CN202494359U - Modularized fluoroplastic tube gas heat exchanger - Google Patents
Modularized fluoroplastic tube gas heat exchanger Download PDFInfo
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- CN202494359U CN202494359U CN2012201351088U CN201220135108U CN202494359U CN 202494359 U CN202494359 U CN 202494359U CN 2012201351088 U CN2012201351088 U CN 2012201351088U CN 201220135108 U CN201220135108 U CN 201220135108U CN 202494359 U CN202494359 U CN 202494359U
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Abstract
The utility model discloses a modularized fluoroplastic tube gas heat exchanger, which comprises a heat exchanger shell and heat exchange tubes, wherein the upper end of the heat exchanger shell is provided with a water inlet and a water outlet, and the lower end of the heat exchanger shell is provided with a drain outlet; a water inlet end plate is detachably connected to the water inlet and is provided with a water inlet hole; a water outlet end plate is detachably connected to the water outlet and is provided with a water outlet hole; the heat exchange tubes are a U-shaped fluoroplastic heat exchange tube bundle; water inlet ends of fluoroplastic tubes in the fluoroplastic heat exchange tube bundle are communicated with the water inlet hole, and water outlet ends of the fluoroplastic tubes in the fluoroplastic heat exchange tube bundle are communicated with the water outlet hole; and positioning nets are distributed in the heat exchanger shell from top to bottom in parallel at an interval. According to the gas heat exchanger, modularized design is adopted, so that the equipment utilization rate of the gas heat exchanger can be greatly increased; and one positioning net is used every a certain distance for fixing the fluoroplastic heat exchange tube bundle, so that the flexible fluoroplastic tubes can be prevented from shaking to deform under the flow impact of gas.
Description
Technical field
The utility model relates to a kind of flue gas heat exchange device of in heat power plant boiler or other Industrial Boiler using waste heat from tail gas recovery systems, using.
Background technology
On heat power plant boiler or other Industrial Boilers; Be provided with and carry out the using waste heat from tail gas recovery system that flue gas waste heat recovery is used; In the using waste heat from tail gas recovery system, generally be that the flue gas heat exchange device is installed in wet flue gas desulfurization tower porch, reclaim fume afterheat through the flue gas heat exchange device.The flue gas heat exchange device is determining the performance of residual neat recovering system as the nucleus equipment of flue gas waste heat recovery system.Flue gas waste heat recovery significant, this is because flue gas waste heat recovery both can be used the waste heat of flue gas, and the temperature that gets into fume desulfurizing tower is reduced, and reduces the evaporation to the moisture in the desulfurization sprayed slurry, reduces the water consumption.
But, owing to contain composition such as sulphur in the fossil fuel such as fire coal, so when in heat power plant boiler or other Industrial Boilers, burning, can produce and contain sulfur dioxide SO
2, sulfur trioxide SO
3, corrosive gas such as hydrogen chloride HCL, hydrogen fluoride HF flue gas (claiming tail gas again), especially when exhaust gas temperature was lower than flue gas acid dew point, it is concentrated that above corrosive gas can condense, and produces acid and reveal, its corrosive power can be stronger.So in order to protect upstream device (comprising air preheater, deduster, air-introduced machine, flue, chimney etc.) and flue gas heat exchange device not to be corroded; When boiler design; Must guarantee flue-gas temperature at (generally between 110-140 ℃) more than the acid dew-point temperature, this is the irreducible main cause of exhaust gas temperature, also makes a large amount of heats pass through fume emission to atmosphere; Caused and to have reclaimed the flue gas part of waste heat, the not enough significant disadvantage of economic effect.
Heat exchanger tube in the existing flue gas heat exchange device generally is to adopt common stainless steel metal tube material, and it has following some shortcoming.1, because the heat exchanger tube wall surface temperature far below flue gas acid dew point, so can produce acid dew at the wall of heat exchanger cryogenic tube bundle, causes cold end corrosion; 2, the flue gas heat exchange device of existing common stainless steel metal tube material can not be realized the low-temperature heat exchange utilization of flue gas, if promptly think recovery flue gas heat as much as possible, just must reduce flue-gas temperature as far as possible; And meanwhile, the flue gas heat of recovery is many more, and then the cold end corrosion phenomenon on the heat exchanger tube of stainless steel metal tubing matter will be serious further; Make the life-span of heat exchanger tube be difficult to guarantee; That is to say that owing to limited by cold end corrosion, the flue gas heat exchange device of existing common stainless steel metal tube material can not be with the fume afterheat hyperabsorption; Must guarantee that flue-gas temperature more than acid dew point, can only absorb part of waste heat in the flue gas; 3, use in the flue gas that the boiler of fossil fuels such as fire coal produces and contain a certain amount of flue dust, acid is revealed and is contacted with flue dust, and scale problems is also inevitable, specifically; Be exactly when the cigarette temperature drop low, now is exposed in acid, flue dust reveals with acid and combines to generate dirty layer of hard in the flue gas; Be attached to the heat exchanger tube surface, and position, dead angle such as tube bundle support plate, because the requirement of heat exchange area; Make and restrain placed in close, even measures such as employing steam blowing also are difficult to thoroughly clean out; The dirt layer can be more and more thicker, finally makes heat exchanger gas collateral resistance surpass design load, even cause compressor emergency shutdown.
It is to adopt the special steel alloy material that can bear cold end corrosion that heat exchanger tube in the existing flue gas heat exchange device also has some, but its fancy price is difficult to let the people accept.Also there are some heat exchanger tubes to adopt metal tube to add the technology of anticorrosion lining; For example fume side serves as a contrast enamel, lined with fluoroplastic material, lining Teflon coating; Spraying silica SiO2 or aluminium oxide Al 2O3 etc.; But because the temperature difference is bigger before and after the heat exchanger itself, the generation lining that all is difficult to of lining hard material ftractures with avoiding, causes interior metal pipe local corrosion; The final safe operation that influences equipment, in addition the lined with fluoroplastic material also exist cost an arm and a leg, thermal conductivity factor is very low, heat exchanger volume is huge and fouling after can cause the damaged of outer lining fluorine plastic tube during the labor cleaning and make the shortcoming of interior metal pipe corrosion.
Heat exchanger tube in the existing flue gas heat exchange device also has some to adopt the heat exchanger tube of being processed by the fluoroplastics material fully; The shortcoming of this flue gas heat exchange device is that the fluorine plastic tube in the flue gas heat exchange device is flexibility; Under the impact flow of flue gas, be easy to generate the shake and deform; Not only be very easy to damage, and also variation thereupon of heat exchange efficiency.
In addition, existing flue gas heat exchange device structure is reasonable inadequately, as long as there is place's heat exchanger tube to go wrong, then whole flue gas heat exchange device all need be stopped transport and overhauled to cooperate, thus very inconvenient, need to improve.
The utility model content
The purpose of the utility model provides a kind of modular fluorine plastic tube flue gas heat exchange device, solve the technical problem that traditional flue gas heat exchange device structure is reasonable inadequately, keep in repair inconvenience; And solve Traditional use the flue gas heat exchange device of fluorine plastic tube damage easily and the technical problem of the easy variation of heat exchange efficiency.
For realizing above-mentioned purpose; The utility model adopts following technical scheme: a kind of modular fluorine plastic tube flue gas heat exchange device, be arranged in the exhaust gases passes, and be provided with the outer cover of heat exchanger that water inlet and delivery port, lower end are provided with sewage draining exit on comprising; And be arranged on outer cover of heat exchanger inside, be connected the heat exchanger tube between water inlet and the delivery port; It is characterized in that: said water inlet bolt is removably connected with the water inlet end plate, and has the inlet opening on the water inlet end plate, and said delivery port place bolt is removably connected with the delivery port end plate; And have apopore on the delivery port end plate; Said heat exchanger tube is the fluoroplastics heat-exchanging tube bundle of U-shaped, and the water inlet end of the fluorine plastic tube in the fluoroplastics heat-exchanging tube bundle is communicated with said inlet opening, and the water side of the fluorine plastic tube in the fluoroplastics heat-exchanging tube bundle is communicated with said apopore.
Longitudinal direction along said outer cover of heat exchanger can be provided with a row's water inlet and a discharge mouth of a river.
Said outer cover of heat exchanger is provided with water inlet, leans on flue gas air inlet one side to set out the mouth of a river by the flue gas side of giving vent to anger.
In outer cover of heat exchanger, parallel interval Distribution and localization net from top to bottom; This network for location is made up of the network for location parallel of parallel interval distribution and the network for location warp of parallel interval distribution; Said network for location parallel and network for location warp are the corrosion-and high-temp-resistant material of rigidity, the fluorine plastic tube in the said fluoroplastics heat-exchanging tube bundle from network for location parallel and network for location warp surround Kong Gezhong pass.
Be set in sequence in the Kong Gezhong of network for location along the weft direction of network for location, fluorine plastic tube in the said fluoroplastics heat-exchanging tube bundle, jump the Kong Gezhong that lattice are arranged on network for location along the warp direction of network for location, fluorine plastic tube in the said fluoroplastics heat-exchanging tube bundle.
Said network for location parallel and network for location warp surround the broadwise width of hole lattice can be 2mm～10mm, the warp-wise width can be 2mm～15mm.
Compared with prior art the utlity model has following characteristics and beneficial effect: the utility model is a kind of can low temperature resistant burn into antiscale ability strong, gas-water indirect heat exchanger that can the long-term safety reliability service, has the characteristics of rational in infrastructure, easy operating management, corrosion resistant, good antiscale property.Heat exchanger tube in the flue gas heat exchange device adopts the fluoroplastics material, can effectively solve the etching problem and the scale problems of flue gas heat exchange device, and the high efficiente callback fume afterheat, energy savings.In addition, the heat exchanger tube in the flue gas heat exchange device adopts the fluoroplastics material, has realized low-temperature heat exchange; Just can make flue gas waste heat recovery system in the maximum possible recovery fume afterheat; Weaken the cold end corrosion phenomenon of heat exchanger tube, in other words, exactly when having reached maximum energy-saving effect; Make the life-span of heat exchanger tube be able to guarantee, flue gas heat exchange device reliability is significantly improved.
The utility model adopts modular designs, and modular designs comprises that one or several are detachably connected on the heat exchange module on the outer cover of heat exchanger, and heat exchange module includes water inlet end plate, delivery port end plate and fluoroplastics heat-exchanging tube bundle.The largest benefit that adopts modular designs is that dismounting is easy, is convenient to equipment repair and maintenance, and this is because the import and export of heat exchange module is provided with shut-off valve (referring to Fig. 9, Figure 10); When being a heat exchange module, if the tube bank leakage problem can turn-off the shut-off valve at this place; Can unload it down maintenance or replacing then; When several heat exchange modules,, can turn-off the shut-off valve at this place if the tube bank leakage problem appears in a certain heat exchange module; Under the situation of other heat exchange module operation, the heat exchange module that goes wrong is isolated out maintenance separately or replacing then.This design can make the utilization rate of equipment and installations of flue gas heat exchange device significantly improve, and no longer takes place to leak the whole problem of stopping transport of flue gas heat exchange device that causes because of tube bank.In addition, because the fluoroplastics heat-exchanging tube bundle is flexible, so adopted the heat exchange module of fluoroplastics heat-exchanging tube bundles to remove more convenient.
The utility model replaces materials such as metal heat-exchanging tube bundle with flexible fluoroplastics heat-exchanging tube bundle, having produced can be corrosion-resistant, the novel flue gas heat exchange device of good antiscale property.The heat exchanger tube of flue gas heat exchange device adopts the fluoroplastics extrusion modling, has overcome common metal heat exchanger tube ubiquitous cold end corrosion, fouling, wear problem under flue gas condition.The fluoroplastics chemical property is stable, is one of corrosion-resistant material, is the ideal material of making the Korrosionsmedium heat exchanger; This material melting point is 310 ℃, thermal conductivity 0.24 w/ (m.K), and anti-flammability is the V-0 level; Tensile strength 28MPa has creep resistance, lubricity, non-viscosity, resistance to ag(e)ing, noninflammability, and heat endurance is very good; Simultaneously can long-term work under 200 ℃, satisfy the flue-gas temperature conditional request of large-sized boilers such as power station.
Compare with metal material,, be merely 0.19-0.24 w/ (m.K) though the thermal conductivity factor of flexible fluoroplastics heat exchanger tube is extremely low; But because the anticorrosive wear-resistant of flexible fluoroplastics heat exchanger tube decreases characteristic; Can with pipe do very thin, wall thickness is very thin, heat exchange tube diameter can be arranged between φ 3mm～10mm; Thereby obtained great heat exchange area; So the heat exchange area of tube bank normally the common metal heat exchange of heat pipe (the heat exchanger tube diameter is at 5～20 times of φ 20～30mm), thereby reaches huge exchange capability of heat, makes the whole coefficient of heat transfer of heat exchanger can reach 110～175 w/ (m
2.K).In addition, fluorine plastic tube is a flexible pipe, has overcome the disadvantage of the easy fouling corrosion of traditional metal heat exchange of heat pipe, can improve the good antiscale property performance of heat exchanger, and fouling is cleared up easily.Specifically; Be exactly under the flow of flue gas effect, fluorine plastic tube can produce small size vibrations and swing, and the black dirt that is attached to the surface is difficult to form big lump; Be rarefaction; Be convenient to cleaning, the while fluoroplastics surface not characteristics of viscosity can make most of black dirt come off voluntarily, can also adopt the dust stratification that adheres to of water backwashing manner exchange heat pipe outer wall to clear up in addition.
Described network for location is applied in the utility model (in the inside of the utility model; Whenever keep at a certain distance away and just use a network for location to fix the fluoroplastics heat-exchanging tube bundle); The location (fixing) that is used for the fluoroplastics heat-exchanging tube bundle can prevent that like this fluoroplastics heat-exchanging tube bundle of flexibility from shaking distortion under the impact flow of flue gas, can also make each fluoroplastics heat exchanger tube keep the gap; Flue gas is circulated smoothly, guarantee flue gas and the abundant contact heat-exchanging of fluoroplastics heat exchanger tube; The version of network for location can make the plane of orientation of fluoroplastics heat-exchanging tube bundle that dust stratification does not take place; Guarantee the reliability service of the utility model; Guarantee the heat exchange efficiency of the utility model, that is to say, improved the service life and the operational reliability of fluoroplastics heat-exchanging tube bundles greatly.
Description of drawings
Below in conjunction with accompanying drawing the utility model is done further detailed explanation.
Fig. 1 is the structural representation that is provided with the utility model of two groups of heat exchange modules.
Fig. 2 is the sketch map of the A-A section among Fig. 1.
Fig. 3 is the sketch map of the B-B section among Fig. 1.
Fig. 4 is the sketch map of the C-C section among Fig. 1.
Fig. 5 is the enlarged diagram at I place among Fig. 4.
Fig. 6 is the sketch map of water inlet end plate.
Fig. 7 is the sketch map of delivery port end plate.
Fig. 8 is the sketch map that is provided with the utility model of six groups of heat exchange modules.
Fig. 9 is that the utility model that is provided with two groups of heat exchange modules is connected the principle schematic on the exhaust gases passes.
Figure 10 is that the utility model that is provided with six groups of heat exchange modules is connected the principle schematic on the exhaust gases passes.
Reference numeral: 1-outer cover of heat exchanger, 2-water inlet, 3-delivery port, 4-sewage draining exit, 5-exhaust gases passes, 6-water inlet end plate, 6.1-inlet opening, 7-delivery port end plate, 7.1-apopore, 8-fluoroplastics heat-exchanging tube bundle, 9-network for location, 9.1-network for location parallel, 9.2-network for location warp, 9.3-hole lattice, 10-shut-off valve.
The specific embodiment
Embodiment one is referring to Fig. 1-Fig. 3, Fig. 6, shown in Figure 7; This modular fluorine plastic tube flue gas heat exchange device is arranged in the exhaust gases passes 5, is provided with the outer cover of heat exchanger 1 that water inlet 2 and delivery port 3, lower end are provided with sewage draining exit 4 on comprising; And be arranged on outer cover of heat exchanger inside, be connected the heat exchanger tube between water inlet 2 and the delivery port 3; Said water inlet 2 place's bolts are removably connected with water inlet end plate 6, and have inlet opening 6.1 on the water inlet end plate 6, and said delivery port 3 place's bolts are removably connected with delivery port end plate 7; And have apopore 7.1 on the delivery port end plate 7; Said heat exchanger tube is the fluoroplastics heat-exchanging tube bundle 8 of U-shaped, and the water inlet end of the fluorine plastic tube in the fluoroplastics heat-exchanging tube bundle 8 is communicated with said inlet opening 6.1, and the water side of the fluorine plastic tube in the fluoroplastics heat-exchanging tube bundle 8 is communicated with said apopore 7.1.The two ends of fluoroplastics heat-exchanging tube bundle 8 are fixed on water inlet end plate 6 and the delivery port end plate 7.Said outer cover of heat exchanger is provided with water inlet 2, leans on flue gas air inlet one side to set out the mouth of a river 3 by the flue gas side of giving vent to anger.Said fluorine plastic tube has flexible nature by the fluoroplastics extrusion modling.Said outer cover of heat exchanger is generally rectangle, and concrete size is confirmed according to the size of the exhaust gases passes 5 that connects.
Refrigerant medium in the modular fluorine plastic tube flue gas heat exchange device is a condensate.Heat exchange process is to flow in the exhaust gases passes 5 of flue gas outside heat exchanger tube, and condensate flows in heat exchanger tube, and water-gas carries out heat exchange through the tube wall of fluoroplastics heat-exchanging tube bundle.
Longitudinal direction along said outer cover of heat exchanger is provided with a row's water inlet 2 and a discharge mouth of a river 3.The quantity of water inlet 2 and delivery port 3 is decided an in general minimum water inlet 2 and delivery port 3 of being provided with according to the width of exhaust gases passes 5.Said water inlet end plate 6, delivery port end plate 7 and fluoroplastics heat-exchanging tube bundle 8 have been formed heat exchange module, in the flue gas heat exchange device one or several heat exchange modules can be arranged.The quantity of heat exchange module is corresponding with the quantity of water inlet 2 and delivery port 3.In other words, dispose the quantity of heat exchange module exactly according to the requirement of heat exchange area, the import and export of the condensate of flue gas heat exchange device can form advances the form of having more more.
Referring to Fig. 3, in embodiment one, the warp direction of the said outer cover of heat exchanger in edge is provided with two water inlets 2 and two delivery ports 3, is provided with two heat exchange modules simultaneously.Referring to Fig. 8, in embodiment two, the warp direction of the said outer cover of heat exchanger in edge is provided with six water inlets 2 and six delivery ports 3, is provided with six heat exchange modules simultaneously.
Referring to Fig. 9, Figure 10, the import and export of heat exchange module is provided with shut-off valve 10, promptly with water inlet pipe that water inlet 2 is connected on with outlet pipe that delivery port 3 is connected on shut-off valve 10 is set.Shut-off valve can be in operation each heat exchange module to isolate maintenance.When the heat exchanger tube of flue gas heat exchange device takes place to leak, can the shut-off valve of one of them heat exchange module branch intake-outlet cut out, move other heat exchange module then, through the examination of a heat exchange module of a heat exchange module, judge the leak point.After judging the residing heat exchange module in fluoroplastics heat-exchanging tube bundle leak point, normal heat exchange module is opened the shut-off valve at intake-outlet place, works on; The shut-off valve at the intake-outlet place of out of order heat exchange module cuts out; After shutoff is carried out in tube bank to fault, open the shut-off valve of its import and export, flue gas heat exchange device integral body is put into operation; Guarantee flue gas heat exchange device half capacity operation at least, so totally improved equipment availability.
Referring to Fig. 1, Fig. 4, Fig. 5; In outer cover of heat exchanger 1, from top to bottom parallel interval is distributed with network for location 9; This network for location 9 is made up of parallel interval network for location parallel 9.1 that distributes and the network for location warp 9.2 that parallel interval distributes; Said network for location parallel and network for location warp are the corrosion-and high-temp-resistant material of rigidity, the fluorine plastic tube in the said fluoroplastics heat-exchanging tube bundle 8 from network for location parallel 9.1 and network for location warp 9.2 surround hole lattice 9.3 pass.The size of hole lattice 9.3 confirms that according to the heat-exchanging tube bundle caliber in general, the broadwise width d1 of hole lattice 9.3 is 2mm～10mm, and warp-wise width d2 is 2mm～15mm.Network for location is corrosion-resistant material (corrosive deposit in the ability flue gas), and the selection principle has certain rigid for can tolerate 200 ℃.
Referring to Fig. 5; As most preferred embodiment; Be set in sequence in the hole lattice 9.3 of network for location 9 along the weft direction of network for location, fluorine plastic tube in the said fluoroplastics heat-exchanging tube bundle 8, jump lattice along the warp direction of network for location, fluorine plastic tube in the said fluoroplastics heat-exchanging tube bundle 8 and be arranged in the hole lattice 9.3 of network for location 9.Adopt this arrangement; The one, can make each fluoroplastics heat exchanger tube keep the gap; Flue gas is circulated smoothly; Make the heat exchanger effectiveness of fluoroplastics heat-exchanging tube bundle 8 the highest, the 2nd, the jumping lattice leave the empty part branch in the middle of being provided with and can making network for location, and the empty part branch can make the dust stratification between two heat exchanger tubes not retain.
In order to cooperate the detachable of heat exchange module, being connected between network for location and the outer cover of heat exchanger removably connects.When heat exchange module was one, network for location was a little network for location.When heat exchange module when being a plurality of, network for location is the big network for location that a plurality of little network for location by correspondence is combined into, and also removably connects between the little network for location of two adjacent heat exchange modules.
Among Fig. 1, Fig. 3, Fig. 4 and Fig. 8-Figure 10, solid arrow is represented the trend of condensate, and hollow arrow is represented the flow direction (flue gas is horizontally through the flue gas heat exchange device shown in figure hollow core arrow) of flue gas.
In the heat power plant boiler flue gas waste heat recovery experimental project of certain 600MW capacity, arrange the flue gas heat exchange device at the boiler of power plant back-end ductwork, absorb waste heat in the flue gas, be used for hot-water supply outside factory.The initial designs condition is: flue gas heat exchange device inlet flue gas flow is 2610t/h, 123 ℃ of smoke inlet temperature, and 35 ℃ of water inlet temperature require to be heated to be 78 ℃ of hot water.As adopt common metal pipe flue gas heat exchange device, for preventing the cold end corrosion problem in the flue gas waste heat recovery, flue-gas temperature can only drop to 100 ℃, still has great amount of heat energy to be brought into smoke stack emission by flue gas.When adopting the utility model flue gas heat exchange device, can the exhanst gas outlet temperature be reduced to 60 ℃, can heat 720t/h hot water, add hot 450t/h hot water during than use common metal pipe flue gas heat exchange device.
Heat exchanger in the instantiation adopts the fluorine plastic tube of extraordinary fluoroplastics extrusion modling Φ 8 * 0.8mm as heat exchanger tube, and it is 10620m that the total heat area is changed in tube bank
2, assembling side by side by 1～No. 6 six modular unit, the tube bank heat exchange area of each module is 1328m
2, the fume side of each module is imported and exported and is of a size of 1.62 * 11m, and module thickness is 0.9m; Each module water side-entrance all is provided with shut-off valve, can control water inlet state separately separately, and each module water side is imported and exported bore and is DN300mm; The water passing capacity of each module is 170t/h; Six modules are assembled side by side and are become a flue gas heat exchange device, and the fume side of flue gas heat exchange device is imported and exported and is of a size of 13.76 * 11m, and flue gas heat exchange device thickness is 0.9m.It is the ordinary carbon steel material that outer cover of heat exchanger adopts material, liner high temp glass scale anticorrosion.Flue gas heat exchange device inlet flue gas flow is 2610t/h, 123 ℃ of smoke inlet temperature, and 60 ℃ of exhanst gas outlet temperature, 35 ℃ of water inlet temperature, 78 ℃ of water outlet temperatures, discharge is 720t/h.Discovery heat-exchanging tube bundle in service has leakage situation, can close the terminal valve of 1 ~ No. 6 module one by one, and one of them module is isolated out from running status, and other modules continue maintenance work, and heat supply this moment outlet capacity still is higher than 900t/h.Carry out examination and maintenance to isolating the module that, open terminal valve after maintenance is accomplished, continue to devote oneself to work, this is provided with form significantly improves the utilization rate of equipment and installations of flue gas heat exchange device, no longer takes place to cause the whole shut down condition of flue gas heat exchange device because of the tube bank leakage.
In flue gas waste heat recovery system, by the fluoroplastics heat-exchanging tube bundle replace the metal heat-exchanging tube bundle to produce can be corrosion-resistant, the utility model of good antiscale property, good energy-conserving effect, stable, utilization rate of equipment and installations is high.The hot water profit is by 10 yuan/t, and power plant's annual utilization hours calculated by 5500 hours, 1 600MW thermal power plant coal-powder boiler, and behind use the utility model, profit increases by 2,475 ten thousand yuan/year, remarkable in economical benefits during than use common metal pipe flue gas heat exchange device.
Claims (6)
1. modular fluorine plastic tube flue gas heat exchange device; Be arranged in the exhaust gases passes (5); Be provided with the outer cover of heat exchanger (1) that water inlet (2) and delivery port (3), lower end are provided with sewage draining exit (4) on comprising; And the heat exchanger tube that is arranged on outer cover of heat exchanger inside, is connected water inlet between (2) and the delivery port (3); It is characterized in that: said water inlet (2) is located bolt and is removably connected with water inlet end plate (6), and has inlet opening (6.1) on the water inlet end plate (6), and said delivery port (3) is located bolt and is removably connected with delivery port end plate (7); And have apopore (7.1) on the delivery port end plate (7); Said heat exchanger tube is the fluoroplastics heat-exchanging tube bundle (8) of U-shaped, and the water inlet end of the fluorine plastic tube in the fluoroplastics heat-exchanging tube bundle (8) is communicated with said inlet opening (6.1), and the water side of the fluorine plastic tube in the fluoroplastics heat-exchanging tube bundle (8) is communicated with said apopore (7.1).
2. modular fluorine plastic tube flue gas heat exchange device according to claim 1 is characterized in that: the longitudinal direction along said outer cover of heat exchanger is provided with a row's water inlet (2) and a discharge mouth of a river (3).
3. modular fluorine plastic tube flue gas heat exchange device according to claim 1 is characterized in that: said outer cover of heat exchanger is provided with water inlet (2), leans on flue gas air inlet one side to set out the mouth of a river (3) by the flue gas side of giving vent to anger.
4. modular fluorine plastic tube flue gas heat exchange device according to claim 1; It is characterized in that: in outer cover of heat exchanger (1), from top to bottom parallel interval is distributed with network for location (9); This network for location (9) is made up of the network for location parallel (9.1) of parallel interval distribution and the network for location warp (9.2) of parallel interval distribution; Said network for location parallel and network for location warp are the corrosion-and high-temp-resistant material of rigidity, the fluorine plastic tube in the said fluoroplastics heat-exchanging tube bundle (8) from network for location parallel (9.1) and network for location warp (9.2) surround hole lattice (9.3) pass.
5. modular fluorine plastic tube flue gas heat exchange device according to claim 4; It is characterized in that: be set in sequence in the hole lattice (9.3) of network for location (9) along the weft direction of network for location, fluorine plastic tube in the said fluoroplastics heat-exchanging tube bundle (8), jump lattice along the warp direction of network for location, fluorine plastic tube in the said fluoroplastics heat-exchanging tube bundle (8) and be arranged in the hole lattice (9.3) of network for location (9).
6. modular fluorine plastic tube flue gas heat exchange device according to claim 4; It is characterized in that: said network for location parallel (9.1) and network for location warp (9.2) surround the broadwise width (d1) of hole lattice (9.3) be 2mm～10mm, warp-wise width (d2) is 2mm～15mm.
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| CN2012201351088U CN202494359U (en) | 2012-04-01 | 2012-04-01 | Modularized fluoroplastic tube gas heat exchanger |
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| CN2012201351088U CN202494359U (en) | 2012-04-01 | 2012-04-01 | Modularized fluoroplastic tube gas heat exchanger |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102607299A (en) * | 2012-04-01 | 2012-07-25 | 北京新世翼节能环保科技股份有限公司 | Module type flue gas heat exchanger with fluorine plastic pipes |
| CN103411449A (en) * | 2013-08-28 | 2013-11-27 | 长沙华成换热设备有限公司 | Large combined type box heat exchanger |
| CN106017149A (en) * | 2016-05-30 | 2016-10-12 | 欧阳顺亮 | Fume heat exchanger and welding method of fume heat exchanger |
| CN106705110A (en) * | 2016-09-30 | 2017-05-24 | 上海双木散热器制造有限公司 | Anti-corrosion steam air preheater pipeline system for waste incineration power generation |
| EP3792552A1 (en) * | 2019-09-03 | 2021-03-17 | SL-Technik GmbH | Biomass heating system with flue gas condensation |
-
2012
- 2012-04-01 CN CN2012201351088U patent/CN202494359U/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102607299A (en) * | 2012-04-01 | 2012-07-25 | 北京新世翼节能环保科技股份有限公司 | Module type flue gas heat exchanger with fluorine plastic pipes |
| CN103411449A (en) * | 2013-08-28 | 2013-11-27 | 长沙华成换热设备有限公司 | Large combined type box heat exchanger |
| CN103411449B (en) * | 2013-08-28 | 2016-04-27 | 长沙华成换热设备有限公司 | Large-scale combined box heat exchanger |
| CN106017149A (en) * | 2016-05-30 | 2016-10-12 | 欧阳顺亮 | Fume heat exchanger and welding method of fume heat exchanger |
| CN106705110A (en) * | 2016-09-30 | 2017-05-24 | 上海双木散热器制造有限公司 | Anti-corrosion steam air preheater pipeline system for waste incineration power generation |
| CN106705110B (en) * | 2016-09-30 | 2018-07-10 | 上海双木散热器制造有限公司 | Corrosion-proof type waste incineration and generating electricity steam type airheater pipe-line system |
| EP3792552A1 (en) * | 2019-09-03 | 2021-03-17 | SL-Technik GmbH | Biomass heating system with flue gas condensation |
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