CN204345652U - A kind of industrial hazardous waste incineration system - Google Patents
A kind of industrial hazardous waste incineration system Download PDFInfo
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- CN204345652U CN204345652U CN201420801277.XU CN201420801277U CN204345652U CN 204345652 U CN204345652 U CN 204345652U CN 201420801277 U CN201420801277 U CN 201420801277U CN 204345652 U CN204345652 U CN 204345652U
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Abstract
The utility model discloses a kind of industrial hazardous waste incineration system, comprise rotary kiln, waste liquid stove, membranous wall formula sedimentation furnace, membranous wall formula waste heat boiler, half-dried quench tower, dry type reactor, sack cleaner, air-introduced machine, spray column, absorption tower, gas pipeline, low pressure steam line, compressed air line and chimney, secondary combustion chamber and fore-cooling room is also provided with between waste liquid stove and membranous wall formula sedimentation furnace, this industrial hazardous waste incineration system, this industrial hazardous waste incineration system not only structure is simple, easy to operate, cost is low, long service life, and to danger wastes Thorough combustion, greatly reduce harmfulness, and operating efficiency is high, simultaneously independent solid-state and liquid state can be processed, highly versatile, operating efficiency is high, reduce costs.
Description
Technical field
The utility model relates to waste incineration system, specifically a kind of industrial hazardous waste incineration system.
Background technology
Along with the development of society, solid-state castoff product in industrial production and liquid waste gas article get more and more, hazardous waste not only has the long-term pollution to environment, and there is the harmfulness such as inflammable, explosive, poisonous, burn into infection, existing many means of planting process discarded object, generally adopt the method for high-temp combustion at present, but in processing procedure, still there is burning insufficient, process incomplete problem, cause the pollution to environment; And the problems such as it is short that treatment facility exists service life, and cost is high, inefficiency; Domesticly choose the main force type of furnace one of of rotary kiln type incinerator as dangerous waste incineration, be particularly useful for commercialization and focus on CIU, rotary kiln incineration has the features such as highly versatile, but uses the problem of still Shortcomings to it.
Utility model content
Technical problem to be solved in the utility model is, for the shortcoming of above prior art, proposes a kind of industrial hazardous waste incineration system, this industrial hazardous waste incineration system not only structure is simple, and easy to operate, cost is low, long service life, and to danger wastes Thorough combustion, greatly reduce harmfulness, and operating efficiency is high, simultaneously independent solid-state and liquid state can be processed, highly versatile, operating efficiency is high, reduces costs.
In order to solve the problems of the technologies described above, the technical solution of the utility model is achieved in the following ways: a kind of industrial hazardous waste incineration system, comprise rotary kiln, waste liquid stove, membranous wall formula sedimentation furnace, membranous wall formula waste heat boiler, half-dried quench tower, dry type reactor, sack cleaner, air-introduced machine, spray column, absorption tower, gas pipeline, low pressure steam line, compressed air line and chimney, between waste liquid stove and membranous wall formula sedimentation furnace, be also provided with secondary combustion chamber and fore-cooling room;
Rotary kiln one end is provided with feed arrangement, the other end is communicated with waste liquid stove by flue tube, rotary kiln is also provided with ash hole near waste liquid stove one end, feed arrangement comprises lifting charging device and hydraulic pressure closed-type feed device composition, lifting charging device comprises guide rail and is arranged on the feeding vehicle on guide rail, hydraulic pressure closed-type feed device comprises feed hopper, the transport tube being arranged on feed hopper lower end and the piston rod be horizontally set on transport tube, the first Imported gas and start-up burner is also provided with near one end of hydraulic pressure closed-type feed device at rotary kiln, feeding vehicle can move and send in feed hopper by solid waste on guide rail, first Imported gas is communicated with gas pipeline,
Waste liquid furnace upper end is provided with and liquid waste import, liquid waste import is connected with liquid feeding device, liquid feeding device comprises liquid storage tank and two delivery pumps be arranged in parallel, by delivery pump by the Liquid transfer in liquid storage tank in waste liquid stove, all be communicated with low pressure steam line at the import and export of delivery pump, between delivery pump outlet and low pressure steam line, be also provided with a branch road be back in liquid storage tank;
The bottom of waste liquid stove is provided with the two rod slag extractor of water-cooled for getting rid of inner waste residue, waste liquid furnace sidewall is also provided be communicated with gas pipeline the second Imported gas, exhaust gas inlet and combustion adjuvant import;
The upper end of waste liquid stove is communicated with secondary combustion chamber one end, the secondary combustion chamber other end is communicated with fore-cooling room, also be connected with denitrification apparatus at secondary combustion chamber, denitrification apparatus comprises urea liquid storage tank, urea solution metering pump, electric heater, dilution water measuring pump and blender, urea liquid storage tank is connected with urea solution metering pump inlet, urea solution metering pump discharge is connected with electric heater, electric heater is connected with blender import, mixer outlet is connected with secondary combustion chamber, be connected with also exporting with dilution water measuring pump between blender import in electric heater outlet, the pipeline be communicated with gas pipeline is also provided with in secondary combustion chamber,
Fore-cooling room is connected with membranous wall formula sedimentation furnace, fore-cooling room is also communicated with the cooling storage tank of outside, outside boiler water is communicated with cooling storage tank with high steam, cooling storage tank is communicated with membranous wall formula sedimentation furnace with fore-cooling room, membranous wall formula sedimentation furnace lower end is connected with membranous wall formula waste heat boiler, the exhanst gas outlet of membranous wall formula waste heat boiler upper end is connected with half-dried quench tower, and membranous wall formula sedimentation furnace and membranous wall formula waste heat boiler lower end are equipped with waste residue scavenge port;
The top of half-dried quench tower inside is provided with atomizer, atomizer is also connected with compression blank pipe road, atomizer is connected with the circulatory pool being arranged on outside, the outlet of half-dried quench tower lower end is connected with dry type reactor, also be communicated with high pressure roots blower fan with the rock lime storage tank being arranged on outside in dry type reactor, the outlet of dry type reactor is connected with sack cleaner, sack cleaner is connected with outside compressed air line, sack cleaner lower end is also provided with waste residue scavenge port, sack cleaner upper end is communicated with air-introduced machine, air-introduced machine is communicated with spray column, spray column and absorption tower are connected in series, absorption tower is connected with chimney, the sidewall of spray column with absorption tower is equipped with the shower nozzle be communicated with circulatory pool.
Like this, this industrial hazardous waste incineration system not only structure is simple, easy to operate, cost is low, long service life, liquid waste device is set, solid waste device and exhaust gas inlet, meet different duty requirements, improve its operating efficiency, delivery pump a preparation and a use in parallel is adopted in liquid feeding device, facilitate inspection and maintenance, flexible and convenient operation, operating efficiency is high, and in waste liquid stove, adopt shower nozzle, increase its atomizing effect, improve the contact area of liquid waste thing and natural gas, can Thorough combustion, reach smokeless, odorless, the effect of non-secondary pollution, flue gas is in waste liquid stove, make the micro-content organism in flue gas Ji bioxin is able to abundant decomposition, decomposition efficiency is more than 99.99%, guarantee that in flue gas, undecomposed organic principle and carbon granule decompose completely, reduce and pollute, and in secondary combustion chamber, be provided with denitrification apparatus, spray into the reaction of nitrogen oxides in appropriate solution and flue gas, conversion of nitrogen oxides is made to be nitrogen and water,
Atomizer is provided with in half-dried quench tower, alkaline solution can be become trickle droplet by nozzle atomization, the alkali lye droplet be atomized is by heat smoke effect upwards, and near nozzle, form the high-density region that an alkaline droplet suspends, the acidic materials in flue gas, through during this region, neutralization reaction occur.By regulating alkali lye amount carry out control temperature thus restrained effectively the regeneration of bioxin, the water smoke that some Mars simultaneously in flue gas are injected into extinguishes, and protects follow-up cloth bag not to be burned;
Rock lime storage tank is connected in dry type reactor, in rock lime storage tank, mixture is purged by high pressure roots blower fan, enter and connect flue and incineration tail gas and react, further cleaning of off-gas, spray into charcoal lime (mixture of calcium oxide powder and activated carbon powder) to remove and absorb the acid ingredient such as bioxin and SOx, HF, HCl, NOx in flue gas, and gas enters sack cleaner, remove the fine solid particle be detained in flue gas.The charcoal lime of jetting in pipeline enters sack cleaner, is adsorbed on cloth bag, and fully the charcoal lime of reactive adsorption does not continue to absorb, react, and guarantees to react completely; And be provided with spray column and absorption tower removes the hydrochloric acid gas in flue gas and the SO in flue gas respectively
2deng other sour gas, purify up to standard after flue gas be discharged in air by chimney.
The technical scheme that the utility model limits further is:
Aforesaid industrial hazardous waste incineration system, in the exit of dry type reactor, a branch road in parallel with sack cleaner is directly communicated with air-introduced machine, be provided with by-pass flue, sack cleaner inlet temperature not in limits time, cloth bag bypass three-way electromagnetic valve is opened, and flue gas enters chimney by bypass, does not form fatal damages when guaranteeing cigarette temperature abnormality to cloth bag, in the service life of raising equipment, reduce costs.
Aforesaid industrial hazardous waste incineration system, is also provided with detection mouth in the upper end of chimney, facilitates staff to detect, and guarantees that flue gas is discharged in air after up to standard constantly.
Aforesaid industrial hazardous waste incineration system, stores alkaline solution in circulatory pool, carries out acid-base neutralization by alkaline solution, the sour gas in removing smoke.
Aforesaid industrial hazardous waste incineration system, is provided with at the two ends of rotary kiln and is equipped with air blast, impel sufficient combustion by air blast, improves efficiency of combustion.
The beneficial effects of the utility model are: this industrial hazardous waste incineration system not only structure is simple, easy to operate, cost is low, long service life, liquid waste device is set, solid waste device and exhaust gas inlet, meet different duty requirements, improve its operating efficiency, delivery pump a preparation and a use in parallel is adopted in liquid feeding device, facilitate inspection and maintenance, flexible and convenient operation, operating efficiency is high, and in waste liquid stove, adopt shower nozzle, increase its atomizing effect, improve the contact area of liquid waste thing and natural gas, can Thorough combustion, reach smokeless, odorless, the effect of non-secondary pollution, flue gas is in waste liquid stove, make the micro-content organism in flue gas Ji bioxin is able to abundant decomposition, decomposition efficiency is more than 99.99%, guarantee that in flue gas, undecomposed organic principle and carbon granule decompose completely, reduce and pollute, and in secondary combustion chamber, be provided with denitrification apparatus, spray into the reaction of nitrogen oxides in appropriate solution and flue gas, conversion of nitrogen oxides is made to be nitrogen and water,
Atomizer is provided with in half-dried quench tower, alkaline solution can be become trickle droplet by nozzle atomization, the alkali lye droplet be atomized is by heat smoke effect upwards, and near nozzle, form the high-density region that an alkaline droplet suspends, the acidic materials in flue gas, through during this region, neutralization reaction occur.By regulating alkali lye amount carry out control temperature thus restrained effectively the regeneration of bioxin, the water smoke that some Mars simultaneously in flue gas are injected into extinguishes, and protects follow-up cloth bag not to be burned;
Rock lime storage tank is connected in dry type reactor, in rock lime storage tank, mixture is purged by high pressure roots blower fan, enter and connect flue and incineration tail gas and react, further cleaning of off-gas, spray into charcoal lime (mixture of calcium oxide powder and activated carbon powder) to remove and absorb the acid ingredient such as bioxin and SOx, HF, HCl, NOx in flue gas, and gas enters sack cleaner, remove the fine solid particle be detained in flue gas.The charcoal lime of jetting in pipeline enters sack cleaner, is adsorbed on cloth bag, and fully the charcoal lime of reactive adsorption does not continue to absorb, react, and guarantees to react completely; And be provided with spray column and absorption tower removes the hydrochloric acid gas in flue gas and the SO in flue gas respectively
2deng other sour gas, purify up to standard after flue gas be discharged in air by chimney.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model;
Fig. 2 is the structural representation of rotary kiln feed arrangement in the utility model;
Fig. 3 is the feed arrangement structural representation of liquid waste in the utility model;
Fig. 4 is the structural representation of waste liquid stove in the utility model;
Fig. 5 is the structural representation of denitrification apparatus in the utility model;
Fig. 6 is the structural representation of membranous wall formula sedimentation furnace and membranous wall formula waste heat boiler in the utility model;
Fig. 7 is the structural representation of dry type reactor and sack cleaner in the utility model;
Wherein: 1-rotary kiln, 2-waste liquid stove, 3-membranous wall formula sedimentation furnace, 4-membranous wall formula waste heat boiler, the half-dried quench tower of 5-, 6-dry type reactor, 7-sack cleaner, 8-air-introduced machine, 9-spray column, 10-absorption tower, 11-secondary combustion chamber, 12-fore-cooling room, 13-ash hole, 14-guide rail, 15-feeding vehicle, 16-feed hopper, 17-transport tube, 18-piston rod, 19-first Imported gas, 20-start-up burner, the import of 21-liquid waste, 22-liquid storage tank, 23-delivery pump, 24-gas pipeline, 25-low pressure steam line, 26-branch road, 27-second Imported gas, 28-exhaust gas inlet, the import of 29-combustion adjuvant, 30-urea liquid storage tank, 31-urea solution metering pump, 32-electric heater, 33-dilution water measuring pump, 34-blender, 35-cools storage tank, 36-exhanst gas outlet, 37-waste residue scavenge port, 38-atomizer, 39-circulatory pool, 40-high pressure roots blower fan, 41-shower nozzle, 42-detects mouth, 43-air blast, the two rod slag extractor of 44-water-cooled, 45-compresses blank pipe road, 46-rock lime storage tank, 47-chimney.
Detailed description of the invention
Below the utility model is described in further detail:
embodiment 1
The present embodiment provides a kind of industrial hazardous waste incineration system, comprise rotary kiln 1, waste liquid stove 2, membranous wall formula sedimentation furnace 3, membranous wall formula waste heat boiler 4, half-dried quench tower 5, dry type reactor 6, sack cleaner 7, air-introduced machine 8, spray column 9, absorption tower 10, gas pipeline 24, low pressure steam line 25, compressed air line 45 and chimney 47, between waste liquid stove 2 and membranous wall formula sedimentation furnace 3, be also provided with secondary combustion chamber 11 and fore-cooling room 12;
Rotary kiln 1 one end is provided with feed arrangement, the other end is communicated with waste liquid stove 2 by flue tube, rotary kiln 1 is also provided with ash hole 13 near waste liquid stove 2 one end, feed arrangement comprises lifting charging device and hydraulic pressure closed-type feed device composition, the feeding vehicle 15 that lifting charging device comprises guide rail 14 and is arranged on guide rail 14, hydraulic pressure closed-type feed device comprises feed hopper 16, the transport tube 17 being arranged on feed hopper 16 lower end and the piston rod 18 be horizontally set on transport tube 17, the first Imported gas 19 and start-up burner 20 is also provided with near one end of hydraulic pressure closed-type feed device at rotary kiln 1, feeding vehicle 15 can move and be sent into by solid waste in feed hopper 16 on guide rail 14, first Imported gas 19 is communicated with gas pipeline 24,
Waste liquid stove 2 upper end is provided with and liquid waste import 21, liquid waste import 21 is connected with liquid feeding device, liquid feeding device comprises liquid storage tank 22 and two delivery pumps be arranged in parallel 23, by delivery pump 23 by the Liquid transfer in liquid storage tank 22 in waste liquid stove 2, all be communicated with low pressure steam line 25 at the import and export of delivery pump 23, be also provided with a branch road 26 be back in liquid storage tank 22 exporting at delivery pump 23 between low pressure steam line 25;
The bottom of waste liquid stove 2 is provided with the two rod slag extractor 44 of water-cooled for getting rid of inner waste residue, waste liquid stove 2 sidewall is also provided be communicated with gas pipeline 24 the second Imported gas 27, exhaust gas inlet 28 and combustion adjuvant import 29;
The upper end of waste liquid stove 2 is communicated with secondary combustion chamber 11 one end, secondary combustion chamber 11 other end is communicated with fore-cooling room 12, also be connected with denitrification apparatus at secondary combustion chamber 11, denitrification apparatus comprises urea liquid storage tank 30, urea solution metering pump 31, electric heater 32, dilution water measuring pump 33 and blender 34, urea liquid storage tank 30 is connected with urea solution metering pump 31 import, urea solution metering pump 31 outlet is connected with electric heater 32, electric heater 32 is connected with blender 34 import, blender 34 outlet is connected with secondary combustion chamber 11, export also to export with dilution water measuring pump 33 between blender 34 import at electric heater 32 and be connected, the pipeline be communicated with gas pipeline 24 is also provided with in secondary combustion chamber 11,
Fore-cooling room 12 is connected with membranous wall formula sedimentation furnace 3, fore-cooling room 12 is also communicated with the cooling storage tank 35 of outside, outside boiler water is communicated with cooling storage tank 35 with high steam, cooling storage tank 35 is communicated with membranous wall formula sedimentation furnace 3 with fore-cooling room 12, membranous wall formula sedimentation furnace 3 lower end is connected with membranous wall formula waste heat boiler 4, the exhanst gas outlet 36 of membranous wall formula waste heat boiler 4 upper end is connected with half-dried quench tower 5, and membranous wall formula sedimentation furnace 3 and membranous wall formula waste heat boiler 4 lower end are equipped with waste residue scavenge port 37;
The top of half-dried quench tower 5 inside is provided with atomizer 38, atomizer 38 is also connected with compression blank pipe road 45, atomizer 38 is connected with the circulatory pool 39 being arranged on outside, the outlet of half-dried quench tower 5 lower end is connected with dry type reactor 6, also be communicated with high pressure roots blower fan 40 with the rock lime storage tank 46 being arranged on outside in dry type reactor 6, the outlet of dry type reactor 6 is connected with sack cleaner 7, sack cleaner 7 is connected with outside compressed air line 45, sack cleaner 7 lower end is also provided with waste residue scavenge port 37, sack cleaner 7 upper end is communicated with air-introduced machine 8, air-introduced machine 8 is communicated with spray column 9, spray column 9 and absorption tower 10 are connected in series, absorption tower 10 is connected with chimney 47, the sidewall of spray column 9 with absorption tower 10 is equipped with the shower nozzle 41 be communicated with circulatory pool 39.
In the exit of dry type reactor 6, a branch road in parallel with sack cleaner 7 is directly communicated with air-introduced machine 8, be provided with by-pass flue, sack cleaner inlet temperature not in limits time, cloth bag bypass three-way electromagnetic valve is opened, flue gas enters chimney by bypass, fatal damages is not formed to cloth bag when guaranteeing cigarette temperature abnormality, improve the service life of equipment, reduce costs; Also be provided with in the upper end of chimney 47 and detect mouth 42, facilitate staff to detect, guarantee that flue gas is discharged in air after up to standard constantly; Store alkaline solution in circulatory pool 39, carry out acid-base neutralization by alkaline solution, the sour gas in removing smoke; Be provided with at the two ends of rotary kiln 1 and be equipped with air blast 43, impel sufficient combustion by air blast, improve efficiency of combustion.
Like this by the technical scheme of embodiment, this industrial hazardous waste incineration system not only structure is simple, and easy to operate, cost is low, long service life, and to danger wastes Thorough combustion, greatly reduce harmfulness, and operating efficiency is high, simultaneously independent solid-state and liquid state can be processed, highly versatile, operating efficiency is high, reduces costs.
Above embodiment is only and technological thought of the present utility model is described; protection domain of the present utility model can not be limited with this; every technological thought according to the utility model proposes, any change that technical scheme basis is done, all falls within the utility model protection domain.
Claims (5)
1. an industrial hazardous waste incineration system, it is characterized in that: comprise rotary kiln (1), waste liquid stove (2), membranous wall formula sedimentation furnace (3), membranous wall formula waste heat boiler (4), half-dried quench tower (5), dry type reactor (6), sack cleaner (7), air-introduced machine (8), spray column (9), absorption tower (10), gas pipeline (24), low pressure steam line (25), compressed air line (45) and chimney (47), between described waste liquid stove (2) and membranous wall formula sedimentation furnace (3), be also provided with secondary combustion chamber (11) and fore-cooling room (12);
Described rotary kiln (1) one end is provided with feed arrangement, the other end is communicated with waste liquid stove (2) by flue tube, described rotary kiln (1) is also provided with ash hole (13) near waste liquid stove (2) one end, described feed arrangement comprises lifting charging device and hydraulic pressure closed-type feed device composition, described lifting charging device comprises guide rail (14) and is arranged on the feeding vehicle (15) on guide rail (14), described hydraulic pressure closed-type feed device comprises feed hopper (16), the transport tube (17) being arranged on feed hopper (16) lower end and the piston rod (18) be horizontally set on transport tube (17), the first Imported gas (19) and start-up burner (20) is also provided with near one end of hydraulic pressure closed-type feed device at described rotary kiln (1), described feeding vehicle (15) can above move at guide rail (14) and be sent into by solid waste in feed hopper (16), described first Imported gas (19) is communicated with gas pipeline (24),
Described waste liquid stove (2) upper end is provided with and liquid waste import (21), described liquid waste import (21) is connected with liquid feeding device, described liquid feeding device comprises liquid storage tank (22) and two delivery pumps be arranged in parallel (23), by delivery pump (23) by the Liquid transfer in liquid storage tank (22) in waste liquid stove (2), all be communicated with low pressure steam line (25) at the import and export of described delivery pump (23), be arranged in described delivery pump (23) outlet with low pressure steam line (25) between be also provided with the branch road (26) that is back to liquid storage tank (22),
The bottom of described waste liquid stove (2) is provided with the two rod slag extractor (44) of water-cooled for getting rid of inner waste residue, described waste liquid stove (2) sidewall is also provided be communicated with gas pipeline (24) the second Imported gas (27), exhaust gas inlet (28) and combustion adjuvant import (29);
The upper end of described waste liquid stove (2) is communicated with secondary combustion chamber (11) one end, described secondary combustion chamber (11) other end is communicated with fore-cooling room (12), also be connected with denitrification apparatus at described secondary combustion chamber (11), described denitrification apparatus comprises urea liquid storage tank (30), urea solution metering pump (31), electric heater (32), dilution water measuring pump (33) and blender (34), described urea liquid storage tank (30) is connected with urea solution metering pump (31) import, urea solution metering pump (31) outlet is connected with electric heater (32), electric heater (32) is connected with blender (34) import, blender (34) outlet is connected with secondary combustion chamber (11), be connected with also exporting with dilution water measuring pump (33) between blender (34) import in described electric heater (32) outlet, the pipeline be communicated with gas pipeline (24) is also provided with in described secondary combustion chamber (11),
Described fore-cooling room (12) is connected with membranous wall formula sedimentation furnace (3), described fore-cooling room (12) is also communicated with the cooling storage tank (35) of outside, the boiler water of described outside is communicated with cooling storage tank (35) with high steam, described cooling storage tank (35) is communicated with membranous wall formula sedimentation furnace (3) with fore-cooling room (12), described membranous wall formula sedimentation furnace (3) lower end is connected with membranous wall formula waste heat boiler (4), the exhanst gas outlet (36) of described membranous wall formula waste heat boiler (4) upper end is connected with half-dried quench tower (5), described membranous wall formula sedimentation furnace (3) and membranous wall formula waste heat boiler (4) lower end are equipped with waste residue scavenge port (37),
The top that described half-dried quench tower (5) is inner is provided with atomizer (38), described atomizer (38) is also connected with compression blank pipe road (45), described atomizer (38) is connected with the circulatory pool (39) being arranged on outside, the outlet of described half-dried quench tower (5) lower end is connected with dry type reactor (6), also be communicated with high pressure roots blower fan (40) with the rock lime storage tank (46) being arranged on outside in described dry type reactor (6), the outlet of described dry type reactor (6) is connected with sack cleaner (7), described sack cleaner (7) is connected with outside compressed air line (45), sack cleaner (7) lower end is also provided with waste residue scavenge port (37), described sack cleaner (7) upper end is communicated with air-introduced machine (8), described air-introduced machine (8) is communicated with spray column (9), described spray column (9) and absorption tower (10) are connected in series, described absorption tower (10) is connected with chimney (47), described spray column (9) with the sidewall of absorption tower (10) are equipped with the shower nozzle (41) be communicated with circulatory pool (39).
2. industrial hazardous waste incineration system according to claim 1, is characterized in that: in the exit of described dry type reactor (6), a branch road in parallel with sack cleaner (7) is directly communicated with air-introduced machine (8).
3. industrial hazardous waste incineration system according to claim 1, is characterized in that: be also provided with in the upper end of described chimney (47) and detect mouth (42).
4. industrial hazardous waste incineration system according to claim 1, is characterized in that: described circulatory pool stores alkaline solution in (39).
5. industrial hazardous waste incineration system according to claim 1, is characterized in that: be provided with at the two ends of described rotary kiln (1) and be equipped with air blast (43).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420801277.XU CN204345652U (en) | 2014-12-16 | 2014-12-16 | A kind of industrial hazardous waste incineration system |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201420801277.XU CN204345652U (en) | 2014-12-16 | 2014-12-16 | A kind of industrial hazardous waste incineration system |
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| CN204345652U true CN204345652U (en) | 2015-05-20 |
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| CN201420801277.XU Expired - Fee Related CN204345652U (en) | 2014-12-16 | 2014-12-16 | A kind of industrial hazardous waste incineration system |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104501178A (en) * | 2014-12-16 | 2015-04-08 | 江苏百茂源环保科技有限公司 | Industrial hazardous waste incineration system |
| CN106594741A (en) * | 2016-11-18 | 2017-04-26 | 四川九洲环保科技有限责任公司 | Combustion chamber |
| CN106678808A (en) * | 2016-11-18 | 2017-05-17 | 四川九洲环保科技有限责任公司 | Incineration system |
| CN112984511A (en) * | 2021-01-29 | 2021-06-18 | 苏州乔发环保科技股份有限公司 | Useless treatment facility of retort danger |
-
2014
- 2014-12-16 CN CN201420801277.XU patent/CN204345652U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104501178A (en) * | 2014-12-16 | 2015-04-08 | 江苏百茂源环保科技有限公司 | Industrial hazardous waste incineration system |
| CN106594741A (en) * | 2016-11-18 | 2017-04-26 | 四川九洲环保科技有限责任公司 | Combustion chamber |
| CN106678808A (en) * | 2016-11-18 | 2017-05-17 | 四川九洲环保科技有限责任公司 | Incineration system |
| CN106678808B (en) * | 2016-11-18 | 2018-06-15 | 四川九洲环保科技有限责任公司 | A kind of incineration system |
| CN112984511A (en) * | 2021-01-29 | 2021-06-18 | 苏州乔发环保科技股份有限公司 | Useless treatment facility of retort danger |
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