CN204988008U - Thick gaseous medium heat transfer device is glued to tubular non - - Google Patents
Thick gaseous medium heat transfer device is glued to tubular non - Download PDFInfo
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- CN204988008U CN204988008U CN201520562477.9U CN201520562477U CN204988008U CN 204988008 U CN204988008 U CN 204988008U CN 201520562477 U CN201520562477 U CN 201520562477U CN 204988008 U CN204988008 U CN 204988008U
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- 230000005855 radiation Effects 0.000 description 3
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- 238000004519 manufacturing process Methods 0.000 description 2
- 230000003287 optical effect Effects 0.000 description 2
- 229910001220 stainless steel Inorganic materials 0.000 description 2
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Abstract
本实用新型公开了一种管式非粘稠气态介质换热装置，包括两端设置法兰盘的管道本体，所述管道本体中部设置导温柱，所述导温柱与管道本体之间设置导温板，所述导温板折叠形成若干换热腔室；本实用新型采用的导温板通过折叠形成若干换热腔室或蜂窝状换热腔室，增大了非粘稠气态介质的导热面，同时在导温板上设置翅片，使得热交换更快更均匀，从而实现长度不增加的情况下换热面积提高10倍以上，在导温柱前部设置的圆锥分流器，能够将进入的气流均匀的分散至换热腔室内，实现均匀换热的功能，根据温度和风量，多根并联或串联的方式进行组合换热；本装置结构简单操作简便，值得应用与推广。
The utility model discloses a tube-type non-viscous gaseous medium heat exchange device, which comprises a pipeline body with flanges arranged at both ends, a temperature-conducting column arranged in the middle of the pipeline body, and a heat-conducting column arranged between the temperature-conducting column and the pipeline body. The temperature conducting plate is folded to form several heat exchange chambers; the temperature conducting plate adopted by the utility model is folded to form several heat exchange chambers or honeycomb heat exchange chambers, which increases the capacity of the non-viscous gaseous medium. At the same time, fins are set on the heat conduction plate to make the heat exchange faster and more uniform, so that the heat exchange area can be increased by more than 10 times without increasing the length. The conical shunt installed in front of the heat conduction column can Disperse the incoming airflow evenly into the heat exchange chamber to realize the function of uniform heat exchange. According to the temperature and air volume, multiple parallel or series connections are used for combined heat exchange. This device is simple in structure and easy to operate, and is worthy of application and promotion.
Description
Technical field
The utility model belongs to non-thickness media for heat exchange equipment technical field, is specifically related to a kind of tubular type non-thickness gaseous medium heat-exchanger rig.
Background technology
In industrial processes, for transmission and the heat exchange of non-thickness gaseous medium, perplex the technical barrier of enterprise often, if be only designed to inside or outer setting heat exchange thermal source, heat trnasfer is carried out by self or outer wall, and the non-viscous medium of inside is often due to little with heat exchanging body contact area, make variations in temperature uneven, the medium temperature causing afterbody to flow out is extremely uneven, thus the quality making operation afterwards produce reduces, one " cellular heat transfer unit (HTU) is disclosed in CN204064056U, comprise tubular shell and central tube, described central tube is arranged in described tubular shell, seal cavity is formed between the inwall of described tubular shell and the outer wall of central tube, be provided with polylith demarcation strip between the inwall of described tubular shell and the outer wall of central tube, described sealed chamber is divided into multiple chamber being parallel to described central tube by described demarcation strip, working medium is filled with in described chamber, on the inwall of described chamber, at least one face is disposed with some micro-fins be made up of Heat Conduction Material, form the capillary slot of array between adjacent described micro-fin, described capillary slot is arranged in the mode being conducive to reducing the resistance of described working medium suffered by the indoor moveable of described chamber.But enter that air flow method is wherein unbalanced makes heat exchange uneven; A kind of hot-blast stove internally finned tube is disclosed in CN203177708U, there is the hollow profile of strip uniform wall thickness, the hollow profile of strip uniform wall thickness has cross section to be the pipe of annulus and cross section to be the rectangular tube of straight-flanked ring, the hollow profile of strip uniform wall thickness has inner tubal wall and outer tube wall, at the uniform fin being connected with hollow profile length direction along strip uniform wall thickness of the inner tubal wall of the hollow profile of strip uniform wall thickness, fin is the strip thin plate that width is identical, and the inner tubal wall face of the hollow profile of strip thin plate and strip uniform wall thickness is perpendicular.During use, internally finned tube can as the pipe of the prior art heat-exchange device that make coal-fired hot-blast stove the same as rectangular tube; Though its can evenly by air-flow due to the little wingization that makes of its area of dissipation smaller, needs are caused to design very long lines, larger wing ratio could be realized, and there is no heat-transfer surface due to center, the phenomenon that heat exchange is uneven may be caused, therefore need a kind ofly can either improve the tubular type non-thickness gaseous medium heat-exchanger rig that heat exchange efficiency can reduce again equipment volume.
Utility model content
Technical problem to be solved in the utility model be for viscous medium non-in prior art in heat exchange or transmitting procedure, because wing is than little bulky, heat exchange efficiency is not high and media for heat exchange the is uneven phenomenon that cause, and provide a kind ofly can be heated evenly, augmented flow can as the tubular type of Cemented filling non-thickness gaseous medium heat-exchanger rig.
Technical scheme adopted to achieve these goals is: a kind of tubular type non-thickness gaseous medium heat-exchanger rig, comprise the pipeline body that two ends arrange ring flange and arranged outside thermal source, arrange in the middle part of described pipeline body and lead Wen Zhu, arrange heat-conductive plate between the described Wen Zhuyu of leading pipeline body, described heat-conductive plate is folded to form some heat exchange chambers.
Describedly lead warm column end circular cone current divider is set.
Described heat-conductive plate is folded to form petal-shaped heat exchange chamber.
The described Wen Zhuwei of leading inlet end arranges the blind pipe of opening, and the opening part of described blind pipe arranges circular cone current divider.
Described heat-conductive plate surface arranges fin.
Described heat-conductive plate is folded to form cellular heat exchange chamber.
The utility model adopts two ends to arrange the pipeline body of ring flange and arranged outside thermal source, can be convenient to be connected in series or be connected side by side or Hybrid connections, increase length with this or increase instantaneous delivery, at pipeline body outer setting thermal source, the thermal source adopted can the heat exchange form of one or more independent assortments of electricity, naked light, steam and conduction oil, preferred employing Electromagnetic Heating is that thermal source carries out heat exchange, embodies broad applicability of the present utility model; The heat-conductive plate adopted, by being folded to form some petal-shaped heat exchange chambers or cellular heat exchange chamber, increasing the heat-transfer surface of non-thickness gaseous medium, increases the resistance of gaseous medium, extend the time of staying of gaseous medium, thus improve heat exchange efficiency; Make to lead warm post surface also form temperature difference face owing to possessing good thermal conductivity, thus effectively prevent heat exchange blind area, ensure that the quality of heat exchange; Heat-conductive plate arranges fin, further increases heat exchange area and resistance, make heat exchange more fast evenly, also just can realize good heat transfer effect with less tube side; Lead warm post and preferably select stainless steel, thus avoid fin or heat-conductive plate at high temperature difference or repeatedly get rusty under heating coming off and softening transform, the phenomenon causing heat exchange efficiency to decline and be mixed into the drawback that next procedure affects GAS QUALITY; Arrange in the middle of pipeline body and lead Wen Zhu, control optimal heat radiation length, be blind pipe because it is designed to end, not only alleviate overall quality but also ensure that maximal ventilatory volume while not reducing flow, thus make this device when equal length, heat exchange area is more than 10 times of equal optical tube length, reduces the volume of heat exchanger.Can thermal source and temperature sensor be set simultaneously within it, be used for compensating thermal source, control heat transfer effect; Circular cone current divider is set leading warm column end, make the uniform stream entered to be dispersed to each heat exchanging chamber indoor, realize the function of uniform heat exchange, simultaneously can according to purposes need take off circular cone current divider; Heat exchanger tube can be set on circular cone current divider, be communicated with heat transferring medium in guide Wen Zhu, enhance the versatility of this device, increase the scope of application of this device.
The utility model arranges heat-conductive plate and leads the mode of Wen Zhu in pipeline body, achieves the uniform heat exchange function to non-thickness gaseous medium, and the dispersed non-viscous medium of circular cone current divider of inlet end setting simultaneously, ensure that the effect of heat exchange; The ring flange arranged at pipeline body two ends can strengthen the versatility of this device, under equal resources supplIes, played its practical value to greatest extent, is worth application and promotes.
Accompanying drawing explanation
Below in conjunction with accompanying drawing, the utility model is described further:
Fig. 1 is the utility model Facad structure schematic diagram;
Fig. 2 is that side structure schematic diagram is looked on a left side for the utility model embodiment one;
Fig. 3 is the partial structurtes schematic diagram that the utility model embodiment one leads warm column end;
Fig. 4 is the partial structurtes schematic diagram of the utility model heat-conductive plate surface fin;
Fig. 5 is that side structure schematic diagram is looked on a left side for the utility model embodiment two;
Fig. 6 is the partial structurtes schematic diagram that the utility model embodiment three leads warm column end.
Detailed description of the invention
As Figure 1-4: embodiment one: a kind of tubular type non-thickness gaseous medium heat-exchanger rig, comprise the pipeline body 1 that two ends arrange ring flange 2 and arranged outside thermal source 3, arrange in the middle part of described pipeline body 1 and lead warm post 5, described leading between warm post 5 and pipeline body 1 arranges heat-conductive plate 4, and described heat-conductive plate 4 is folded to form some heat exchange chambers.
Describedly lead warm post 5 end circular cone current divider 6 is set.
Described heat-conductive plate 4 surface arranges fin 5.
Described heat-conductive plate 5 is folded to form petal-shaped heat exchange chamber.
Describedly lead warm post 5 for inlet end and arrange the blind pipe of opening, the opening part of described blind pipe arranges circular cone current divider.
Embodiment one is optimal technical scheme of the present utility model, due to the heat-conductive plate, the pipeline body that adopt and lead Wen Zhu and constitute an airtight heat exchange subenvironment, fin is set on heat-conductive plate simultaneously, increase the contact area of medium and heat transferring medium, and leaving gap between heat-conductive plate, heat radiation can be conducted fast, there is not limitation in the thermal source of employing, be suitable for existing various thermal source or its independent assortment, in gas, effect is all good.
As shown in Fig. 1,3-5; Embodiment two: the difference of itself and embodiment one is: described heat-conductive plate is folded to form some cellular 8 heat exchange chambers.That it changes the shape of heat-conductive plate, and fin is set on its surface, further increase the contact surface of heat exchange.
As Fig. 1,2, shown in 4-6; Embodiment three: the difference of itself and embodiment one or two is: described circular cone current divider 6 arranges wireway 7.It can be communicated with recuperated gas leading in warm post 5 of hollow, heats from inside this device, and be mainly used to as compensation heat exchange, the medium that pipeline is flowed out can be directly qualified, is convenient to following process and uses, and is mainly used in the interim or urgent needs produced.
Embodiment four: the difference of itself and embodiment one or two or three is: described in lead in Wen Zhu heater and temperature sensor be set.Temperature sensor can be connected with outside central controller by it, thus ensures the effect of heat exchange, utilizes and realizes automated production.
Embodiment five: according to the difference of temperature and flow, the mode of serial or parallel connection can be adopted between pipeline body; Parallel connection can increase flow with reduction heat exchanger volume; Series connection can increase stroke, increases heat exchange area, accelerates heat transfer rate.
The utility model adopts two ends to arrange the pipeline body of ring flange and arranged outside thermal source, can be convenient to be connected in series or be connected side by side or Hybrid connections, increase length with this or increase instantaneous delivery, at pipeline body outer setting thermal source, the thermal source adopted can the heat exchange form of one or more independent assortments of electricity, naked light, steam and conduction oil, preferred employing Electromagnetic Heating is that thermal source carries out heat exchange, embodies broad applicability of the present utility model; The heat-conductive plate adopted, by being folded to form some petal-shaped heat exchange chambers or cellular heat exchange chamber, increasing the heat-transfer surface of non-thickness gaseous medium, increases the resistance of gaseous medium, extend the time of staying of gaseous medium, thus improve heat exchange efficiency; Make to lead warm post surface also form temperature difference face owing to possessing good thermal conductivity, thus effectively prevent heat exchange blind area, ensure that the quality of heat exchange; Heat-conductive plate arranges fin, further increases heat exchange area and resistance, make heat exchange more fast evenly, also just can realize good heat transfer effect with less tube side; Lead warm post and preferably select stainless steel, thus avoid fin or heat-conductive plate at high temperature difference or repeatedly get rusty under heating coming off and softening transform, the phenomenon causing heat exchange efficiency to decline and be mixed into the drawback that next procedure affects GAS QUALITY; Arrange in the middle of pipeline body and lead Wen Zhu, control optimal heat radiation length, be blind pipe because it is designed to end, not only alleviate overall quality but also ensure that maximal ventilatory volume while not reducing flow, thus make this device when equal length, heat exchange area is more than 10 times of equal optical tube length, reduces the volume of heat exchanger.Can thermal source and temperature sensor be set simultaneously within it, be used for compensating thermal source, increase heat transfer effect; Circular cone current divider is set leading warm column end, make the uniform stream entered to be dispersed to each heat exchanging chamber indoor, realize the function of uniform heat exchange, simultaneously can according to purposes need take off circular cone current divider; Heat exchanger tube can be set on circular cone current divider, be communicated with heat transferring medium in guide Wen Zhu, enhance the versatility of this device, increase the scope of application of this device.
The utility model arranges heat-conductive plate and leads the mode of Wen Zhu in pipeline body, achieves the uniform heat exchange function to non-thickness gaseous medium, and the dispersed non-viscous medium of circular cone current divider of inlet end setting simultaneously, ensure that the effect of heat exchange; The ring flange arranged at pipeline body two ends can strengthen the versatility of this device, under equal resources supplIes, played its practical value to greatest extent, is worth application and promotes.
What finally illustrate is, above embodiment is only in order to illustrate the technical solution of the utility model and unrestricted, other amendments that those skilled in the art make the technical solution of the utility model or equivalently to replace, only otherwise depart from the spirit and scope of technical solutions of the utility model, all should be encompassed in the middle of right of the present utility model.
Claims (6)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520562477.9U CN204988008U (en) | 2015-07-30 | 2015-07-30 | Thick gaseous medium heat transfer device is glued to tubular non - |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520562477.9U CN204988008U (en) | 2015-07-30 | 2015-07-30 | Thick gaseous medium heat transfer device is glued to tubular non - |
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| Publication Number | Publication Date |
|---|---|
| CN204988008U true CN204988008U (en) | 2016-01-20 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520562477.9U Expired - Fee Related CN204988008U (en) | 2015-07-30 | 2015-07-30 | Thick gaseous medium heat transfer device is glued to tubular non - |
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| CN (1) | CN204988008U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114383046A (en) * | 2021-11-30 | 2022-04-22 | 中国船舶重工集团公司第七一九研究所 | Active pipeline shunting device |
| CN114905230A (en) * | 2022-04-28 | 2022-08-16 | 沈阳东方钛业股份有限公司 | Inner finned tube and processing method thereof |
-
2015
- 2015-07-30 CN CN201520562477.9U patent/CN204988008U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114383046A (en) * | 2021-11-30 | 2022-04-22 | 中国船舶重工集团公司第七一九研究所 | Active pipeline shunting device |
| CN114905230A (en) * | 2022-04-28 | 2022-08-16 | 沈阳东方钛业股份有限公司 | Inner finned tube and processing method thereof |
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| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160120 Termination date: 20200730 |
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| CF01 | Termination of patent right due to non-payment of annual fee |