CN108571906A - A kind of gas phase adverse current plate heat exchanger - Google Patents
A kind of gas phase adverse current plate heat exchanger Download PDFInfo
- Publication number
- CN108571906A CN108571906A CN201810631774.2A CN201810631774A CN108571906A CN 108571906 A CN108571906 A CN 108571906A CN 201810631774 A CN201810631774 A CN 201810631774A CN 108571906 A CN108571906 A CN 108571906A
- Authority
- CN
- China
- Prior art keywords
- plate
- heat exchange
- heat exchanger
- flanging
- exchange plate
- 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.)
- Pending
Links
- 230000002411 adverse Effects 0.000 title claims abstract description 17
- 238000007789 sealing Methods 0.000 claims abstract description 28
- 230000008676 import Effects 0.000 claims abstract description 23
- 238000005452 bending Methods 0.000 claims description 3
- 238000003466 welding Methods 0.000 claims description 2
- 239000007789 gas Substances 0.000 description 24
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 7
- 239000003546 flue gas Substances 0.000 description 7
- 239000002918 waste heat Substances 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- 238000011084 recovery Methods 0.000 description 4
- 238000005265 energy consumption Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 239000000428 dust Substances 0.000 description 2
- PZZOEXPDTYIBPI-UHFFFAOYSA-N 2-[[2-(4-hydroxyphenyl)ethylamino]methyl]-3,4-dihydro-2H-naphthalen-1-one Chemical compound C1=CC(O)=CC=C1CCNCC1C(=O)C2=CC=CC=C2CC1 PZZOEXPDTYIBPI-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 239000012717 electrostatic precipitator Substances 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000003595 mist Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
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
-
- 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
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
- F28F9/02—Header boxes; End plates
- F28F9/04—Arrangements for sealing elements into header boxes or end plates
- F28F9/16—Arrangements for sealing elements into header boxes or end plates by permanent joints, e.g. by rolling
- F28F9/18—Arrangements for sealing elements into header boxes or end plates by permanent joints, e.g. by rolling by welding
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 discloses a kind of gas phase adverse current plate heat exchangers, including heat exchanger core body, the top of the heat exchanger core body is equipped with upper sealing plate, lower section is equipped with lower sealing plate, and one end end of heat exchanger core body is equipped with thermal current import and cold air discharge port, other end end is equipped with cold airflow import and hot gas outflux, the heat exchanger core body is mutually spliced by multigroup heat exchange beam combination to be formed, heat exchange beam combination is made of heat exchange plate A and heat exchange plate B, the heat exchange plate A and heat exchange plate B forms adjacent and spaced thermal current passway and cold air circulation road after mutually splicing, the thermal current import at the thermal current passway and both ends and hot gas outflux are interconnected, the both ends of the cold air circulation road are interconnected with cold airflow import and cold air discharge port.The present invention exchanges heat the cross-flow of traditional right-angled intersection, is transformed into countercurrent flow, improves temperature difference correction factor, to which total heat transfer efficiency gets a promotion.
Description
Technical field
The present invention relates to the smaller gas waste-heat recycling of a kind of gas phase adverse current plate heat exchanger, the especially temperature difference, specifically
It is a kind of to be commercially used for the adverse current plate heat exchanger of heat exchange or waste heat recovery between the smaller gas of the temperature difference and gas.
Background technology
It being significantly improved with the awareness of saving energy of enterprise, initiative reducing energy consumption increases considerably, therefore, market heat exchanging
Device is in great demand.But during reducing energy consumption, the feelings that the smaller flue gas of the temperature difference needs waste heat recovery are inevitably encountered
Condition, and the cross-flow of traditional gas plate heat exchanger exchanges heat, temperature difference correction factor is less than 1, and some only has 0.85, needs to make
More backhauls, it is bulky.And in many cases, in thermal current all can dust-laden, it is stifled that thermal current dust-laden be easy to cause heat exchanger
Plug.
For at this stage, due to the influence of temperature difference correction factor, the total heat transfer efficiency of traditional gas plate heat exchanger
Can be low, and deashing is more difficult so that system after reducing energy consumption can not stable operation, and when flue-gas temperature is relatively high,
Also the cleaner of the better dust removal effects such as sack cleaner and electrostatic precipitator can not be used to shift to an earlier date dedusting to flue gas, and it is common
Whirlwind or 5 microns of multi-tube dust cleaner pair fine dusts removal rate below are relatively low；Such as use broad passage plate heat exchanger, equipment knot
Dirty stopping state can be alleviated, but waste heat recovery effect is then had a greatly reduced quality, and reason is：Plate channel is excessive, and unit is horizontal
The quantity of heat exchange plate will be greatly decreased in the flue gas flow channel of sectional area, and heat exchange area is insufficient, and expected energy-saving effect is not achieved；
Flue gas flow channel sectional area is such as significantly increased in the case where heat exchange area is constant, then flow velocity of the flue gas in heat exchanger substantially under
Drop, flow velocity decline cause overall heat-transfer coefficient K substantially to reduce, and expected energy-saving effect is still not achieved, and industry energy conservation transformation exists
It is exactly Mist heat recovering to increase the purpose of heat exchanger in smoke evacuation system.
Therefore, flue gas waste heat recovery field is there is an urgent need for a kind of structure type is simply novel, and heat transfer efficiency is high and deashing is convenient
Heat exchanger.
Invention content
The purpose of the present invention is to provide a kind of gas phase adverse current plate heat exchangers, to solve traditional gas plate heat exchanger
Deficiency in the case where the temperature difference is smaller, and it can be suitably used for the hot fluid operating mode of dust-laden.
To achieve the above object, the technical solution adopted by the present invention is that：A kind of gas phase adverse current plate heat exchanger, including heat exchange
Device core, the top of the heat exchanger core body is equipped with upper sealing plate, lower section is equipped with lower sealing plate, and one end end of heat exchanger core body is set
There are thermal current import and cold air discharge port, other end end to be equipped with cold airflow import and hot gas outflux, the heat exchanger core body
Mutually spliced by multigroup heat exchange beam combination and formed, heat exchange beam combination be made of heat exchange plate A and heat exchange plate B, the heat exchange plate A and
Heat exchange plate B forms adjacent and spaced thermal current passway and cold air circulation road, the thermal current passway after mutually splicing
Thermal current import and hot gas outflux with both ends are interconnected, both ends and cold airflow import and the cold air of the cold air circulation road
Outflux is interconnected.
Further, the heat exchange plate A and heat exchange plate B is flanging and one along the left and right ends of gas flow direction
Be divided into two, and with the upper semisection on one side with the flanging direction of lower semisection on the contrary, the upper semisection of corresponding another side and the folding of lower semisection
Edge direction is opposite with two sections of flanging directions of its opposite side.
Further, the both sides up and down of the heat exchange plate A and heat exchange plate B are the upper of flanging and same plate
The flanging setting in the same direction of lower both ends, and the direction of heat exchange plate A and heat exchange plate B upper and lower ends flangings is opposite.
Further, the heat exchange plate A is along the left and right ends of gas flow direction, the wherein upper semisection of one end flanging
Left folding, lower semisection right folding, corresponding other end flanging, upper semisection right folding, lower semisection left folding.
Further, the heat exchange plate B is along the left and right ends of gas flow direction, the wherein upper semisection of one end flanging
Right folding, lower semisection left folding, corresponding other end flanging, upper semisection left folding, lower semisection right folding.
Further, the equal right folding of top and bottom flanging of the heat exchange plate A, the top and bottom of heat exchange plate B
The equal left folding of flanging.
Further, the end of all flangings of surrounding of the heat exchange plate A and heat exchange plate B is equipped with convenient for split simultaneously
The bending edge of welding.
Further, the thermal current in the heat exchanger core body and cold airflow be at countercurrent flow, and thermal current import with it is cold
Airflow inlet is located at same level height, and hot gas outflux is located at same level height with cold air discharge port.
Further, the upper sealing plate is shoot door, and lower sealing plate is ash dropping hopper, and two blocks of sealing plates are movably arranged on heat exchanger
The upper and lower ends of core, for sealing and deashing.
Beneficial effects of the present invention are as follows：
（1）The present invention mainly innovates Conventional plate-type heat exchanger, and the cross-flow of traditional right-angled intersection is exchanged heat, is transformed into
Countercurrent flow improves temperature difference correction factor, to which total heat transfer efficiency is promoted.The outlet of thermal current and the outlet of cold airflow are changed
Heat, temperature difference correction factor 1 are more than cross-flow and exchange heat.
（2）Under the operating mode of dust-laden, upper sealing plate is transformed into shoot door, and lower sealing plate is transformed into ash dropping hopper, can completely and
Thermal current passway intercommunication, can be in negative pressure system without Hand scarf under Parking situation.
（3）The present invention does not specially require template, and applicability is extensive, and flanging width is also without particular requirement, in dust-laden
Under operating mode, high salient point may be selected, the template and flanging of fat pipe are convenient for deashing.
（4）Compared with the prior art, structure of the invention is novel, easy to make, of low cost, and heat transfer efficiency is high, and can use
In dust-laden and the not operating mode of dust-laden.
The additional aspect and advantage of the present invention will be set forth in part in the description, and will partly become from the following description
Obviously, or practice through the invention is recognized.
Description of the drawings
Fig. 1 is the front view of the present invention.
Fig. 2 is the folded edges figure of heat exchange plate A of the present invention.
Fig. 3 is the folded edges figure of heat exchange plate B of the present invention.
Fig. 4 is present invention heat exchange beam combination structural schematic diagram.
Fig. 5 is present invention heat exchanger core schematic diagram.
In figure：1- thermal current imports；2- heat exchanger core bodies；3- cold airflow imports；4- cold air discharge ports；5- hot gas flows out
Mouthful；6- heat exchange plates A；7- heat exchange plates B；8- upper sealing plates；Sealing plate under 9-；10- heat exchange beam combinations；11- thermal current passways；12 cold air
Circulation road, 13- upper channels, 14- lower channels.
Specific implementation mode
The present invention is described in detail with specific embodiment below in conjunction with the accompanying drawings.
Embodiment one.
As shown in Fig. 1 to 5, a kind of gas phase adverse current plate heat exchanger, including heat exchanger core body 2, the heat exchanger core body 2
Top is equipped with upper sealing plate 8, lower section is equipped with lower sealing plate 9, and one end end of heat exchanger core body 2 is equipped with thermal current import 1 and cold air
Outflux 4, other end end are equipped with cold airflow import 3 and hot gas outflux 5, and the heat exchanger core body 2 is by multigroup heat exchange beam combination
10 mutually splicing composition, heat exchange beam combinations 10 are made of heat exchange plate A6 and heat exchange plate B7, the heat exchange plate A6 and heat exchanger plates
Piece B7 forms adjacent and spaced thermal current passway 11 and cold air circulation road 12, the thermal current passway 11 after mutually splicing
Thermal current import 1 and hot gas outflux 5 with both ends are interconnected, both ends and the cold airflow import 3 of the cold air circulation road 12
It is interconnected with cold air discharge port 4.
In the present embodiment, the heat exchange plate A6 and heat exchange plate B7 are flanging along the left and right ends of gas flow direction
And be divided into two, and with the upper semisection on one side with the flanging direction of lower semisection on the contrary, the upper semisection and lower semisection of corresponding another side
Flanging direction it is opposite with two sections of flanging directions of its opposite side.
The both sides up and down of the heat exchange plate A6 and heat exchange plate B7 are the upper and lower ends of flanging and same plate
Flanging setting in the same direction, and the direction of heat exchange plate A6 and heat exchange plate B7 upper and lower ends flangings is opposite.
Embodiment two.
On the basis of embodiment one, the heat exchange plate A6 is rolled over along the left and right ends of gas flow direction, wherein one end
Upper semisection left folding, the lower semisection right folding on side, corresponding other end flanging, upper semisection right folding, lower semisection left folding.The heat exchange plate
B7 is along the left and right ends of gas flow direction, wherein the upper semisection right folding, lower semisection left folding of one end flanging, corresponding other end folding
Side, upper semisection left folding, lower semisection right folding.The equal right folding of top and bottom flanging of the heat exchange plate A6, heat exchange plate B7's is upper
End and the equal left folding of lower end flanging.
The end of all flangings of surrounding of the heat exchange plate A6 and heat exchange plate B7 be equipped with convenient for split and weld
Bending edge.
Thermal current in the heat exchanger core body 2 and cold airflow are at countercurrent flow, and thermal current import 1 and cold airflow import
3 are located at same level height, and hot gas outflux 5 is located at same level height with cold air discharge port 4.
The upper sealing plate 8 is shoot door, and lower sealing plate 9 is ash dropping hopper, and two blocks of sealing plates are movably arranged on heat exchanger core body 2
Upper and lower ends, for sealing and deashing.
To sum up, the present invention is combined into heat exchange beam combination 10 by one A6 of heat exchange plate and heat exchange plate B7, heat exchange beam combination 10
The air-flow of lower channel and left and right sides disengaging runner is connected, and multigroup heat exchange beam combination 10 forms heat exchange core body 2, to prevent heat exchange core
Body air-flow leaks, and upper sealing plate 8 and lower sealing plate 9 is arranged in lower channel, and upper sealing plate 8 can be transformed into shoot door, lower sealing plate 9 can
It is transformed into ash dropping hopper.
The basic principles, main features and advantages of the invention have been shown and described above.Those skilled in the art
It should be appreciated that above-described embodiment protection domain that the invention is not limited in any way, all to be obtained using modes such as equivalent replacements
The technical solution obtained, falls in protection scope of the present invention.
Part that the present invention does not relate to is the same as those in the prior art or can be realized by using the prior art.
Claims (9)
1. a kind of gas phase adverse current plate heat exchanger, including heat exchanger core body, it is characterised in that set above the heat exchanger core body
There are upper sealing plate, lower section to be equipped with lower sealing plate, and one end end of heat exchanger core body is equipped with thermal current import and cold air discharge port, another
End is held to be equipped with cold airflow import and hot gas outflux, the heat exchanger core body is mutually spliced by multigroup heat exchange beam combination to be formed, and is changed
Hot beam combination is made of heat exchange plate A and heat exchange plate B, the heat exchange plate A and heat exchange plate B formed after mutually splicing it is adjacent and
The thermal current import at spaced thermal current passway and cold air circulation road, the thermal current passway and both ends and hot gas outflux
It is interconnected, both ends and the cold airflow import and cold air discharge port of the cold air circulation road are interconnected.
2. a kind of gas phase adverse current plate heat exchanger according to claim 1, it is characterised in that the heat exchange plate A and heat exchange
Plate B is flanging along the left and right ends of gas flow direction and is divided into two, and with the folding of the upper semisection on one side and lower semisection
Edge direction is on the contrary, the upper semisection of corresponding another side is opposite with two sections of flanging directions of its opposite side with the flanging direction of lower semisection.
3. a kind of gas phase adverse current plate heat exchanger according to claim 2, it is characterised in that the heat exchange plate A and heat exchange
The both sides up and down of plate B are the upper and lower ends flanging setting in the same direction of flanging and same plate, and heat exchange plate A and are changed
The direction of hot plate piece B upper and lower ends flangings is opposite.
4. a kind of gas phase adverse current plate heat exchanger according to claim 2 or 3, it is characterised in that the edges the heat exchange plate A
The left and right ends of gas flow direction, wherein the upper semisection left folding, lower semisection right folding of one end flanging, corresponding other end flanging,
Upper semisection right folding, lower semisection left folding.
5. a kind of gas phase adverse current plate heat exchanger according to claim 2 or 3, it is characterised in that the edges the heat exchange plate B
The left and right ends of gas flow direction, wherein the upper semisection right folding, lower semisection left folding of one end flanging, corresponding other end flanging,
Upper semisection left folding, lower semisection right folding.
6. a kind of gas phase adverse current plate heat exchanger according to claim 3, it is characterised in that the upper end of the heat exchange plate A
With the equal right folding of lower end flanging, the equal left folding of top and bottom flanging of heat exchange plate B.
7. a kind of gas phase adverse current plate heat exchanger according to claim 3, it is characterised in that the heat exchange plate A and heat exchange
The end of all flangings of surrounding of plate B is equipped with the bending edge convenient for split and welding.
8. a kind of gas phase adverse current plate heat exchanger according to claim 1, it is characterised in that in the heat exchanger core body
Thermal current and cold airflow are at countercurrent flow, and thermal current import is located at same level height, hot gas outflux with cold airflow import
It is located at same level height with cold air discharge port.
9. a kind of gas phase adverse current plate heat exchanger according to claim 1, it is characterised in that the upper sealing plate is shoot door,
Lower sealing plate is ash dropping hopper, and two blocks of sealing plates are movably arranged on the upper and lower ends of heat exchanger core body, for sealing and deashing.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810631774.2A CN108571906A (en) | 2018-06-19 | 2018-06-19 | A kind of gas phase adverse current plate heat exchanger |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810631774.2A CN108571906A (en) | 2018-06-19 | 2018-06-19 | A kind of gas phase adverse current plate heat exchanger |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108571906A true CN108571906A (en) | 2018-09-25 |
Family
ID=63573375
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810631774.2A Pending CN108571906A (en) | 2018-06-19 | 2018-06-19 | A kind of gas phase adverse current plate heat exchanger |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN108571906A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109210972A (en) * | 2018-11-02 | 2019-01-15 | 南京普兰特换热设备有限公司 | A kind of plate heat exchanger |
| WO2022021915A1 (en) * | 2020-07-30 | 2022-02-03 | 浙江锦欣节能科技有限公司 | Main heat exchanger of wall-mounted stove |
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| CN204043455U (en) * | 2014-09-05 | 2014-12-24 | 四平市巨元瀚洋板式换热器有限公司 | The board-like airair heat exchanger of a kind of pure adverse current |
| CN104534905A (en) * | 2014-12-24 | 2015-04-22 | 南京宜热纵联节能科技有限公司 | Plate heat exchanger for dust to be removed conveniently |
| CN105043144A (en) * | 2015-06-12 | 2015-11-11 | 西安交通大学 | Double-side etching high-temperature and high-pressure printed circuit board heat exchanger |
| CN106839832A (en) * | 2017-01-23 | 2017-06-13 | 中国科学技术大学 | A kind of bend flow channel heat exchanger in the thermodynamic cycle for supercritical fluid |
| CN208366129U (en) * | 2018-06-19 | 2019-01-11 | 南京宜热纵联节能科技溧阳有限公司 | A kind of gas phase adverse current plate heat exchanger |
-
2018
- 2018-06-19 CN CN201810631774.2A patent/CN108571906A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN204043455U (en) * | 2014-09-05 | 2014-12-24 | 四平市巨元瀚洋板式换热器有限公司 | The board-like airair heat exchanger of a kind of pure adverse current |
| CN104534905A (en) * | 2014-12-24 | 2015-04-22 | 南京宜热纵联节能科技有限公司 | Plate heat exchanger for dust to be removed conveniently |
| CN105043144A (en) * | 2015-06-12 | 2015-11-11 | 西安交通大学 | Double-side etching high-temperature and high-pressure printed circuit board heat exchanger |
| CN106839832A (en) * | 2017-01-23 | 2017-06-13 | 中国科学技术大学 | A kind of bend flow channel heat exchanger in the thermodynamic cycle for supercritical fluid |
| CN208366129U (en) * | 2018-06-19 | 2019-01-11 | 南京宜热纵联节能科技溧阳有限公司 | A kind of gas phase adverse current plate heat exchanger |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109210972A (en) * | 2018-11-02 | 2019-01-15 | 南京普兰特换热设备有限公司 | A kind of plate heat exchanger |
| WO2022021915A1 (en) * | 2020-07-30 | 2022-02-03 | 浙江锦欣节能科技有限公司 | Main heat exchanger of wall-mounted stove |
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| PB01 | Publication | ||
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| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20180925 |
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| RJ01 | Rejection of invention patent application after publication |