluidised form of gas-liquid two-phase fluid is larger, be difficult to realize fluid well-distributing distribute and uniform flow flowing in runner between plate, when especially gas-liquid two-phase mix refrigerant is sprayed by distributor apertures the liquid refrigerant of high pressure, abundant atomization cannot be realized, thus affect the quick volatilization of liquid refrigerant, and then increase flow resistance, reduce the heat exchange property of heat exchanger.In addition in the runner of the equally distributed plate composition of ripple, the assignment of traffic of fluid is uneven, comparatively large, more less away from its flow velocity of this region to the flow velocity of the straight line near zone of outlet from import, in runner, the uneven meeting of assignment of traffic causes flow resistance to increase and the reduction of heat exchanger heat exchange property.After gas-liquid two-phase mix refrigerant enters distributor, fully cannot be mixed, thus make flow resistance comparatively large, flow can not effectively uniform distribution and between plate Uniform Flow in runner, thus make that heat exchanger pressure drop is comparatively large, heat exchange property reduction.Therefore, require further improvement the structure of plate-type heat exchanger slab and distributor, to obtain best heat exchange property.
Utility model content
For the problems referred to above, the utility model provides one and is provided with Novel plate heat exchanger.
The technical solution adopted in the utility model is, build a kind of Novel plate heat exchanger, above-mentioned plate type heat exchanger is provided with corrugated plate group, above-mentioned corrugated plate group comprises first wave card and the Second Wave card of the stacked setting in interval, a corner apertures of first wave card is other is provided with the first distributor, and the sidewall of a corner apertures of Second Wave card is provided with the second distributor; The medium that above-mentioned first distributor of multiple coaxial setting and the second distributor form plate type heat exchanger distributes passage.Above-mentioned first distributor comprises fin and outer fin in annular, and the height of above-mentioned outer fin, higher than the height of interior fin, forms fluid cavity between above-mentioned interior fin and outer fin; Above-mentioned second distributor comprises two the axial dispensing orifices be connected with Second Wave card corner apertures, is also provided with arc distribution plate between above-mentioned dispensing orifice.
Further, above-mentioned outer fin is also provided with many medium dispersion slots, the bottom land of above-mentioned distribution dispersion slot lower than the peak of above-mentioned interior fin, higher than the minimum point of above-mentioned fluid cavity.While being conducive to reducing flow resistance, force fluid to start flowing along the plate ripple away from fluid distributor opposite side, make flow distribution of fluid between plate more even, improve plate heat exchanger effectiveness.
Further, the cross section of above-mentioned dispersion slot is circular arc or ellipse arc.
Further, above-mentioned multiple dispersion slot helically centrifugal type distribution or radial type distribution around corner apertures center.Force fluid to start flowing along the plate ripple away from fluid distributor opposite side, make flow distribution of fluid between plate more even, improve plate heat exchanger effectiveness.
Further, the side of above-mentioned second distributor is other is provided with annular heavy stand face, and the upper surface of above-mentioned annular heavy stand face and above-mentioned Second Wave card forms cylindrical cavity.Be mainly used in abundant mixing.
Further, above-mentioned first wave card and Second Wave card are equipped with boss and the pit of multiple positions form fit.For the screens clamping when assembling, make whole corrugated plate group firm stable more.
Further, above-mentioned interior fin is also provided with many gathering sills.For direct fluid and reduction flow resistance.
Compared with prior art, a kind of Novel plate heat exchanger provided by the utility model, by improving sheet structure and dispensing arrangement, while further increasing the heat exchanger effectiveness of plate type heat exchanger, also have fluid chemical field abundant, fluid flowing is even, the advantage that flow resistance is low.
Accompanying drawing explanation
Fig. 1 is the utility model schematic perspective view.
Fig. 2 is the structural representation of the utility model first wave card.
Fig. 3 is the structural representation of the utility model Second Wave card.
Fig. 4 is the structural representation of utility model first distributor.
Fig. 5 is the structural representation of the utility model second distributor.
Detailed description of the invention
Set forth a lot of detail in the following description so that fully understand the utility model.But the utility model can be much different from alternate manner described here to implement, those skilled in the art can when doing similar popularization without prejudice to when the utility model intension, and therefore the utility model is by the restriction of following public specific embodiment.
Below in conjunction with drawings and Examples, detailed description of the invention of the present utility model is described further.
embodiment 1
In the present embodiment, by reference to the accompanying drawings, structure of the present utility model is described in detail.
Refer to accompanying drawing, a kind of Novel plate heat exchanger that the utility model provides, which is provided with corrugated plate group, corrugated plate group comprises first wave card 1 and the Second Wave card 2 of the stacked setting in interval, a corner apertures of first wave card 1 is other is provided with the first distributor 11, and the sidewall of a corner apertures of Second Wave card 2 is provided with the second distributor 21; The medium that first distributor 11 of multiple coaxial setting and the second distributor 21 form plate type heat exchanger distributes passage.First distributor 11 comprises fin 111 and outer fin 112 in annular, and the height of outer fin 112, higher than the height of interior fin 111, forms fluid cavity 113 between interior fin 111 and outer fin 112; Second distributor 21 comprises two the axial dispensing orifices 211 be connected with Second Wave card corner apertures, is also provided with arc distribution plate 212 between dispensing orifice 211.
As preferably, outer fin 112 is also provided with many medium dispersion slots 1121, distribute the peak of bottom land lower than interior fin 111 of dispersion slot 1121, higher than the minimum point of fluid cavity 113, the cross section of dispersion slot 1121 is circular arc or ellipse arc, multiple dispersion slot 1121 is helically centrifugal type distribution or radial type distribution around corner apertures center, and interior fin 111 is also provided with many gathering sills 1111.
As preferably, is provided with annular heavy stand face 213 by the side of the second distributor 21, annular heavy stand face 213 forms cylindrical cavity with the upper surface of Second Wave card 2.
As preferably, first wave card 1 and Second Wave card 2 are equipped with boss and the pit of multiple positions form fit.
Although the utility model with preferred embodiment openly as above; but it is not for limiting the utility model; any those skilled in the art are not departing from spirit and scope of the present utility model; can make possible variation and amendment, the scope that therefore protection domain of the present utility model should define with the utility model claim is as the criterion.
Claims (8)
1. a Novel plate heat exchanger, described plate type heat exchanger is provided with corrugated plate group, it is characterized in that, described corrugated plate group comprises first wave card (1) and the Second Wave card (2) of the stacked setting in interval, a corner apertures of first wave card (1) is other is provided with the first distributor (11), and the sidewall of a corner apertures of Second Wave card (2) is provided with the second distributor (21); The medium that described first distributor (11) of multiple coaxial setting and the second distributor (21) form plate type heat exchanger distributes passage.
2. a kind of Novel plate heat exchanger according to claim 1, it is characterized in that, described first distributor (11) comprises fin (111) and outer fin (112) in annular, the height of described outer fin (112), higher than the height of interior fin (111), forms fluid cavity (113) between described interior fin (111) and outer fin (112); Described second distributor (21) comprises two the axial dispensing orifices (211) be connected with Second Wave card corner apertures, is also provided with arc distribution plate (212) between described dispensing orifice (211).
3. a kind of Novel plate heat exchanger according to claim 1, it is characterized in that, described outer fin (112) is also provided with many medium dispersion slots (1121), the bottom land of described distribution dispersion slot (1121) lower than the peak of described interior fin (111), higher than the minimum point of described fluid cavity (113).
4. a kind of Novel plate heat exchanger according to claim 3, is characterized in that, the cross section of described dispersion slot (1121) is circular arc or ellipse arc.
5. a kind of Novel plate heat exchanger according to claim 3, is characterized in that, described multiple dispersion slot (1121) is helically centrifugal type distribution or radial type distribution around corner apertures center.
6. a kind of Novel plate heat exchanger according to claim 1, it is characterized in that, the side of described second distributor (21) is other is provided with annular heavy stand face (213), and described annular heavy stand face (213) forms cylindrical cavity with the upper surface of described Second Wave card (2).
7. a kind of Novel plate heat exchanger according to claim 1, is characterized in that, described first wave card (1) and Second Wave card (2) is equipped with boss and the pit of multiple positions form fit.
8. a kind of Novel plate heat exchanger according to claim 1, is characterized in that, described interior fin (111) is also provided with many gathering sills (1111).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201420851293.XU CN204438866U (en) | 2014-12-30 | 2014-12-30 | A kind of Novel plate heat exchanger |
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CN201420851293.XU CN204438866U (en) | 2014-12-30 | 2014-12-30 | A kind of Novel plate heat exchanger |
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CN204438866U true CN204438866U (en) | 2015-07-01 |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107684817A (en) * | 2016-08-03 | 2018-02-13 | 天津华赛尔传热设备有限公司 | A kind of flue gas desulfurization process system |
CN108759528A (en) * | 2018-07-24 | 2018-11-06 | 江阴市亚龙换热设备有限公司 | Novel plate heat exchanger |
CN108759529A (en) * | 2018-07-24 | 2018-11-06 | 江阴市亚龙换热设备有限公司 | High heat transfer rate plate heat exchanger |
CN116086219A (en) * | 2023-01-06 | 2023-05-09 | 浙江英特科技股份有限公司 | Plate heat exchanger with distribution hole structure |
-
2014
- 2014-12-30 CN CN201420851293.XU patent/CN204438866U/en active Active
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107684817A (en) * | 2016-08-03 | 2018-02-13 | 天津华赛尔传热设备有限公司 | A kind of flue gas desulfurization process system |
CN108759528A (en) * | 2018-07-24 | 2018-11-06 | 江阴市亚龙换热设备有限公司 | Novel plate heat exchanger |
CN108759529A (en) * | 2018-07-24 | 2018-11-06 | 江阴市亚龙换热设备有限公司 | High heat transfer rate plate heat exchanger |
CN116086219A (en) * | 2023-01-06 | 2023-05-09 | 浙江英特科技股份有限公司 | Plate heat exchanger with distribution hole structure |
CN116086219B (en) * | 2023-01-06 | 2023-11-24 | 浙江英特科技股份有限公司 | Plate heat exchanger with distribution hole structure |
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