CN201463671U - Heat exchanging core for air heat recovery device - Google Patents

Heat exchanging core for air heat recovery device Download PDF

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Publication number
CN201463671U
CN201463671U CN2009201103866U CN200920110386U CN201463671U CN 201463671 U CN201463671 U CN 201463671U CN 2009201103866 U CN2009201103866 U CN 2009201103866U CN 200920110386 U CN200920110386 U CN 200920110386U CN 201463671 U CN201463671 U CN 201463671U
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CN
China
Prior art keywords
heat
heat exchanger
heat exchange
sealing strip
heat exchanging
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Expired - Fee Related
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CN2009201103866U
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Chinese (zh)
Inventor
陈光辉
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BEIJING COGENG NEW WIND ENERGY TECHNOLOGY DEVELOPMENT Co Ltd
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BEIJING COGENG NEW WIND ENERGY TECHNOLOGY DEVELOPMENT Co Ltd
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Priority to CN2009201103866U priority Critical patent/CN201463671U/en
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Abstract

The utility model discloses a heat exchanging core for an air heat recovery device, which comprises a shell and a heat exchanging unit arranged in the shell, wherein the heat exchanging unit comprises a plurality of heat exchanging fins which are overlapped in the shell in parallel, and the heat exchanging fin comprises a heat exchanging region with the convex and concave isosceles trapezoid section, and a sealing edge positioned around the heat exchanging region. With the heat exchanging core, the advantages of large heat exchanging area, high operation efficiency of whole equipment, long service life, high heat recovery efficiency, and good sealing performance between a new air channel and a dirt air pollution channel can be achieved.

Description

A kind of air heat regenerator heat exchange core
Technical field
The utility model relates to the ventilation field, particularly, relates to a kind of air heat regenerator heat exchange core.
Background technology
As far back as 1996, German lung company developed first fresh air ventilator in the world, and formally imports China in 2000, through updating and innovating, has been widely used in the ventilation field at present.
In the prior art, air heat regenerator improves equipment as fresh air ventilator, can reclaim the energy that is run off in indoor dirty wind and the outdoor new wind exchange process better when fresh air ventilator is worked.Particularly, when fresh air ventilator is worked, indoor dirty wind is discharged to outdoor, simultaneously outdoor new wind is delivered to indoorly, carry out equivalent displacement between the two.
With regard to northern area, in summer, indoor temperature generally is lower than outdoor temperature; In the winter time, indoor temperature is higher than outdoor temperature.When indoor dirty wind and outdoor new wind being carried out the equivalent displacement, suppose not establish the energy recycle device of similar air heat regenerator, so, summer, indoor cold will be lost with the displacement of air, winter, therefore indoor heat also can run off, and had so just increased the load of refrigeration and heating equipment greatly, thereby had caused very big waste, as waste of electric energy, the shortening of service life of equipment etc.
In order to slow down above-mentioned waste of electric energy and the situations such as shortening of equipment operating period, so in fresh air ventilator, set up air heat regenerator; Wherein, energy losing issue when air heat regenerator can correspondingly solve above-mentioned indoor and outdoor ventilation, during fresh air ventilator work, indoor dirty wind and outdoor new wind pass through air heat regenerator simultaneously, heat-conduction effect by special substance, the energy that runs off is sent into indoor by outdoor new wind, just can be reached energy-conservation effect.
In the prior art, the material by the heat exchange core can be divided into air heat regenerator the full heat regenerator made of paper and the sensible heat recover of aluminum.
For above-described air heat regenerator, in realizing process of the present utility model, the inventor finds the sensible heat recover of air heat regenerator of the prior art, especially aluminum, has following defective at least:
(1) in the sensible heat recover of aluminum, the aluminium foil of selecting for use is that thickness is 0.05 millimeter normal aluminium foil, can not stretch, and after being made into a plurality of little airflow passages, the heat exchange area of original aluminium foil is reduced;
(2) in above-mentioned air heat regenerator, the cross section of each little airflow passage is isosceles triangle, and is too narrow, and the circulation to air causes very big resistance even obstruction easily; Simultaneously, can reduce integral device, promptly the running efficiency of the fresh air ventilator of this air heat regenerator is installed, also can shorten the service life of this fresh air ventilator;
(3) gas channel in above-mentioned air heat regenerator inside is smooth shape, and heat recovery efficiency is lower;
(4) in above-mentioned air heat regenerator, between new wind passage and the dirty wind passage, adopt gluing flats to isolate, when inhomogeneous, then be easy to occur the phenomenon that new wind mixes with dirty wind as if the latex of bonding place.
Summary of the invention
The purpose of this utility model is, at the problems referred to above, proposes a kind of air heat regenerator heat exchange core, to realize that heat exchange area is big, the running efficiency height of integral device, long service life, heat recovery efficiency height, and the advantage of the good airproof performance between new wind passage and the dirty wind passage.
For achieving the above object, the technical solution adopted in the utility model is: a kind of air heat regenerator heat exchange core comprises shell, and is installed in the heat exchange unit in the described shell that described heat exchange unit comprises the parallel a plurality of heat exchanger fins that overlay in the described shell; Each heat exchanger fin comprises that cross sectional shape is the heat transfer zone of concavo-convex alternate isosceles trapezoid, and the sealing strip that is positioned at described heat transfer zone periphery.
Further, described heat exchanger fin adopts heat treatment after " O " state stretches and thickness is the rectangle aluminium foil of 0.1-0.12mm, is stamped to form through mould; Wherein: through the zone of described mould punching press is heat transfer zone, is sealing strip without the zone of described mould punching press; Described heat transfer zone comprises that cross sectional shape is a plurality of gas channels of isosceles trapezoid, the concavo-convex alternate setting of described a plurality of gas channels.
Further, in described a plurality of gas channels, in the interior outside of each gas channel, being evenly equipped with diameter is a plurality of little round pool of 1-3mm.
Further, in described a plurality of heat exchanger fins, the gas channel antarafacial of adjacent two heat exchanger fins vertically is provided with.
Further, in described a plurality of heat exchanger fins, the bonding sealing-in of corresponding sealing strip flange seaming of a pair of sealing strip of each heat exchanger fin and an adjacent heat exchanger fin forms new wind passage or dirty wind passage; Another forms dirty wind passage or new wind passage to the bonding sealing-in of corresponding sealing strip flange seaming of sealing strip and another adjacent heat exchanger fin.
The air heat regenerator heat exchange core of each embodiment of the utility model, owing to comprise shell, and be installed in the heat exchange unit in the shell, heat exchange unit comprises the parallel a plurality of heat exchanger fins that overlay in the shell; Heat exchanger fin comprises that cross sectional shape is the heat transfer zone of concavo-convex alternate isosceles trapezoid, and the sealing strip that is positioned at the heat transfer zone periphery; Adopting " O " state stretching after heat treatment and thickness is the aluminium foil of 0.1-0.12mm, through the cross section is that the alternate mould of isosceles trapezoid convex-concave is stamped to form heat exchanger fin up and down, heat exchange area is bigger, the cross section of each gas channel is an isosceles trapezoid, near semicircle, the gas channel broad can reduce gas-flow resistance, be not easy to stop up, help improving the running efficiency of heat regenerator; Here, the internal structure and the heat exchange material of air heat regenerator heat exchange core are improved, air moment is detained and produces eddy flow, the ordinary hot recover in compared to existing technology, organic efficiency is higher; Thereby it is little to overcome in the prior art heat exchange area, and the running efficiency of integral device is low, service life short, and heat recovery efficiency is low, and the defective of the sealing difference between new wind passage and the dirty wind passage; To realize that heat exchange area is big, the running efficiency height of integral device, long service life, heat recovery efficiency height, and the advantage of the good airproof performance between new wind passage and the dirty wind passage.
Other features and advantages of the utility model will be set forth in the following description, and, partly from specification, become apparent, perhaps understand by implementing the utility model.The purpose of this utility model and other advantages can realize and obtain by specifically noted structure in the specification of being write, claims and accompanying drawing.
Below by drawings and Examples, the technical solution of the utility model is described in further detail.
Description of drawings
Accompanying drawing is used to provide further understanding of the present utility model, and constitutes the part of specification, is used from explanation the utility model with embodiment one of the present utility model, does not constitute restriction of the present utility model.In the accompanying drawings:
Fig. 1 is the structural representation according to shell in the utility model air heat regenerator heat exchange core;
Fig. 2 is the structural representation according to heat exchange unit in the utility model air heat regenerator heat exchange core;
Fig. 3 is the A-A cutaway view of Fig. 2;
Fig. 4 is the B portion enlarged drawing of Fig. 2.
In conjunction with the accompanying drawings, Reference numeral is as follows among the utility model embodiment:
The 1-top board; 2-first support bar; The 3-base plate; 4-second support bar; 5-the 3rd support bar; 6-first heat exchanger fin; 7-second heat exchanger fin; 8-the 3rd heat exchanger fin; The 9-sealing strip; 10-first gas channel; 11-second gas channel; 12-roundlet hole.
The specific embodiment
Below in conjunction with accompanying drawing preferred embodiment of the present utility model is described, should be appreciated that preferred embodiment described herein only is used for description and interpretation the utility model, and be not used in qualification the utility model.
According to the utility model embodiment, provide a kind of air heat regenerator heat exchange core.As Fig. 1-shown in Figure 4, present embodiment comprises shell and heat exchange unit, and heat exchange unit is installed in the shell; Wherein, heat exchange unit comprises the parallel a plurality of heat exchanger fins that overlay in the shell; Each heat exchanger fin comprises heat transfer zone and sealing strip, and the cross sectional shape of heat transfer zone is concavo-convex alternate isosceles trapezoid, and sealing strip is positioned at the heat transfer zone periphery.
In Fig. 1, shell comprises top board 1 and the base plate 3 that be arranged in parallel, and is vertically connected on first support bar 2, second support bar 4, the 3rd support bar 5 and the 4th support bar between the corresponding angles of top board 1 and base plate 3; A plurality of heat exchanger fins are with first support bar 2, second support bar 4, the 3rd support bar 5 and the 4th support bar is vertical is provided with.
In the present embodiment, can adopt heat treatment, be stamped to form above-mentioned heat exchanger fin through mould after " O " state stretches and thickness is the rectangle aluminium foil of 0.1-0.12mm; Wherein, on this rectangle aluminium foil, be heat transfer zone through the zone of mould punching press, be sealing strip without the zone of mould punching press; In heat transfer zone, comprise that cross sectional shape is a plurality of gas channels of isosceles trapezoid, the concavo-convex alternate setting of a plurality of gas channels.Here, mould is divided into two up and down, and through after the long-time polishing of meticulous grinding machine, forms the cross section on the surface and be a plurality of grooves of concavo-convex alternate isosceles trapezoid, the trapezoidal semicircle that approaches of these isosceles.
The air heat regenerator heat exchange core of present embodiment adopts through heat treatment and " O " state and is drawn into the aluminium foil that thickness is 0.1-0.12mm, through above-mentioned mould punching press, the surface of former aluminium foil is stretched significantly, and the surface area of gained heat exchanger fin and heat exchange area are all increased; In addition, the cross sectional shape of each gas channel is an isosceles trapezoid, is similar to semicircle, and the gas channel broad helps the deflate gas-flow resistance, is not easy to stop up, and helps improving the running efficiency of heat regenerator.
Further, in the present embodiment, in above-mentioned a plurality of gas channels, in the interior outside of each gas channel, being evenly equipped with diameter is a plurality of little round pool of 1-3mm, help further increasing the heat exchange area of heat exchanger fin, and when making the too small round pool of air communication, form little eddy flow, cause the moment of air to be detained, more effectively to reclaim airborne cold or heat, help improving heat recovery efficiency.Here, the steel ball that thousands of diameters are 1-3mm can be on the groove of above-mentioned mould, be bumped into, like this,, a plurality of little round pools can be on the said flow passage, formed through the extruding of mould up and down.In Fig. 3 and Fig. 4, it is the convex gas channel that little round pool is labeled as 12, the first gas channels 10, and second gas channel 11 is the spill gas channel, first gas channel 10 and the 11 adjacent settings of second gas channel.
In the above-described embodiments, a plurality of heat exchanger fins are parallel when overlaying in the shell, the gas channel antarafacial of adjacent two heat exchanger fins vertically is provided with, for example, in Fig. 2, first heat exchanger fin 6, second heat exchanger fin 7 and the 3rd heat exchanger fin 8 orders stack, wherein, the vertical setting of gas channel antarafacial of the gas channel of first heat exchanger fin 6 and second heat exchanger fin 7, in like manner, the vertical setting of gas channel antarafacial of the gas channel of second heat exchanger fin 7 and the 3rd heat exchanger fin 8.The bonding sealing-in of corresponding sealing strip flange seaming of a pair of sealing strip of each heat exchanger fin and an adjacent heat exchanger fin forms new wind passage or dirty wind passage; Another forms dirty wind passage or new wind passage to the bonding sealing-in of corresponding sealing strip flange seaming of sealing strip and another adjacent heat exchanger fin; For example, in Fig. 2, two sealing strip flange up and down of first heat exchanger fin 6 are with the sealing-in of two sealing strip seamings up and down of second heat exchanger fin 7; Two sealing strip flange about second heat exchanger fin 7 are with two sealing strip seamings sealing-in about the 3rd heat exchanger fin 8.Here, can adopt the aluminium foil adhesive gum special when bonding, be the adhesive glue of BA163 as model; Under any condition, the phenomenon that new wind passage mixes with dirty wind passage can not appear.
In sum, the air heat regenerator heat exchange core of each embodiment of the utility model comprises shell, and is installed in the heat exchange unit in the shell, and heat exchange unit comprises the parallel a plurality of heat exchanger fins that overlay in the shell; Heat exchanger fin comprises that cross sectional shape is the heat transfer zone of concavo-convex alternate isosceles trapezoid, and the sealing strip that is positioned at the heat transfer zone periphery; Wherein, it is the aluminium foil of 0.1-0.12mm that heat exchanger fin adopts " O " state stretching after heat treatment and thickness, helps increasing heat exchange area; This aluminium foil is that the alternate mould of isosceles trapezoid convex-concave is stamped to form heat exchanger fin up and down through the cross section, and the cross section of each gas channel is an isosceles trapezoid, near semicircle, the gas channel broad, help reducing gas-flow resistance, be not easy to stop up, help improving the running efficiency of heat regenerator; In the interior outside of the gas channel of heat exchanger fin, use steel column to be pressed with a plurality of little round pool of diameter as 1-3mm, can further increase heat exchange area, form micro cyclone during the too small round pool of air communication, cause the moment of air to be detained, help improving heat recovery efficiency; Between new wind passage and dirty wind passage, adopt the sealing of flange seaming bonding mode, the phenomenon that new wind mixes with dirty wind can not appear under any condition; Thereby it is little to overcome in the prior art heat exchange area, and the running efficiency of integral device is low, service life short, and heat recovery efficiency is low, and the defective of the sealing difference between new wind passage and the dirty wind passage; To realize that heat exchange area is big, the running efficiency height of integral device, long service life, heat recovery efficiency height, and the advantage of the good airproof performance between new wind passage and the dirty wind passage.
It should be noted that at last: the above only is preferred embodiment of the present utility model, be not limited to the utility model, although the utility model is had been described in detail with reference to previous embodiment, for a person skilled in the art, it still can be made amendment to the technical scheme that aforementioned each embodiment put down in writing, and perhaps part technical characterictic wherein is equal to replacement.All within spirit of the present utility model and principle, any modification of being done, be equal to replacement, improvement etc., all should be included within the protection domain of the present utility model.

Claims (5)

1. an air heat regenerator heat exchange core is characterized in that, comprises shell, and is installed in the heat exchange unit in the described shell, and described heat exchange unit comprises the parallel a plurality of heat exchanger fins that overlay in the described shell; Each heat exchanger fin comprises that cross sectional shape is the heat transfer zone of concavo-convex alternate isosceles trapezoid, and the sealing strip that is positioned at described heat transfer zone periphery.
2. air heat regenerator heat exchange core according to claim 1 is characterized in that, described heat exchanger fin adopts heat treatment after " O " state stretches and thickness is the rectangle aluminium foil of 0.1-0.12mm, is stamped to form through mould; Wherein: through the zone of described mould punching press is heat transfer zone, is sealing strip without the zone of described mould punching press;
Described heat transfer zone comprises that cross sectional shape is a plurality of gas channels of isosceles trapezoid, the concavo-convex alternate setting of described a plurality of gas channels.
3. air heat regenerator heat exchange core according to claim 1 and 2 is characterized in that, in described a plurality of gas channels, in the interior outside of each gas channel, being evenly equipped with diameter is a plurality of little round pool of 1-3mm.
4. air heat regenerator heat exchange core according to claim 3 is characterized in that, in described a plurality of heat exchanger fins, the gas channel antarafacial of adjacent two heat exchanger fins vertically is provided with.
5. air heat regenerator heat exchange core according to claim 4, it is characterized in that, in described a plurality of heat exchanger fins, the bonding sealing-in of corresponding sealing strip flange seaming of a pair of sealing strip of each heat exchanger fin and an adjacent heat exchanger fin forms new wind passage or dirty wind passage; Another forms dirty wind passage or new wind passage to the bonding sealing-in of corresponding sealing strip flange seaming of sealing strip and another adjacent heat exchanger fin.
CN2009201103866U 2009-07-29 2009-07-29 Heat exchanging core for air heat recovery device Expired - Fee Related CN201463671U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2009201103866U CN201463671U (en) 2009-07-29 2009-07-29 Heat exchanging core for air heat recovery device

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Application Number Priority Date Filing Date Title
CN2009201103866U CN201463671U (en) 2009-07-29 2009-07-29 Heat exchanging core for air heat recovery device

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CN201463671U true CN201463671U (en) 2010-05-12

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109297295A (en) * 2018-09-03 2019-02-01 深圳市华星光电技术有限公司 Heat exchanger and roasting plant
CN111988971A (en) * 2020-09-18 2020-11-24 珠海银河温控技术有限公司 Heat exchange unit and heat exchange module

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109297295A (en) * 2018-09-03 2019-02-01 深圳市华星光电技术有限公司 Heat exchanger and roasting plant
CN111988971A (en) * 2020-09-18 2020-11-24 珠海银河温控技术有限公司 Heat exchange unit and heat exchange module

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GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20100512

Termination date: 20170729