CN103512412B - U-shaped heat pipe heat exchanging component and the U-shaped heat exchange of heat pipe integrated with electrostatic precipitator - Google Patents
U-shaped heat pipe heat exchanging component and the U-shaped heat exchange of heat pipe integrated with electrostatic precipitator Download PDFInfo
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- CN103512412B CN103512412B CN201310468215.1A CN201310468215A CN103512412B CN 103512412 B CN103512412 B CN 103512412B CN 201310468215 A CN201310468215 A CN 201310468215A CN 103512412 B CN103512412 B CN 103512412B
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- heat pipe
- heat
- working medium
- electrostatic precipitator
- cooling working
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- 238000001816 cooling Methods 0.000 claims abstract description 36
- 238000001704 evaporation Methods 0.000 claims abstract description 18
- 239000012530 fluid Substances 0.000 claims abstract description 15
- 238000009833 condensation Methods 0.000 claims abstract description 13
- 230000005494 condensation Effects 0.000 claims abstract description 11
- 238000007789 sealing Methods 0.000 claims abstract description 8
- 238000005476 soldering Methods 0.000 claims abstract description 8
- 210000001513 Elbow Anatomy 0.000 claims abstract description 7
- 238000005452 bending Methods 0.000 claims abstract description 4
- 238000007493 shaping process Methods 0.000 claims abstract description 4
- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 20
- 239000003546 flue gas Substances 0.000 claims description 19
- 230000001808 coupling Effects 0.000 claims description 7
- 238000010168 coupling process Methods 0.000 claims description 7
- 238000005859 coupling reaction Methods 0.000 claims description 7
- 239000000428 dust Substances 0.000 description 6
- 238000011084 recovery Methods 0.000 description 6
- 239000002918 waste heat Substances 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 210000003284 Horns Anatomy 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- 239000007788 liquid Substances 0.000 description 4
- 238000007664 blowing Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 238000009434 installation Methods 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000005260 corrosion Methods 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000000779 smoke Substances 0.000 description 2
- 238000003466 welding Methods 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 1
- 238000005299 abrasion Methods 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000003044 adaptive Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 239000003517 fume Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
Abstract
U-shaped heat pipe heat exchanging component and the U-shaped heat exchange of heat pipe integrated with electrostatic precipitator, described U-shaped heat pipe heat exchanging component is made up of the shaping elbow of 180 ° of integrally bending and two straight sections extended continuously, described U-shaped heat exchange of heat pipe comprises cooling working medium import header, multiple cooling working medium sleeve pipes of hot working fluid outlet header and connection cooling working medium import header and hot working fluid outlet header, also comprise described multiple U-shaped heat pipe heat exchanging components as heat pipe, cooling working medium import header is inserted on the top of heat pipe, and insert in cooling working medium sleeve pipe, two straight section top soldering and sealing of heat pipe are also inserted in hot working fluid outlet header, the heat pipe part do not inserted in cooling working medium import header is evaporation endothermic section, and the part inserted in cooling working medium import header is condensation heat release section, evaporation endothermic section is arranged on intersegmental part in the import expanding section of electrostatic precipitator, and condensation heat release section is placed in the outer top of import expanding section stage casing flue of electrostatic precipitator, the present invention is applicable to the heat exchanger structure of the Large-Scale Equipment such as thermal power plant, petrochemical industry.
Description
Technical field
The present invention relates to heat exchange of heat pipe technical field, be specifically related to a kind of U-shaped heat pipe heat exchanging component and the U-shaped heat exchange of heat pipe integrated with electrostatic precipitator.
Background technology
The flue gas of boiler and industrial process is when flowing through heating surface, its heat distribution is subject to certain restrictions, cause air preheater export and deduster entrance flue gas temperature higher, in order to make the heat in flue gas be utilized fully, can be realized by the mode arranging waste-heat recovery device in the exhaust gases passes before deduster entrance horn mouth.But in some cases, limitting by space, flue is arranged extremely compact, between air preheater and deduster entrance horn mouth, lack flue straight section arrange waste-heat recovery device; Although be sometimes designed with flue straight section, owing to arranging Benitration reactor above flue straight section, waste-heat recovery device is extremely restricted.In view of this, this patent proposes waste-heat recovery device to be arranged in deduster entrance horn mouth centre position, reducing flue-gas temperature, can effectively reduce dust ratio resistance by absorbing flue gas heat; Simultaneously because the reduction of flue-gas temperature, the volume flow of flue gas also reduces, and the flue gas flow rate simultaneously entering electrostatic precipitator also reduces, and these 2 kinds of effects can significantly improve the efficiency of dust collection of electrostatic precipitator.
If in the middle of smoke inlet section horn mouth waste-heat recovery device being arranged in electrostatic precipitator, generally select water pipe heat exchanger traditionally, water pipe heat exchanger tube also can be designed to H type, spirality, aciculiform fin, the extended surfaces such as plate shape fin or coupling fin, compact conformation, steel consumption is low, but water pipe Tube Sheet of Heat Exchanger is intrafascicular is filled with liquid-working-medium, once because of after the quick-fried leakage of the tube bank thinning rear generation water pipe heat exchanger of abrasion and corrosion, liquid working substance in whole system reveals the phenomenon that deduster flying dust bleeder valve may be caused to block, the unplanned of equipment is caused to force blowing out, even and if quick-fried leakage occurs heat exchange of heat pipe, because the hydraulic fluid quality of hot casing pack is little, and evaporate rapidly by flue gas, the phenomenon that electrostatic precipitator flying dust bleeder valve blocks can not be caused, avoid cause thus unplanned and force blowing out.
Heat pipe is a high efficiency heat transfer element, its diabatic process make use of the evaporation endothermic of latent heat of phase change in thermal conduction study and two processes the strongest of condensation heat release, have high thermal conductivity, good isothermal, cold and hot both sides heat transfer area can change arbitrarily, can the series of advantages such as remotely transferring, temperature-controllable.The operation principle of heat pipe: heat pipe absorbs flue gas heat in evaporation endothermic end, and transfer heat to intraductal working medium, seethe with excitement after working medium heat absorption or evaporate and change steam into, steam rises to condensation release end of heat under the effect of pressure differential, steam condenses into liquid releasing heat at heat pipe release end of heat, the cold fluid of heating release end of heat outside, and the condensate liquid in pipe after steam heat release is back to evaporation endothermic end by Action of Gravity Field, be pumped into vacuum due to inside or be arranged to certain pressure, so working medium is easy to evaporation and boiling, the startup of heat pipe is very fast.
But heat pipe is commonly straight tube structure in Long-Time Service, filling operation liquid in straight tube, needs two ends soldering and sealing; The heat pipe of straight tube structure, intraductal working medium heat transport limitation is fixed, and can not change operating mode by adaptive temperature; The heat pipe of straight tube structure, in cantilever beam state in heat exchanger, rigidity is little, only adapts to Mini-type heat exchanger, and is not suitable for the heat exchanger structure of the Large-Scale Equipment such as thermal power plant, petrochemical industry; Simultaneously, the heat pipe of single straight tubular construction, need two ends soldering and sealing, when heat exchanger tube is intensive, welding job amount is doubled and redoubled, and the production cycle is long, and the Design and manufacture limiting large shape heat exchange of heat pipe is produced, cause directly-heated pipe for a long time can only be applicable to small size heat exchanger, the maximization of heat exchange of heat pipe is extremely restricted.
Summary of the invention
In order to solve above-mentioned prior art Problems existing, the object of the present invention is to provide a kind of U-shaped heat pipe heat exchanging component and the U-shaped heat exchange of heat pipe integrated with electrostatic precipitator, being applicable to the heat exchanger structure of the Large-Scale Equipment such as thermal power plant, petrochemical industry.
For reaching above object, the present invention adopts following technical scheme:
A kind of U-shaped heat pipe heat exchanging component, the elbow of 180 ° shaping by integrally bending and two straight sections extended continuously form.Its extended surface adopts H type, spirality, aciculiform fin, plate shape fin or coupling fin shape.
The U-shaped heat exchange of heat pipe integrated with electrostatic precipitator, comprise cooling working medium import header 4, hot working fluid outlet header 1 and be communicated with multiple cooling working medium sleeve pipes 3 of cooling working medium import header 4 and hot working fluid outlet header 1, also comprise multiple U-shaped heat pipe heat exchanging components described above as heat pipe 2, cooling working medium import header 4 is inserted on the top of described heat pipe 2, and insert in cooling working medium sleeve pipe 3, two straight section 2-2 top soldering and sealing of described heat pipe 2 are also inserted in hot working fluid outlet header 1; Heat pipe 2 part do not inserted in cooling working medium import header 4 is evaporation endothermic section, and the part inserted in cooling working medium import header 4 is condensation heat release section; The import expanding section stage casing flue that described evaporation endothermic section is arranged on electrostatic precipitator is inner, and described condensation heat release section is placed in the outer top of import expanding section stage casing flue of electrostatic precipitator.
The import expanding section stage casing flue that described heat pipe 2 is fixed on electrostatic precipitator by central dividing plate 5 is inner.
180 ° of elbow horizontal layout of described heat pipe 2 are perpendicular to flue gas circulating direction or be parallel to flue gas circulating direction.
H type, spirality, aciculiform fin, plate shape fin or coupling fin shape extended surface is adopted outside the evaporation endothermic section pipe of described heat pipe 2.
Compared to the prior art, tool has the following advantages in the present invention:
1, the present invention adopts U-shaped heat pipe heat exchanging, and U-shaped heat pipe is structurally equal to 2 directly-heated pipes, but system rigidity increases, be applicable to the heat exchanger structure of the Large-Scale Equipment such as thermal power plant, petrochemical industry, and single straight heat pipe is cantilever beam state in heat exchanger, rigidity is little, only adapts to Mini-type heat exchanger.
2, the present invention adopts U-shaped heat pipe heat exchanging, and compared with employing single straight heat pipe, every single u-shaped heat pipe is structurally equal to 2 directly-heated pipes, and only needs soldering and sealing 2 pipe ends, and 2 directly-heated pipes need soldering and sealing 4 pipe ends, and therefore, pipe end seal welding job amount reduces half.
3, the present invention adopt U-shaped heat pipe to be placed in can according to the evaporation heat transfer limit of non-uniform temperature profile adjustment U-shaped heat pipe two straight sections of flow area in the middle of flue, make it to become the U-shaped heat pipe becoming heat transport limitation, than single straight heat pipe, there is security of significantly conducting heat.
4, U-shaped heat exchange of heat pipe of the present invention is arranged on the import expanding section stage casing of electrostatic precipitator, once there is wall thickness reduction because of wearing and tearing or corrosion and booster, the quick-fried leakage of single U-shaped pipe does not affect the long period safe operation of overall heat exchange device, simultaneously, even if there is quick-fried leakage, because the hydraulic fluid quality of U-shaped pipe casing pack is little, and evaporate rapidly by flue gas, can not cause as the quick-fried leakage of water pipe heat exchanger afterwards large water gaging reveal the phenomenon that deduster flying dust bleeder valve may be caused to block, avoid that the equipment caused thus is unplanned forces blowing out.
5, heat exchanger of the present invention is arranged in the import expanding section stage casing of deduster, can make full use of the flue space of electric cleaner import, does not increase extra occupation of land space.
6, the U-shaped heat exchange of heat pipe of the present invention instead of the effect of homogenizing plate in electrostatic precipitator entrance horn mouth, play the effect of current-sharing, expansion heat exchange, chilling cooling, effectively can complete waste heat recovery while reduction exhaust gas temperature, there is the dual-use function of cooling energy-saving and Improvement of dust removal, and long period safe and highly efficient operation can be realized.
7, the present invention adopts modularized design, and compact conformation is convenient to installation and removal.
Accompanying drawing explanation
Fig. 1 is single U-shaped heat pipe heat exchanging component.
Appearance schematic diagram when Fig. 2 is mounting arrangements of the present invention.
Fig. 3 is the structural representation of heat exchanger in the present invention.
Fig. 4 is the structural representation of heat exchanger of the present invention and electrostatic precipitator integrative installation technology.
Detailed description of the invention
Below in conjunction with drawings and the specific embodiments, the present invention is described in further detail.
As shown in Figure 1, a kind of U-shaped heat pipe heat exchanging component of the present invention, the elbow 2-1 and two of 180 ° the straight section 2-2 that continuously extend shaping by integrally bending forms.Its extended surface adopts H type, spirality, aciculiform fin, plate shape fin or coupling fin shape.
As shown in Figures 2 and 3, the U-shaped heat exchange of heat pipe that the present invention is integrated with electrostatic precipitator, comprise cooling working medium import header 4, hot working fluid outlet header 1 and be communicated with multiple cooling working medium sleeve pipes 3 of cooling working medium import header 4 and hot working fluid outlet header 1, also comprise multiple U-shaped heat pipe heat exchanging components described above as heat pipe 2, cooling working medium import header 4 is inserted on the top of described heat pipe 2, and insert in cooling working medium sleeve pipe 3, two straight section 2-2 top soldering and sealing of described heat pipe 2 are also inserted in hot working fluid outlet header 1; Heat pipe 2 part do not inserted in cooling working medium import header 4 is evaporation endothermic section, and the part inserted in cooling working medium import header 4 is condensation heat release section; The import expanding section stage casing flue that described evaporation endothermic section is arranged on electrostatic precipitator is inner, and described condensation heat release section is placed in the outer top of import expanding section stage casing flue of electrostatic precipitator.
As the preferred embodiment of the present invention, described heat pipe 2 is fixed on intersegmental part in the import expanding section of electrostatic precipitator by central dividing plate 5, realizes smoke impervious.
As the preferred embodiment of the present invention, 180 ° of elbow horizontal layout of described heat pipe 2 are perpendicular to flue gas circulating direction or be parallel to flue gas circulating direction.
As the preferred embodiment of the present invention, outside the evaporation endothermic section pipe of described heat pipe 2, adopt H type, spirality, aciculiform fin, plate shape fin or coupling fin shape extended surface.
As shown in Figure 4, be the structural representation of heat exchanger of the present invention and electrostatic precipitator integrative installation technology, the flue space of electric cleaner import can be made full use of, do not increase extra occupation of land space.
Operation principle of the present invention is: the evaporation endothermic section of heat pipe 2 is arranged on the flue inside, import expanding section stage casing of electrostatic precipitator, absorb the heat of flue gas, heat passes to inside heat pipe working media via U-shaped heat pipe wall, after working media absorbs heat, temperature raises and flashes to steam, condensation heat release section is risen under the active force that steam produces at pressure reduction, steam-condensation in U-shaped heat pipe also outwards discharges the latent heat of vaporization, cooling working medium is full of in cooling working medium sleeve pipe 3 outside heat pipe 2, heat convection is carried out on heat pipe 2 top, cooling working medium in heating cooling working medium sleeve pipe 3, Action of Gravity Field is relied on to get back to evaporation endothermic section after steam-condensation, so move in circles, heat in flue gas is passed to cooling working medium endlessly, cooling working medium is heated, fume afterheat is utilized effectively.
Claims (5)
1. the U-shaped heat exchange of heat pipe integrated with electrostatic precipitator, comprise cooling working medium import header (4), hot working fluid outlet header (1) and be communicated with multiple cooling working medium sleeve pipes (3) of cooling working medium import header (4) and hot working fluid outlet header (1), it is characterized in that: also comprise multiple heat pipe (2), described heat pipe (2) is U-shaped heat pipe heat exchanging component, and the elbow (2-1) of 180 ° shaping by integrally bending and two straight sections (2-2) extended continuously form; Cooling working medium import header (4) is inserted on the top of described heat pipe (2), and insert in cooling working medium sleeve pipe (3), two straight sections (2-2) top soldering and sealing of described heat pipe (2) is also inserted in hot working fluid outlet header (1); Heat pipe (2) part do not inserted in cooling working medium import header (4) is evaporation endothermic section, and the part inserted in cooling working medium import header (4) is condensation heat release section; The import expanding section stage casing flue that described evaporation endothermic section is arranged on electrostatic precipitator is inner, and described condensation heat release section is placed in the outer top of import expanding section stage casing flue of electrostatic precipitator.
2. the U-shaped heat exchange of heat pipe integrated with electrostatic precipitator according to claim 1, is characterized in that: the extended surface of described heat pipe (2) adopts H type, spirality, aciculiform fin, plate shape fin or coupling fin shape.
3. the U-shaped heat exchange of heat pipe integrated with electrostatic precipitator according to claim 1, is characterized in that: the import expanding section stage casing flue that described heat pipe (2) is fixed on electrostatic precipitator by central dividing plate (5) is inner.
4. the U-shaped heat exchange of heat pipe integrated with electrostatic precipitator according to claim 1, is characterized in that: 180 ° of elbow horizontal layout of described heat pipe (2) are perpendicular to flue gas circulating direction or be parallel to flue gas circulating direction.
5. the U-shaped heat exchange of heat pipe integrated with electrostatic precipitator according to claim 1, is characterized in that: adopt H type, spirality, aciculiform fin, plate shape fin or coupling fin shape extended surface outside the evaporation endothermic section pipe of described heat pipe (2).
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CN201310468215.1A CN103512412B (en) | 2013-09-30 | 2013-09-30 | U-shaped heat pipe heat exchanging component and the U-shaped heat exchange of heat pipe integrated with electrostatic precipitator |
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CN103512412B true CN103512412B (en) | 2015-11-25 |
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CN105648513B (en) * | 2015-12-31 | 2018-08-07 | 天津君议台科技发展股份有限公司 | Heat pipe plating solution cooling system and working media |
CN106500519A (en) * | 2016-11-16 | 2017-03-15 | 江苏海云花新材料有限公司 | A kind of weaving terylene finishing agent production condenser |
CN107172860A (en) * | 2017-06-20 | 2017-09-15 | 太仓陶氏电气有限公司 | A kind of antistatic shockproof corrosion-resistant tubular radiator and its production method |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN2779248Y (en) * | 2005-02-07 | 2006-05-10 | 南京圣诺热管有限公司 | Separator tube hot-tube type steam generator |
CN102927548A (en) * | 2012-12-10 | 2013-02-13 | 南京圣诺热管有限公司 | Afterheat recycling device and method of high temperature flue gas containing high adhesive dust |
CN203731907U (en) * | 2013-09-30 | 2014-07-23 | 西安交通大学 | U-shaped heat pipe heat exchanging element and U-shaped heat pipe heat exchanger |
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JPH0345315B2 (en) * | 1984-11-06 | 1991-07-10 | Mitsubishi Electric Corp |
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Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN2779248Y (en) * | 2005-02-07 | 2006-05-10 | 南京圣诺热管有限公司 | Separator tube hot-tube type steam generator |
CN102927548A (en) * | 2012-12-10 | 2013-02-13 | 南京圣诺热管有限公司 | Afterheat recycling device and method of high temperature flue gas containing high adhesive dust |
CN203731907U (en) * | 2013-09-30 | 2014-07-23 | 西安交通大学 | U-shaped heat pipe heat exchanging element and U-shaped heat pipe heat exchanger |
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