CN104613745B - Heat exchange device with mixing bins - Google Patents
Heat exchange device with mixing bins Download PDFInfo
- Publication number
- CN104613745B CN104613745B CN201510060438.3A CN201510060438A CN104613745B CN 104613745 B CN104613745 B CN 104613745B CN 201510060438 A CN201510060438 A CN 201510060438A CN 104613745 B CN104613745 B CN 104613745B
- Authority
- CN
- China
- Prior art keywords
- heat
- heat exchanger
- exchange device
- radiating tube
- mixing bunker
- 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.)
- Expired - Fee Related
Links
- 238000002156 mixing Methods 0.000 title claims abstract description 28
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 18
- 239000002912 waste gas Substances 0.000 claims abstract description 7
- 241000273930 Brevoortia tyrannus Species 0.000 claims description 22
- 239000007789 gas Substances 0.000 claims description 8
- 239000004411 aluminium Substances 0.000 claims description 3
- 229910052782 aluminium Inorganic materials 0.000 claims description 3
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminum Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 3
- RYGMFSIKBFXOCR-UHFFFAOYSA-N copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 3
- 239000010949 copper Substances 0.000 claims description 3
- 229910052802 copper Inorganic materials 0.000 claims description 3
- 238000004519 manufacturing process Methods 0.000 abstract description 5
- 229920002456 HOTAIR Polymers 0.000 abstract description 4
- 238000010438 heat treatment Methods 0.000 abstract description 4
- 238000001035 drying Methods 0.000 abstract description 3
- 238000005265 energy consumption Methods 0.000 abstract description 3
- 230000017525 heat dissipation Effects 0.000 abstract 5
- 230000000875 corresponding Effects 0.000 abstract 2
- 238000010304 firing Methods 0.000 description 3
- 230000001131 transforming Effects 0.000 description 3
- 210000000214 Mouth Anatomy 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000000686 essence Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000006011 modification reaction Methods 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
Abstract
The invention belongs to the field of heating equipment for providing dry and hot air for heating and drying of agricultural products and particularly relates to a heat exchange device with mixing bins. The device comprises a steam inlet, a condensate water and waste gas outlet and heat exchangers, each heat exchanger comprises a hot water steam pipe and a plurality of heat dissipation pipes connected with the corresponding hot water steam pipe, heat dissipation pipe fins are arranged on the outsides of the heat dissipation pipes, one end of each heat exchanger is provided with a heat exchanger air inlet, the other end of each heat exchanger is provided with a heat exchanger air outlet, and the heat exchangers are horizontally connected in parallel; the heat exchanger air outlets of the heat exchangers are mutually communicated and then put together to form a pipeline with a narrowing section; each mixing bin is arranged between the corresponding adjacent heat dissipation pipes, and the mixing bins can allow air which passes through the heat dissipation pipes and has different temperatures to be evenly mixed in the mixing bins in a vertical convection mode. The heat exchange device with the mixing bins is high in heat exchange efficiency, energy consumption is reduced, and production efficiency is improved.
Description
Technical field
The invention belongs to agricultural product are heated, are dried the firing equipment field providing heated dry air and in particular to one kind is provided with
The heat-exchange device of mixing bunker.
Background technology
Heating in agricultural production, be dehydrated, drying is conventional technique, needs frequently dry using being provided that in technical process
The firing equipment of hot-air.The heat exchanger of existing firing equipment has 16 groups of radiating tubes, and in a heat exchanger in a row longitudinally
Arrange one by one, as shown in Figure 1.Radiating tube in heat exchanger and radiating fin arrange more tight, air in interchange channel
Relatively short by the time of interchange channel, cause rate of heat exchange not high, and it is all from top to bottom that water steams in the radiating tube of place
Co-flow, the temperature potential of radiating tube must form the low situation of relative superiority or inferiority, result in the interchange channel upper, middle and lower layer of air temperature difference
Excessive, it is unfavorable for the abundant exchange of heat.Therefore also there is combustion heat exchange not abundant, expend excessive fuel, relatively costly etc.
Shortcoming.It is thus desirable to by transforming to existing heat exchanger, improve heat exchanger effectiveness, to meet the needs of production.
Content of the invention
The present invention is directed to the deficiencies in the prior art, provides a kind of higher heat exchange being provided with mixing bunker of heat exchanger effectiveness
Device, reducing energy consumption, improve production efficiency.
The technical scheme is that and be achieved in that: a kind of heat-exchange device being provided with mixing bunker include vapour inlet,
Condensed water and waste gas outlet and heat exchanger, described heat exchanger includes hot water and steam pipe and many be connected with hot water and steam pipe
Radiating tube, has radiating tube fin outside this radiating tube, described heat exchanger one end is provided with heat exchanger air inlet, and the other end is provided with
Heat exchanger gas outlet it is characterised in that: described heat exchanger is multiple levels heat exchanger in parallel;The plurality of heat exchange
The pipeline narrowing for a section is closed up in the heat exchanger gas outlet of device after being interconnected;Set respectively between described adjacent heat radiation pipe
There is mixing bunker, described mixing bunker can make the air of different temperatures after radiating tube in its internal even conjunction of convection current up and down.
Preferably, the quantity of described heat exchanger at least two.
Preferably, the quantity of described radiating tube at least 8.
Preferably, described radiating tube and radiating tube fin are made up of aluminium or copper product.
The present invention solves defect present in background technology, has the advantages that
The heat-exchange device being provided with mixing bunker that the present invention provides, is formed by arranging multiple levels heat exchanger in parallel
One complete heat-exchange device, increased air flow area, in the case of identical amount, reduces the flowing speed of air
Degree, extends the time of contact of air and radiating tube, improves heat exchanger effectiveness, reduce energy consumption.Between two-stage radiation pipe
Add a mixing bunker, make the even conjunction of cross-ventilation of upper and lower different temperatures in mixing bunker, so that heat is sufficiently swapped, heat is handed over
Change rate lifting, improve production efficiency.
Brief description
Fig. 1 is the structural representation of heat-exchange device before transformation;
Fig. 2 be transformation after be provided with mixing bunker heat-exchange device structural representation;
Fig. 3 is the transverse cross sectional face schematic diagram of Fig. 2;
In figure: 1- pressure hot water steam pipe, 2- radiating tube fin, 3- mixing bunker, 4- heat exchanger air inlet, 5- heat exchange
Device gas outlet, 6- vapour inlet, 7- condensed water and waste gas outlet, 8- radiating tube.
Specific embodiment
Below in conjunction with the accompanying drawing in the embodiment of the present invention, the technical scheme in the embodiment of the present invention is carried out clear, complete
Site preparation description is it is clear that described embodiment is only a part of embodiment of the present invention, rather than whole embodiments.It is based on
Embodiment in the present invention, it is every other that those of ordinary skill in the art are obtained under the premise of not making creative work
Embodiment, broadly falls into the scope of protection of the invention.
A kind of heat-exchange device being provided with mixing bunker as shown in Figures 2 and 3, including vapour inlet 6, condensed water and waste gas
Outlet 7 and heat exchanger, heat exchanger includes hot water and steam pipe 1 and many radiating tubes 8 being connected with hot water and steam pipe 1, and this dissipates
There is radiating tube fin 2, heat exchanger one end is provided with heat exchanger air inlet 4, and the other end is provided with heat exchanger and gives vent to anger outside heat pipe 8
Mouth 5, heat exchanger is two levels heat exchanger in parallel;After the heat exchanger gas outlet 5 of two heat exchangers is interconnected
Close up the pipeline for a truncated tapered, be so conducive to the quick discharge of hot-air.Set respectively between adjacent heat radiation pipe 8
There is mixing bunker 3, mixing bunker 3 can make by the air of different temperatures after radiating tube 8 in its internal even conjunction of convection current up and down.Radiating tube 8
Quantity at least 8.Radiating tube 8 and radiating tube fin 2 are made up of aluminium or copper product.
The course of work of the present invention is: produces pressure steam with pressure boiler, by pipeline, steam is passed through pressure
Radiating tube 8 and air that hot water and steam pipe 1 is transported in heat exchanger carry out thermal energy exchange, and produce hot-air from heat exchanger
The pipe outlet of gas outlet 5 is discharged, for the drying in producing, heating.This is provided with the heat-exchange device of mixing bunker and is provided with two
Individual level the heat exchanger connecting, are interconnected two heat converter air-out mouths 5, finally will be converged by the hot blast of heat exchanger
Integrated one, so constitute the heat exchanger of two hot switching paths, be equivalent to increase heat exchanger hollow air-flow
Dynamic section.In the case of equal flow, reduce flow velocity, make the time lengthening of air and heat sink contact, heat exchange is more
Plus fully.Air themperature for making air duct upper, middle and lower layer equalizes, and is respectively equipped with mixing bunker in two adjacent groups radiating tube 8
3, make thermal current carry out heat exchange inside it, so that the gas flow temperature of levels is equalized, improve rate of heat exchange.Finally will radiate
The condensed water that pipe produces and waste gas are sent boiler back to by condensed water and waste gas outlet 7 after bottom is collected and are carried out energy recovery profit
With.
The foregoing is only presently preferred embodiments of the present invention, not in order to limit the present invention, all essences in the present invention
Within god and principle, any modification, equivalent substitution and improvement made etc., should be included within the scope of the present invention.
Claims (4)
1. a kind of heat-exchange device being provided with mixing bunker, including vapour inlet (6), condensed water and waste gas outlet (7) and heat exchange
Device, described heat exchanger includes hot water and steam pipe (1) and many radiating tubes (8) being connected with hot water and steam pipe (1), this radiating tube
(8) outside have radiating tube fin (2), and described heat exchanger one end is provided with heat exchanger air inlet (4), and the other end is provided with heat exchange
Device gas outlet (5) it is characterised in that: described heat exchanger is that multiple levels are in parallel;The heat exchange of the plurality of heat exchanger
The pipeline narrowing for a section is closed up, after being interconnected, in device gas outlet (5);Adjacent heat radiation pipe is respectively equipped with mixing bunker between (8)
(3), described mixing bunker (3) can make by the air of radiating tube (8) different temperatures afterwards in its internal even conjunction of convection current up and down.
2. the heat-exchange device being provided with mixing bunker according to claim 1 it is characterised in that: the number of described heat exchanger
Amount at least two.
3. the heat-exchange device being provided with mixing bunker according to claim 1 and 2 it is characterised in that: described radiating tube (8)
Quantity at least 8.
4. the heat-exchange device being provided with mixing bunker according to claim 3 it is characterised in that: described radiating tube (8) and
Radiating tube fin (2) is made up of aluminium or copper product.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201510060438.3A CN104613745B (en) | 2015-02-05 | 2015-02-05 | Heat exchange device with mixing bins |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201510060438.3A CN104613745B (en) | 2015-02-05 | 2015-02-05 | Heat exchange device with mixing bins |
Publications (2)
Publication Number | Publication Date |
---|---|
CN104613745A CN104613745A (en) | 2015-05-13 |
CN104613745B true CN104613745B (en) | 2017-01-25 |
Family
ID=53148307
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201510060438.3A Expired - Fee Related CN104613745B (en) | 2015-02-05 | 2015-02-05 | Heat exchange device with mixing bins |
Country Status (1)
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CN (1) | CN104613745B (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
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CN105953615B (en) * | 2016-05-11 | 2019-07-16 | 中国能源建设集团广东省电力设计研究院有限公司 | Binary channels heat-exchange system and its air temperature modification method |
Family Cites Families (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB9515492D0 (en) * | 1995-07-28 | 1995-09-27 | Aitken William H | Apparatus for combined heat and mass transfer |
JPH1047883A (en) * | 1996-07-30 | 1998-02-20 | Mitsubishi Materials Corp | Heat exchanger |
CN2419562Y (en) * | 1999-06-30 | 2001-02-14 | 罗友义 | Steam-water heat exchanging pipeline for heating and hot water supplying system |
CN201069329Y (en) * | 2007-07-26 | 2008-06-04 | 鲁德祥 | Removable hot pipe fin heat exchanger |
JP2009097733A (en) * | 2007-10-12 | 2009-05-07 | Denso Corp | Adsorption heat exchanger and its manufacturing method |
CN204461008U (en) * | 2015-02-05 | 2015-07-08 | 裴建华 | A kind of heat-exchange device being provided with mixing bunker |
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2015
- 2015-02-05 CN CN201510060438.3A patent/CN104613745B/en not_active Expired - Fee Related
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CN104613745A (en) | 2015-05-13 |
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PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C41 | Transfer of patent application or patent right or utility model | ||
TA01 | Transfer of patent application right |
Effective date of registration: 20161124 Address after: 678108 Baoshan City, Yunnan province Changning County Mengtong town Mengtong Street Applicant after: Changning Hualong agricultural development limited liability company Address before: 678108 Baoshan City, Yunnan province Changning County Mengtong town Mengtong Village Applicant before: Pei Jianhua |
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C14 | Grant of patent or utility model | ||
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: 20170125 Termination date: 20180205 |