CN103090400B - Waste gas and water incineration disposal device - Google Patents
Waste gas and water incineration disposal device Download PDFInfo
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- CN103090400B CN103090400B CN201310033412.0A CN201310033412A CN103090400B CN 103090400 B CN103090400 B CN 103090400B CN 201310033412 A CN201310033412 A CN 201310033412A CN 103090400 B CN103090400 B CN 103090400B
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Abstract
The invention provides a waste gas and water incineration disposal device and belongs to the technical field of environmentally protective facility. The waste gas and water incineration disposal device comprises an incinerator, a heat exchanger and a dust extraction mechanism. A top portion of the incinerator forms an air inlet chamber; an organic waste gas introducing interface which is communicated with the air inlet chamber is arranged on the lateral portion of the air inlet chamber. A burner is arranged on the top portion of the air inlet chamber, the burner probes into a furnace hearth of the incinerator after passing through the air inlet chamber, a smoke extraction pipe which is communicated with the furnace hearth is arranged on the bottom portion of the incinerator. A furnace gate is arranged on the upper lateral portion of the incinerator. The heat exchanger is accompanied with the incinerator, the smoke extraction pipe is connected with the heat exchanger and the dust extraction mechanism is connected with the heat exchanger pipeline. The waste gas and water incineration disposal device is characterized by comprising an organic wastewater import mechanism which is used for spraying the organic wastewater into a smoke extraction pipe chamber for evaporating in a spray pattern. The organic wastewater introducing mechanism is connected with the smoke extraction and probes into the smoke extraction pipe chamber. The waste gas and water incineration disposal device has the advantages that the investment in the device is reduced, the energy is saved and the inputted human resources for pollution control are reduced and the second pollution is avoided.
Description
Technical field
The invention belongs to technical field of environmental protection facilities, be specifically related to a kind of waste gas, water incineration disposal device.
Background technology
In the production process of industrial products, in order to avoid the waste gas, waste water and the solid waste (custom claims the three wastes) that produce cause the pollution to environment, therefore usually need to process, and along with the difference of poisonous and harmful composition, the treating apparatus used is also different.The technical information of the various environmental protection facilities about process waste gas can be seen in a large number in Chinese patent literature, slightly with exemplify if CN1084460C(is for the emission-control equipment of incinerating apparatus), CN1517589A(Waste gas treatment system for paint drying oven), CN101539298A(is used for the waste gas processing method of steel plate color-coating line and incinerator), the energy saver of CN101893248B(volatide organic waste gas treating system), CN202289783U(waste gas treatment equipment) and CN101788152A(waste gas treatment equipment and waste gas processing method), etc.
Be not limited to the above-mentioned patent that exemplifies and patent application scheme all for exhaust-gas treatment, the process thus for waste water does not have referential technical meaning.As is known in the industry, not only a large amount of waste gas can be produced in the production process of some industrial products, and produce reluctant a large amount of waste water simultaneously, typical example as in producing at coating film on glass except the waste gas of being discharged by kiln, be also attended by and such as the sewage produced discharged etc. to raw material workshop and flushings of Workplace terrace, circulation discharge, waste heat boiler blowdown, desulphurization system.The chemical analysis of the waste gas that kiln is discharged is very complicated, such as containing hydrogen, nitrogen, carbon monoxide, carbon dioxide, helium, hydrogen chloride, methane, ethene, methyl alcohol, formaldehyde, dimethyltin chloride, tin ash, fluoride, titanium tetrachloride, titanium dioxide, silica, silane and antimony oxide, etc., and be also often rich in this type of material in sewage.Therefore, for producing the manufacturer of this series products (low radiation coated glass), need to overlook either of the two ground or claim one should to process with favouring one and slighting the other to waste gas and waste water with working along both lines, only this really could embody being responsible for the environment that the mankind depend on for existence.
Technical information in the pollutant process produced in coating film on glass is produced can be seen in equally in disclosed Chinese patent literature, " waste gas processing method of float glass process online production low radiation coated glass " that such as publication number CN101274151A recommends; And for example Authorization Notice No. CN202109499U " the online low-radiation coating waste gas treatment device " that provide; For another example publication No. CN102614761A introduce " coating film on glass exhaust-gas treatment dry method energy-saving technique ", etc.In these the three sections of patent documents exemplified, CN101274151A adopts the mode of condensation and multi-stage spray to process to organic exhaust gas, and the deficiency that this patent formula exists is: treatment effeciency is low, water resources consumption amount large, the equipment that comes into operation is many, poor processing effect and there is the anxiety of secondary pollution.Because all the other two sections of patent documents adopt burning mode to process organic exhaust gas, the deficiency of CN101274151A thus can be made up.But all there is the problem of attending to one thing and lose sight of another in these three patent formula being not limited to exemplify, so-called Gu this be the process focused on organic exhaust gas, so-called mistake that be the disposal ignored organic wastewater.Although can according to the common practise to pollutant control by organic wastewater otherwise processed, separate waste gas and waste water to process certainly producing following technical problem: one, the equipment that comes into operation significantly increases, thus causes processing cost to increase; Its two, due to separately process, be therefore unfavorable for saving to greatest extent control gas, when harnessing the river consume the energy got; Its three, drop into manpower many and be unfavorable for saving valuable human resources; Its four, due to by the separately process of waste gas, waste water, be therefore both unfavorable for controlling, easily increased again the probability of secondary pollution.
In view of above-mentioned prior art, be necessary to be improved, for this reason, the applicant has done lasting exploration, finally define technical scheme described below, and carried out simulated test in the applicant plant area taking under strict secrecy provision, result proves practicable.
Summary of the invention
Task of the present invention is to provide a kind of and contributes to organic exhaust gas and organic wastewater to process with running neck and neck and use saving equipment, save the energy, reduce human input and both conveniently can control waste gas, the water incineration disposal device that can avoid secondary pollution.
Task of the present invention has been come like this, a kind of waste gas, water incineration disposal device, comprise an incinerator, the top of this incinerator is configured with an inlet plenum, the sidepiece of this inlet plenum is provided with an organic exhaust gas and introduces interface, this organic exhaust gas is introduced interface and is communicated with inlet plenum, a burner is provided with at the top of inlet plenum, this burner is insinuated in the burner hearth of incinerator after approach inlet plenum, one is connected for the smoke exhaust pipe by the high-temperature flue gas extraction in burner hearth in the bottom of incinerator, this smoke exhaust pipe communicates with described burner hearth, and be provided with one in the following side of incinerator for implementing clean fire door to burner hearth, one heat exchanger and a dedusting mechanism, heat exchanger is with described incinerator, described smoke exhaust pipe is connected with this heat exchanger, and dust-falling mechanism is connected with heat exchanger pipeline, for draining into the external world to the flue gas ash removal coming from heat exchanger after dedusting, be characterised in that: also include one for organic wastewater to be injected into the organic wastewater retraction mechanism of evaporating in the smoke evacuation tube chamber of described smoke exhaust pipe with spray pattern, this organic wastewater retraction mechanism is connected with smoke exhaust pipe and is insinuated in described smoke evacuation tube chamber.
In a specific embodiment of the present invention, described organic wastewater retraction mechanism comprises spray gun, shower nozzle, pure air inlet tube, compressed air inlet tube and organic wastewater inlet tube, spray gun and described incinerator are fixed, and one end of this spray gun is insinuated in described smoke evacuation tube chamber, shower nozzle is positioned at smoke evacuation tube chamber and fixes with described one end of spray gun, pure air inlet tube, compressed air inlet tube are all connected with the other end of described spray gun with organic wastewater inlet tube, and communicate with described shower nozzle.
In another specific embodiment of the present invention, described spray gun comprises pure air fairlead, compressed air fairlead and organic wastewater fairlead, pure air fairlead and described incinerator are fixed, one end of this pure air fairlead is insinuated in the smoke evacuation tube chamber of described smoke exhaust pipe, be connected with described shower nozzle and communicate with shower nozzle, compressed air fairlead is positioned at the pure air fairlead tube chamber of pure air fairlead, one end of this compressed air fairlead is connected with shower nozzle and communicates with shower nozzle, organic wastewater fairlead is positioned at the compressed air fairlead tube chamber of compressed air fairlead, one end of this organic wastewater fairlead is connected with shower nozzle and communicates with shower nozzle, described pure air inlet tube is connected with the other end of pure air fairlead, and communicate with pure air fairlead tube chamber, described compressed air inlet tube is connected with the other end of compressed air fairlead, and communicate with compressed air fairlead tube chamber, described organic wastewater inlet tube is connected with the other end of organic wastewater fairlead, and communicate with the organic wastewater fairlead tube chamber of organic wastewater fairlead.
In another specific embodiment of the present invention, described shower nozzle comprises exterior nut cap, interior nut, nozzle and mixing cap, the outer wall of described one end of exterior nut cap and described pure air fairlead is fixed, and communicate with the smoke evacuation tube chamber of the described smoke exhaust pipe of described incinerator, the outer wall of described one end of interior nut and described compressed air fairlead is fixed, the outer wall of described one end of mixing cap and described organic wastewater fairlead is fixed, nozzle is fixed on described one end of compressed air fairlead by interior nut, and it is corresponding with mixing cap, described pure air fairlead tube chamber communicates with described exterior nut cap, described compressed air fairlead tube chamber communicates with mixing cap, described organic wastewater fairlead tube chamber communicates with mixing cap, and mix cap and communicate with nozzle.
In another specific embodiment of the present invention, a spout is configured with in the middle position of described exterior nut cap, this spout communicates with the smoke evacuation tube chamber of described smoke exhaust pipe, described nozzle is configured with spray orifice, spray orifice communicates with spout, and lead to the described cap that mixes, the wall body of mixing cap offers compressed air introduction hole, and this compressed air introduction hole communicates with described compressed air fairlead tube chamber.
Also have in a specific embodiment of the present invention, the outer wall of described pure air fairlead is fixed with a spray gun mounting flange, and this spray gun mounting flange and described incinerator are fixed.
More of the present invention and in a specific embodiment, the pipeline of described pure air inlet tube is equipped with pure air control valve; The pipeline of described compressed air inlet tube is equipped with compressed air regulating valve; The pipeline of described organic wastewater inlet tube is equipped with organic wastewater control valve.
In an of the present invention and then specific embodiment, described heat exchanger is tubular heat exchanger or tube coil type heat exchanger.
Of the present invention again more and in a specific embodiment, described dedusting mechanism comprises support, motor, blower fan and dust cleaning case, support is bearing on the terrace of field of employment, motor and blower fan connect, and be fixed on support by blower fan together with motor, the flue gas mouth that enters of this blower fan is connected with dust cleaning case, and the exhaust smoke outlet of blower fan is communicated with the external world by pipeline, dust cleaning case is fixed on support, and described heat exchanger is between described incinerator and support.
In an again of the present invention and then specific embodiment, the outer wall of described incinerator is provided with heat-insulation layer.
Technical scheme provided by the invention owing to having arranged an organic wastewater retraction mechanism on the smoke exhaust pipe of incinerator, thus while burning organic exhaust gas, organic wastewater is evaporated and the toxic organics in organic wastewater is burned by high-temperature flue gas, play the effect of the double gain that waste gas waste water is administered simultaneously, not only equipment investment can be reduced, economize energy, and the human resources that can reduce input by pollution treatment, and secondary pollution can be avoided.
Accompanying drawing explanation
Fig. 1 is embodiments of the invention schematic diagram.
The concrete structure figure that Fig. 2 is the spray gun shown in Fig. 1 and shower nozzle.
Fig. 3 is the partial enlarged drawing of Fig. 2.
Detailed description of the invention
In order to enable the auditor of Patent Office especially the public clearly understand technical spirit of the present invention and beneficial effect, applicant will elaborate below by way of example, but be not all the restriction to the present invention program to the description of embodiment, any conceive according to the present invention done be only pro forma but not substantial equivalent transformation and all should be considered as technical scheme category of the present invention.
Refer to Fig. 1, give an incinerator 1, an inlet plenum 11 is equipped at the top of this incinerator 1, one burner 112 using oil as fuel is installed at the top of this inlet plenum 11, this burner 112 is being insinuated in the burner hearth 12 of incinerator 1 after inlet plenum 11, is equipped with an organic exhaust gas introduces interface 111 at the sidepiece of inlet plenum 11.Because the present embodiment is for the organic exhaust gas of low radiation coated glass production industry and organic wastewater, therefore, organic exhaust gas in low-emission coated production technology (pipeline is furnished with valve) by the road by organic exhaust gas introduce interface 111 introduce inlet plenum 11, and in burner hearth 12 combustion of incinerator 1 be mixed to required oil-gas ratio with fuel oil in inlet plenum 11 after, high-temperature flue gas in burning process is discharged by the smoke exhaust pipe 13 connected in the bottom of incinerator 1, carries out subsequent treatment.Be equipped with one to be conducive to implementing regularly burner hearth 12 or irregularly cleaning the fire door 14 of maintenance in the following side of incinerator 1.In addition, energy-conservation in order to embody, namely in order to avoid incinerator 1 heat trnasfer and heat radiation, be therefore provided with on the outer wall of incinerator 1 or claim to be enclosed with heat-insulation layer 15, preferred scheme can arrange smoke exhaust pipe heat-insulation layer 132 equally to aforesaid smoke exhaust pipe 15.In a state of use, incinerator 1 is supported on terrace by group leg of bottom it 16.
Please continue to refer to Fig. 1, give the heat exchanger 2 with incinerator 1, aforesaid smoke exhaust pipe 13 is connected with this heat exchanger 2, that is, the smoke exhaust pipe tube chamber 131 of smoke exhaust pipe 13 communicates with heat exchanger 2.Because heat exchanger 2 belongs to widely used known technology, therefore applicant illustrate only low-temperature receiver intake 21 and the thermal source outlet 22 of heat exchanger 2, and low-temperature receiver alleged here mainly refers to cold water, and thermal source is then hot water.In the present embodiment, heat exchanger 2 uses tubular heat exchanger or tube coil type heat exchanger, and what flow through in pipe is water, and pipe is outer then for coming from the flue gas of smoke exhaust pipe 13.During use, by low-temperature receiver intake 21, cold water is introduced tubulation or the coil pipe of heat exchanger, then drawn by thermal source outlet 22 and in addition reuse, so circulation and flue-gas temperature is reduced.
The heat exchange gas smoke exhaust pipe 23 of aforesaid heat exchanger 2 is connected with dedusting mechanism 3, this dedusting mechanism 3 comprises support 31, motor 32, blower fan 33 and dust cleaning case 34, support 31 is bearing on terrace, motor 32 and blower fan 33 transmission connect, and be fixed on support 31 by blower fan 33 together with motor 32, the flue gas mouth 331 that enters of blower fan 33 is connected with the dust cleaning case outlet flue of dust cleaning case 34, and the exhaust smoke outlet 332 of blower fan 33 is communicated with the external world by pipeline, dust cleaning case 34 is fixed on support 31, the dust cleaning case of this dust cleaning case 34 enters mouth 341 and is connected with aforesaid heat exchanger smoke exhaust pipe 23.Preferred scheme, arranges electrostatic precipitator and/or low-temperature plasma purifier in dust cleaning case 34, or adopts the dust arrester of such as being instructed by Chinese patent ZL200510200344.8, ZL02233407.6 and CN101549249A etc.From aforementioned explanation, blower fan 33 is essentially air exhauster.
Technical essential as technical scheme provided by the invention: be equipped with one and gasify and the organic wastewater retraction mechanism 4 of burning for being injected into spray pattern by organic wastewater in smoke evacuation tube chamber 131 to evaporate on aforesaid smoke exhaust pipe 13, this organic wastewater retraction mechanism 4 is insinuated in smoke evacuation tube chamber 131.
Mention above organic wastewater retraction mechanism 4 preferably but not the structure be definitely limited to is as follows: comprise spray gun 41, shower nozzle 42, pure air inlet tube 43, compressed air inlet tube 44 and organic wastewater inlet tube 45, position and aforementioned incinerator 1 that spray gun 41 is corresponding to smoke exhaust pipe 13 are fixed, and one end of this spray gun 41 and the right-hand member shown in Fig. 1 are insinuated in smoke evacuation tube chamber 131, and shower nozzle 42 is positioned at smoke evacuation tube chamber 131 and fixes with aforementioned one end of spray gun 41.Pure air inlet tube 43, compressed air inlet tube 44 are all connected with the other end of spray gun 41 with organic wastewater inlet tube 45, and communicate with shower nozzle 42.
Refer to Fig. 2 and Fig. 3 and continue composition graphs 1, above mentioned spray gun 41 preferably but not the structure be definitely limited to is as follows: comprise pure air fairlead 411, compressed air fairlead 412 and organic wastewater fairlead 413, position and aforementioned incinerator 1 that pure air fairlead 411 is corresponding to smoke exhaust pipe 13 are fixed, one end of this pure air fairlead 411 and the right-hand member of shown position state are insinuated in smoke evacuation tube chamber 131 (Fig. 1 shows), be connected with shower nozzle 42, and communicate with shower nozzle 42.Compressed air inlet tube 412 is positioned at the pure air fairlead tube chamber 4111 of pure air fairlead 411, namely one end of this compressed air fairlead 412 illustrates right-hand member and is connected with shower nozzle 42, and communicate with shower nozzle 42, organic wastewater fairlead 413 is positioned at the compressed air fairlead tube chamber 4121 of compressed air fairlead 412, one end (right-hand member) of this organic wastewater fairlead 413 is connected with shower nozzle 42, and communicates with shower nozzle 42.Namely aforesaid pure air inlet tube 43 illustrates left end with the other end of pure air fairlead 411 and is connected, and communicates with pure air fairlead tube chamber 4111; Namely aforesaid compressed air inlet tube 44 illustrates left end with the other end of compressed air fairlead 412 and is connected, and communicates with compressed air fairlead tube chamber 4121; Namely aforesaid organic wastewater inlet tube 45 illustrates left end with the other end of organic wastewater fairlead 413 and is connected, and communicates with the organic wastewater fairlead tube chamber 4131 of organic wastewater fairlead 413.As shown in Figure 2, pure air fairlead 411 is fixed with a spray gun mounting flange 4112, this spray gun mounting flange 4112 is fixed with incinerator 1, more precisely fixes with aforementioned leg 16.
Aforesaid shower nozzle 42 preferably but not the structure be definitely limited to is as follows: comprise exterior nut cap 421, interior nut 422, nozzle 423 and mixing cap 424, exterior nut cap 421 is fixedly connected with the external screw thread on the outer wall of one end (diagram right-hand member) of pure air fairlead 411 by the internal thread on its inwall, and communicates with the smoke evacuation tube chamber 131 of the aforementioned smoke exhaust pipe 13 of incinerator.Interior nut 422 is fixedly connected with the external screw thread on the outer wall of one end (diagram right-hand member) of compressed air fairlead 412 by the internal thread on its inwall.Mixing cap 424 is fixed with the outer wall of one end (illustrated right-hand member) of organic wastewater fairlead 413, and specifically, this mixing cap 424 is nested with in one end of organic wastewater fairlead 413.Nozzle 423 is limited to one end (diagram right-hand member) of compressed air fairlead 412 by aforesaid interior nut 422, and corresponding with mixing cap 424.
Shown in Fig. 2 and Fig. 3, be configured with a spout 4211 in the middle position of aforesaid exterior nut cap 421, this spout 4211 communicates with aforementioned smoke evacuation tube chamber 131.Former nozzle 423 is configured with spray orifice 4231, and spray orifice 4231 communicates with spout 4211, and communicates with mixing cap 424.The wall body of mixing cap 424 offers compressed air introduction hole 4241, and compressed air introduction hole 4241 communicates with compressed air fairlead tube chamber 4121.
Shown by Fig. 1 and Fig. 2, the pipeline of aforesaid pure air inlet tube 43 is equipped with pure air control valve 431; The pipeline of aforesaid compressed air inlet tube 43 is equipped with compressed air regulating valve 441; The pipeline of organic wastewater inlet tube 45 is equipped organic wastewater control valve 451.Control to adjust by the flow of pure air control valve 431 to the pure air introduced in pure air fairlead tube chamber 4111 by pure air inlet tube 43, by compressed air regulating valve 441 to by compressed air inlet tube 44, the compressed-air actuated flow introduced in compressed air fairlead tube chamber 4121 controls to adjust, controlled to adjust by the flow of organic wastewater control valve 451 to the organic wastewater introduced in organic wastewater fairlead tube chamber 4131 by organic wastewater inlet tube 45, make organic wastewater, compressed air and pure air three meet the atomization requirement entered in smoke evacuation tube chamber 131, in order to obtaining good evaporation, combustion efficiency.
Applicant sketches use of the present invention, open the valve on the pipeline of organic exhaust gas introducing interface 111, organic exhaust gas is made to enter in inlet plenum 11, start burner 112 to work, and lighted a fire by fire door 14, open pure air control valve 431, compressed air regulating valve 441 and organic wastewater control valve 451, organic exhaust gas is in burner hearth 12 combustion (burning), simultaneously be ejected to exterior nut cap 421 by compressed air and the mixed waste water aerosol of organic wastewater from spray orifice 4231 and pure air enters exterior nut cap 421 from pore 4113, be injected into smoke evacuation tube chamber 131 with the vaporific spout 4211 from exterior nut cap 421 after converging to evaporate, burning.The flue gas coming from smoke evacuation tube chamber 131 enters heat exchanger 2 and changes friendship cooling, then enters dust cleaning case 34 dedusting of dedusting mechanism 3, until arranged by pipeline by the exhaust smoke outlet of blower fan 33 outward.
In sum, technical scheme provided by the invention eliminates the deficiency in prior art, completes invention task, embodies the technique effect described in applicant.
Claims (8)
1. a waste gas, water incineration disposal device, comprise an incinerator (1), the top of this incinerator (1) is configured with an inlet plenum (11), the sidepiece of this inlet plenum (11) is provided with an organic exhaust gas and introduces interface (111), this organic exhaust gas is introduced interface (111) and is communicated with inlet plenum (11), a burner (112) is provided with at the top of inlet plenum (11), this burner (112) is insinuated in the burner hearth (12) of incinerator (1) after approach inlet plenum (11), one is connected for the smoke exhaust pipe (13) by the high-temperature flue gas extraction in burner hearth (12) in the bottom of incinerator (1), this smoke exhaust pipe (13) communicates with described burner hearth (12), and be provided with one in the following side of incinerator (1) for implementing clean fire door (14) to burner hearth (12), one heat exchanger (2) and a dedusting mechanism (3), heat exchanger (2) is with described incinerator (1), described smoke exhaust pipe (13) is connected with this heat exchanger (2), and dust-falling mechanism (3) is connected with heat exchanger (2) pipeline, for draining into the external world to the flue gas ash removal coming from heat exchanger (2) after dedusting, it is characterized in that: also include one for organic wastewater to be injected into the organic wastewater retraction mechanism (4) of evaporating in the smoke evacuation tube chamber (131) of described smoke exhaust pipe (13) with spray pattern, this organic wastewater retraction mechanism (4) is connected with smoke exhaust pipe (13) and is insinuated in described smoke evacuation tube chamber (131), described organic wastewater retraction mechanism (4) comprises spray gun (41), shower nozzle (42), pure air inlet tube (43), compressed air inlet tube (44) and organic wastewater inlet tube (45), spray gun (41) is fixed with described incinerator (1), and one end of this spray gun (41) is insinuated in described smoke evacuation tube chamber (131), shower nozzle (42) is positioned at smoke evacuation tube chamber (131) and fixes with described one end of spray gun (41), pure air inlet tube (43), compressed air inlet tube (44) is all connected with the other end of described spray gun (41) with organic wastewater inlet tube (45), and communicate with described shower nozzle (42), described spray gun (41) comprises pure air fairlead (411), compressed air fairlead (412) and organic wastewater fairlead (413), pure air fairlead (411) is fixed with described incinerator (1), one end of this pure air fairlead (411) is insinuated in the smoke evacuation tube chamber (131) of described smoke exhaust pipe (13), be connected with described shower nozzle (42) and communicate with shower nozzle (42), compressed air fairlead (412) is positioned at the pure air fairlead tube chamber (4111) of pure air fairlead (411), one end of this compressed air fairlead (412) is connected with shower nozzle (42) and communicates with shower nozzle (42), organic wastewater fairlead (413) is positioned at the compressed air fairlead tube chamber (4121) of compressed air fairlead (412), one end of this organic wastewater fairlead (413) is connected with shower nozzle (42) and communicates with shower nozzle (42), described pure air inlet tube (43) is connected with the other end of pure air fairlead (411), and communicate with pure air fairlead tube chamber (4111), described compressed air inlet tube (44) is connected with the other end of compressed air fairlead (412), and communicate with compressed air fairlead tube chamber (4121), described organic wastewater inlet tube (45) is connected with the other end of organic wastewater fairlead (413), and communicate with the organic wastewater fairlead tube chamber (4131) of organic wastewater fairlead (413).
2. waste gas according to claim 1, water incineration disposal device, it is characterized in that described shower nozzle (42) comprises exterior nut cap (421), interior nut (422), nozzle (423) and mixing cap (424), exterior nut cap (421) is fixed with the outer wall of described one end of described pure air fairlead (411), and communicate with the smoke evacuation tube chamber (131) of the described smoke exhaust pipe (13) of described incinerator (1), interior nut (422) is fixed with the outer wall of described one end of described compressed air fairlead (412), mixing cap (424) is fixed with the outer wall of described one end of described organic wastewater fairlead (413), nozzle (423) is fixed on described one end of compressed air fairlead (412) by interior nut (422), and it is corresponding with mixing cap (424), described pure air fairlead tube chamber (4111) communicates with described exterior nut cap (421), described compressed air fairlead tube chamber (4121) communicates with mixing cap (424), described organic wastewater fairlead tube chamber (4131) communicates with mixing cap (424), and mix cap (424) and communicate with nozzle (423).
3. waste gas according to claim 2, water incineration disposal device, it is characterized in that being configured with a spout (4211) in the middle position of described exterior nut cap (421), this spout (4211) communicates with the smoke evacuation tube chamber (131) of described smoke exhaust pipe (13), described nozzle (423) is configured with spray orifice (4231), spray orifice (4231) communicates with spout (4211), and communicate with described mixing cap (424), the wall body of mixing cap (424) offers compressed air introduction hole (4241), this compressed air introduction hole (4241) communicates with described compressed air fairlead tube chamber (4121).
4. waste gas according to claim 1 and 2, water incineration disposal device, it is characterized in that being fixed with a spray gun mounting flange (4112) on the outer wall of described pure air fairlead (411), this spray gun mounting flange (4112) is fixed with described incinerator (1).
5. waste gas according to claim 1, water incineration disposal device, is characterized in that being equipped with pure air control valve (431) on the pipeline of described pure air inlet tube (43); The pipeline of described compressed air inlet tube (43) is equipped with compressed air regulating valve (441); The pipeline of described organic wastewater inlet tube (45) is equipped with organic wastewater control valve (451).
6. waste gas according to claim 1, water incineration disposal device, is characterized in that described heat exchanger (2) is tubular heat exchanger or tube coil type heat exchanger.
7. waste gas according to claim 1, water incineration disposal device, it is characterized in that described dedusting mechanism (3) comprises support (31), motor (32), blower fan (33) and dust cleaning case (34), support (31) is bearing on the terrace of field of employment, motor (32) and blower fan (33) connect, and be fixed on support (31) by blower fan (33) together with motor (32), the flue gas mouth (331) that enters of this blower fan (33) is connected with dust cleaning case (34), and the exhaust smoke outlet (332) of blower fan (33) is communicated with the external world by pipeline, dust cleaning case (34) is fixed on support (31), described heat exchanger (2) is positioned between described incinerator (1) and support (31).
8. the waste gas according to claim 1 or 7, water incineration disposal device, is characterized in that being provided with heat-insulation layer (15) on the outer wall of described incinerator (1).
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| Application Number | Priority Date | Filing Date | Title |
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| CN201310033412.0A CN103090400B (en) | 2013-01-29 | 2013-01-29 | Waste gas and water incineration disposal device |
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| CN201310033412.0A CN103090400B (en) | 2013-01-29 | 2013-01-29 | Waste gas and water incineration disposal device |
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| CN103090400A CN103090400A (en) | 2013-05-08 |
| CN103090400B true CN103090400B (en) | 2015-02-11 |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN103411225A (en) * | 2013-06-09 | 2013-11-27 | 无锡华光锅炉股份有限公司 | Landfill leachate spray combustion device |
| CN109631054B (en) * | 2018-11-01 | 2020-07-28 | 扬州链享环保工程技术有限公司 | Combustion control system of sulfur-containing waste liquid incinerator |
| CN110631033B (en) * | 2019-10-12 | 2024-08-27 | 亚德（上海）环保系统有限公司 | Waste gas incineration oxidation furnace |
| CN116498973B (en) * | 2023-07-03 | 2023-09-22 | 浙江百能科技有限公司 | PTA byproduct solid and liquid waste mixed incineration treatment system |
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