CN103868076A - Gas waste, liquid waste and solid waste integrated incinerator - Google Patents
Gas waste, liquid waste and solid waste integrated incinerator Download PDFInfo
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- CN103868076A CN103868076A CN201410139257.5A CN201410139257A CN103868076A CN 103868076 A CN103868076 A CN 103868076A CN 201410139257 A CN201410139257 A CN 201410139257A CN 103868076 A CN103868076 A CN 103868076A
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- 239000002699 waste material Substances 0.000 title claims abstract description 48
- 239000002910 solid waste Substances 0.000 title claims abstract description 11
- 239000010808 liquid waste Substances 0.000 title abstract description 14
- 238000002485 combustion reaction Methods 0.000 claims abstract description 46
- 239000007788 liquid Substances 0.000 claims abstract description 35
- 239000007789 gas Substances 0.000 claims abstract description 11
- 239000002893 slag Substances 0.000 claims abstract description 10
- 239000007787 solid Substances 0.000 claims description 35
- 239000000463 material Substances 0.000 claims description 32
- 239000002912 waste gas Substances 0.000 claims description 22
- 239000002184 metal Substances 0.000 claims description 16
- 239000000428 dust Substances 0.000 claims description 15
- 239000000203 mixture Substances 0.000 claims description 9
- 238000005507 spraying Methods 0.000 claims description 8
- 238000009413 insulation Methods 0.000 claims description 7
- 230000001174 ascending effect Effects 0.000 claims description 6
- 238000001816 cooling Methods 0.000 claims description 6
- 238000009423 ventilation Methods 0.000 claims description 4
- 238000006243 chemical reaction Methods 0.000 claims description 3
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- 150000003839 salts Chemical group 0.000 abstract description 11
- 239000000126 substance Substances 0.000 abstract description 9
- 238000005516 engineering process Methods 0.000 abstract description 8
- 238000004519 manufacturing process Methods 0.000 abstract description 6
- 238000000926 separation method Methods 0.000 abstract description 4
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- 238000001694 spray drying Methods 0.000 abstract 3
- 238000004056 waste incineration Methods 0.000 abstract 1
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- 239000003905 agrochemical Substances 0.000 description 6
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- 230000003116 impacting effect Effects 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
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- Incineration Of Waste (AREA)
Abstract
The invention discloses a gas waste, liquid waste and solid waste integrated incinerator which comprises a primary combustion chamber, a spray drying system arranged in the primary combustion chamber, a beam type chain fire grate arranged at the bottom of the primary combustion chamber, a water cooled slag removing machine, a cyclone separator and a secondary combustion chamber. The spray drying system comprises a plurality of primary combustion chamber combustors, a plurality of gas waste nozzles and a plurality of liquid waste nozzles, wherein the primary combustion chamber combustors, the gas waste nozzles and the liquid waste nozzles arranged on the inner wall of the primary combustion chamber in a layered mode. The cyclone separator is communicated with a gas waste outlet in the upper end of the primary combustion chamber through a pipe. The secondary combustion chamber is communicated with a gas outlet of the cyclone separator through a pipe. The spray drying and cyclone separation technology is adopted in the chemical salt bearing liquid waste incinerator, a unified waste disposal mode is broken through, simultaneous efficient incineration disposal of liquid, gas and solid waste can be achieved, and the gas waste, liquid waste and solid waste integrated incinerator has the advantages of being simple in manufacturing process, convenient to maintain, safe and stable to run and the like, and is suitable for being popularized and used in the field of salt bearing liquid waste incineration disposal.
Description
Technical field
The present invention relates to a kind of " three wastes " integrated incinerator that chemical industry salt bearing liquid wastes, useless solid and waste gas is carried out to innoxious, minimizing, recycling treatment.
Background technology
In the production process of the industries such as petrochemical industry, oil refining, pharmacy, agricultural chemicals, printing and dyeing and food; often have the generation of some high-risk waste gas and high saliferous (being mainly alkaline metal salt) organic liquid waste, useless solid, waste gas; for avoiding health and the natural environment of these high-risk pollutants to the mankind to threaten, need to carry out innoxious, minimizing and recycling treatment to it.Due to high saliferous, the high toxicity of these discarded objects cause it almost can not be by biochemical treatment, thereby find a kind of rationally, effective incineration treatment technology, thereby reduce the pollution of this discarded object to environment, promote that industry sustainable development is significant.
At present, extensively adopt incineration technology to process high concentrated organic waste liquid in industries such as petrochemical industry, oil refining, pharmacy, agricultural chemicals, printing and dyeing and food both at home and abroad, incinerator is using fuel oil or natural gas as auxiliary fuel, and part incinerator is also using enterprise's high heating value waste gas as auxiliary fuel.Tradition incinerator combustion system is single, can only simply process single discarded object.Especially aspect high organic waste liquid containing salt burning processing, in traditional incinerator stove, temperature is wayward, burns insufficient, without internal dust-removing device for furnace, the alkaline metal salt that contains a large amount of low melting points in the flue gas that burning produces, serious to tail flue gas cooling device and flue blockage, environmental protection is difficult to up to standard.
Summary of the invention
The present invention is directed to above-mentioned technical problem, propose a kind of waste gas, waste liquid, useless solid " three wastes " integrated incinerator based on employing crossbeam type chain-grate, spray dry and Cyclone Separation Technology.
For reaching above object, be achieved through the following technical solutions:
A kind of waste gas, waste liquid, useless solid " three wastes " integrated incinerator, comprise: primary zone, the spraying that is arranged at primary combustion chamber interior is dried system, is arranged at the crossbeam type chain-grate of bottom, primary zone, water-cooled slag remover, cyclone separator and secondary combustion chamber;
The dry system of spraying, comprising: layering is arranged at some primary zones burner, exhaust nozzle and the waste liquid spout of primary combustion chamber interior walls;
Exhaust nozzle and waste liquid spout are arranged between every adjacent two layers primary zone burner, and exhaust nozzle and waste liquid spout are for distributing alternately;
Bottom, primary zone is provided with horizontal chamber, and is provided with crossbeam type chain-grate in horizontal chamber;
Crossbeam type chain-grate top is provided with primary zone's burner;
Crossbeam type chain-grate end is provided with the water-cooled slag remover for solidfied material after cooling and conveying reaction;
Crossbeam type chain-grate comprise front end be provided with solid waste feed hopper, with gear-driven front axle, with compositions such as the air compartments of gear-driven rear axle, chain, fire grate segment, multiple isobaric balanced ventilations, front axle or rear axle all can be arranged decelerator, drag fire grate by electric machine rotation and move backward from front axle, solid waste is carried out high-temp combustion with the air that the multiple isobaric air compartments in fire grate bottom are evenly sent here on fire grate;
Cyclone separator is communicated with the waste gas outlet of upper end, primary zone by pipeline;
Cyclone separator separates solidfied material and exports the material returning device being provided with primary zone's internal communication;
Material returning device inside is as " U " container, one side is dipleg, be cyclone separator bottom cone section and material returning device connecting portion, opposite side is feed pipe, like " L " type, one end is connected with material returning device, the other end connects and is connected with primary zone, material returning device bottom is furnished with loose metal wind ascending pipe near dipleg end, the pressure head of loose metal wind is higher but air quantity is little, the flow direction that the flow direction of the loose metal wind of higher pressure head and the solid dust that cyclone separator is separated enter dipleg is reciprocal direction, the higher pressure head that relies on loose metal wind upwards impacting cyclone separator is separated the solid dust that enters dipleg and is reached loose metal object, inject and can prevent that cyclone separator from separating and enter dipleg solid dust heap and press by loose metal wind, assemble, realizing cyclone separator separates the solid dust that enters dipleg and enters smoothly in material returning device.Material returning device bottom is furnished with feeding wind ascending pipe near primary zone's end, feeding wind is also that pressure head is higher but air quantity is little, the flow direction of the feeding wind of higher pressure head is equidirectional with the flow direction that enters solid dust in material returning device and send into primary zone, the same higher pressure head that relies on feeding wind upwards injects, sent the solid dust in material returning device back to primary zone (burner hearth) and carried out high-temp combustion again by note wind, the dynamic action of primary zone's (burner hearth) has been played promotion and conveying solid substance dust and has entered in feeding wind action;
Secondary combustion chamber is communicated with cyclone separator gas vent by pipeline, and second-time burning chamber interior is provided with secondary burner;
Second-time burning chamber outlet end is provided with exhaust pass;
On pipeline for delivery of high-temperature gas, be provided with expansion joint;
Primary combustion locular wall is by, incinerator outer wall layer, middle heat-insulation layer and refractory lining composition;
Adopt the present invention of technique scheme, primary zone's burner and secondary burner reach designing requirement by burning auxiliary fuel oil or fuel gas by temperature in stove, generally thoroughly destroy required temperature by fire and determine the ignition temperature of primary zone and secondary combustion chamber according to the most difficult component thoroughly destroying by fire in discarded object composition, under normal circumstances for petrochemical industry, oil refining, pharmacy, waste gas in the production process of the industry such as agricultural chemicals and dyestuff, waste liquid, useless solid " three wastes " primary combustion room temperature is between 650 ℃-850 ℃, secondary combustion chamber internal temperature >=1100 ℃,
Reach after requirement temperature, by chemical industry salt bearing liquid wastes by atomizer with vaporific form the top from waste liquid spout spirt primary zone, waste liquid is in primary combustion indoor seasoning, evaporation, burning;
The useless solid feed hopper arranging by crossbeam type chain-grate front end enters crossbeam type chain-grate, and solid waste is carried out high-temp combustion with the air that the multiple isobaric air compartments in crossbeam type chain-grate bottom are evenly sent here on crossbeam type chain-grate;
The crossbeam type chain-grate arranging in bottom, primary zone is also used for collecting the solid-state saliferous lime-ash that in primary zone, chemical industry salt bearing liquid wastes high temperature drying, evaporation, burning form afterwards, unburnt saliferous lime-ash is on crossbeam type chain-grate (grate) simultaneously, carry out layer combustion by the primary zone's burner that is positioned at crossbeam type chain-grate (grate) top together with solid waste, and by the motion of crossbeam type chain-grate, the saliferous lime-ash burning is transported to afterbody ash bucket, fall into water-cooled slag remover by afterbody ash dropping hopper and carry out cooling and carry.
Waste gas is ejected into by exhaust nozzle that primary combustion is indoor carries out chamber shape burning, after burning, from primary zone, high-temperature flue gas out enters cyclone separator, solid particle under cyclone separator separates is again delivered to primary zone through material returning device and is burnt, and after the residue that burning produces is deposited to crossbeam type chain-grate, is transported to outside stove.
Flue gas after cyclone separator separates enters secondary combustion chamber, is that in guaranteeing flue gas, organic murder by poisoning composition thoroughly decomposes, burns in the main purpose of secondary combustion chamber high-temp combustion.
In primary zone, cyclone separator, material returning device, secondary combustion chamber, high-temperature gas carry flue and exhaust pass inside be all designed with in the middle of heat-insulation layer (insulation furnace lining) and refractory lining, taking into account system expands and requires to be provided with expansion joint between high-temperature components at different levels, top, primary zone is provided with explosion proof door simultaneously, guarantees incinerator hot operation safety by above-mentioned measure.
The high-temperature flue gas that incinerator produces is finally discharged and (can be selected waste heat boiler through exhaust pass introducing next stage equipment; carry out energy recovery; guarantee that the final discharge of low-temperature flue gas reaches environmental protection standard requirement, so not only saved the energy but also be conducive to the protection of atmospheric environment).
To sum up the present invention compared with prior art, utilize waste gas, waste liquid, useless solid " three wastes " integrated incinerator of the dry and Cyclone Separation Technology of crossbeam type chain-grate, spraying, break through unified offal treatment pattern, efficient burning disposal when having realized liquid, gas multicomponent discarded object; The features such as the present invention also has that manufacturing process is simple, easy to maintenance, security of operation is stable are suitablely promoted the use of in the industry saliferous waste gas such as petrochemical industry, oil refining, pharmacy, agricultural chemicals, printing and dyeing and food, waste liquid, useless solid " three wastes " burning disposal.
Above-mentioned explanation is only the general introduction of technical solution of the present invention, in order to better understand technological means of the present invention, and can be implemented according to the content of description, and for above and other object of the present invention, feature and advantage can be become apparent, below especially exemplified by preferred embodiment, and coordinate accompanying drawing, be described in detail as follows.
Accompanying drawing explanation
The present invention is totally 2 width accompanying drawings, wherein:
Fig. 1 is main TV structure schematic diagram of the present invention.
Fig. 2 is plan structure schematic diagram of the present invention.
Fig. 3 is crossbeam type chain-grate of the present invention one end partial enlarged drawing.
In figure: 1, primary zone, 1.1, incinerator outer wall layer, 1.2, expansion joint, 1.3, refractory lining, 2, crossbeam type chain-grate, 2.1, solid waste feed hopper, 2.2, with gear-driven front axle, 2.3, with gear-driven rear axle, 2.4, chain, 2.5, fire grate segment, 2.6, the air compartment of isobaric balanced ventilation, 3, water-cooled slag remover, 4, cyclone separator, 5, secondary combustion chamber, 6, primary zone's burner, 7, exhaust nozzle, 8, waste liquid spout, 9, secondary burner, 10, exhaust pass, 11, expansion joint, 12, explosion proof door, 13, material returning device, 14, feeding wind interface, 15, loose metal wind interface, 16, dipleg.
The specific embodiment
A kind of waste gas as depicted in figs. 1 and 2, waste liquid, useless solid " three wastes " integrated incinerator, comprise: primary zone 1, be arranged at the dry system of spraying of 1 inside, primary zone, be arranged at the crossbeam type chain-grate 2 of 1 bottom, primary zone, water-cooled slag remover 3, cyclone separator 4 and secondary combustion chamber 5;
The dry system of spraying, comprising: layering is arranged at some primary zones burner 6, exhaust nozzle 7 and the waste liquid spout 8 of primary zone's 1 inwall;
Exhaust nozzle 7 and waste liquid spout 8 are arranged between every adjacent two layers primary zone burner 6, and exhaust nozzle 7 with waste liquid spout 8 for distributing alternately; As preferably, exhaust nozzle 7 and waste liquid spout 8 are arranged at respectively between adjacent two layers primary zone burner 6, and exhaust nozzle 7 distributes alternately with waste liquid spout 8, between every adjacent two exhaust nozzles 7, be separated with successively 6 layers of 6 layers of primary zone's burners, 8 layers of waste liquid spouts and primary zone's burners;
1 bottom, primary zone is provided with horizontal chamber, and is provided with crossbeam type chain-grate 2 in horizontal chamber;
Crossbeam type chain-grate 2 tops are provided with primary zone's burner 6;
Crossbeam type chain-grate 2 ends are provided with the water-cooled slag remover 3 for solidfied material after cooling and conveying reaction;
Crossbeam type chain-grate 2 comprise front end be provided with solid waste feed hopper 2.1, with gear-driven front axle 2.2, with compositions such as the air compartments 2.6 of gear-driven rear axle 2.3, chain 2.4, fire grate segment 2.5, multiple isobaric balanced ventilations, front axle 2.2 or rear axle 2.3 all can be arranged decelerator, drag fire grate move backward from front axle 2.2 by electric machine rotation;
Cyclone separator 4 is communicated with the waste gas outlet of 1 upper end, primary zone by pipeline;
Cyclone separator 4 separates solidfied material and exports the material returning device 13 being provided with primary zone's 1 internal communication;
Material returning device 13 inside are as " U " container, one side is dipleg 16, be cyclone separator 4 bottom cone sections and material returning device 13 connecting portions, opposite side is feed pipe, like " L " type, one end is connected with material returning device 13, the other end connects and is connected with primary zone, material returning device 13 bottoms are furnished with loose metal wind ascending pipe 15 near dipleg 16 ends, the pressure head of loose metal wind is higher but air quantity is little, the flow direction that the solid dust that the flow direction of the loose metal wind of higher pressure head and cyclone separator 4 are separated enters dipleg 16 is reciprocal direction, the higher pressure head that relies on loose metal wind upwards impacting cyclone separator 4 is separated the solid dust that enters dipleg 16 and is reached loose metal object, inject and can prevent that cyclone separator 4 from separating and enter dipleg 16 solid dusts heaps and press by loose metal wind, assemble, realizing cyclone separator 4 separates the solid dust that enters dipleg 16 and enters smoothly in material returning device 13.Material returning device 13 bottoms are furnished with feeding wind ascending pipe 14 near primary zone's end, feeding wind is also that pressure head is higher but air quantity is little, the flow direction of the feeding wind of higher pressure head is equidirectional with the flow direction that enters solid dust in material returning device 13 and send into primary zone, the same higher pressure head that relies on feeding wind upwards injects, send the solid dust in material returning device 13 back to primary zone (burner hearth) by note wind and carry out again high temperature combustion, the dynamic action of primary zone's (burner hearth) has been played promotion and conveying solid substance dust and has entered in feeding wind action;
Secondary combustion chamber 5 is communicated with cyclone separator 4 gas vents by pipeline, and secondary combustion chamber 5 inside are provided with secondary burner 9;
Secondary combustion chamber 5 ports of export are provided with exhaust pass 10;
On pipeline for delivery of high-temperature gas, be provided with expansion joint 11;
Primary zone's 1 wall is by, incinerator outer wall layer 1.1, and middle heat-insulation layer 1.2 and refractory lining 1.3 form;
Adopt the present invention of technique scheme, primary zone's burner and secondary burner reach designing requirement by burning auxiliary fuel oil or fuel gas by temperature in stove, generally thoroughly destroy required temperature by fire and determine the ignition temperature of primary zone and secondary combustion chamber according to the most difficult component thoroughly destroying by fire in discarded object composition, under normal circumstances for petrochemical industry, oil refining, pharmacy, waste gas in the production process of the industry such as agricultural chemicals and dyestuff, waste liquid, useless solid " three wastes " primary combustion room temperature is between 650 ℃-850 ℃, secondary combustion chamber internal temperature >=1100 ℃, main purpose is to guarantee that in flue gas, organic murder by poisoning composition thoroughly decomposes, burning, to reach the requirement of environmental emission standard,
Reach after requirement temperature, by chemical industry salt bearing liquid wastes by atomizer with vaporific form the top from waste liquid spout 8 spirt primary zones 1, waste liquid is in primary zone's 5 inner dryings, evaporation, burning;
The crossbeam type chain-grate 2 arranging in 5 bottoms, primary zone is used for collecting the solid-state saliferous lime-ash that primary zone 5 interior chemical industry salt bearing liquid wastes high temperature drying, evaporation, burning form afterwards, unburnt saliferous lime-ash is on crossbeam type chain-grate (grate) 2 simultaneously, carry out layer combustion by the primary zone's burner 6 that is positioned at crossbeam type chain-grate (grate) 2 tops, and by the motion of crossbeam type chain-grate 1, the saliferous lime-ash of after-flame is transported to afterbody ash bucket, fall into water-cooled slag remover 2 by afterbody ash dropping hopper and carry out cooling and carry.
Waste gas is ejected into and in primary zone 5, is carried out chamber shape burning by exhaust nozzle 7, after burning, enter cyclone separator 4 from primary zone 5 high-temperature flue gas out, solid particle under cyclone separator 4 separates is again delivered to primary zone 5 through material returning device 13 and is burnt, and after the residue that burning produces is deposited to crossbeam type chain-grate 2, is transported to outside stove.
Flue gas after cyclone separator 4 separates enters secondary combustion chamber 5, is that in guaranteeing flue gas, organic murder by poisoning composition thoroughly decomposes, burns in the main purpose of secondary combustion chamber 5 high-temp combustions.
As preferred version, in primary zone 1, cyclone separator 4, material returning device 13, secondary combustion chamber 5, high-temperature gas carry flue and exhaust pass 10 inside be all designed with in the middle of heat-insulation layer 1.2(insulation furnace lining) and refractory lining 1.3, taking into account system expands and require to be provided with expansion joint 11 between high-temperature component at different levels, 5 tops, primary zone are provided with explosion proof door 12 simultaneously, guarantee incinerator hot operation safety by above-mentioned measure.
The high-temperature flue gas that incinerator produces is introduced next stage equipment through exhaust pass 10 and is finally discharged and (can select waste heat boiler; carry out energy recovery; guarantee that the final discharge of low-temperature flue gas reaches environmental protection standard requirement, so not only saved the energy but also be conducive to the protection of atmospheric environment).
To sum up the present invention compared with prior art, utilize waste gas, waste liquid, the useless solid integrated incinerator of the dry and Cyclone Separation Technology of crossbeam type chain-grate, spraying, break through unified offal treatment pattern, efficient burning disposal when having realized useless solid, liquid body, gas multicomponent discarded object; The features such as the present invention also has that manufacturing process is simple, easy to maintenance, security of operation is stable are suitablely promoted the use of in the industry such as chemical industry, agricultural chemicals salt bearing liquid wastes burning disposal.
The above, it is only preferred embodiment of the present invention, not the present invention is done to any pro forma restriction, although the present invention discloses as above with preferred embodiment, but not in order to limit the present invention, any those skilled in the art are not departing within the scope of technical solution of the present invention, appeal when utilizing the equivalent embodiment that the technology contents disclosing is made a little change or is modified to equivalent variations, in every case be the content that does not depart from technical solution of the present invention, foundation technical spirit of the present invention is to any simple modification made for any of the above embodiments, equivalent variations and modification, all still belong in the scope of technical solution of the present invention.
Claims (4)
1. a waste gas, waste liquid, useless solid integrated incinerator, it is characterized in that: comprise, primary zone (1), be arranged at the dry system of the inner spraying in primary zone (1), be arranged at the crossbeam type chain-grate (2) of bottom, primary zone (1), water-cooled slag remover (3), cyclone separator (4) and secondary combustion chamber (5);
Described spraying is dried system, comprising: layering is arranged at some primary zones burners (6), exhaust nozzle (7) and the waste liquid spout (8) of primary zone (1) inwall;
Described exhaust nozzle (7) and waste liquid spout (8) are arranged between every adjacent two layers primary zone burner (6), and exhaust nozzle (7) and waste liquid spout (8) are for distributing alternately;
Bottom, described primary zone (1) is provided with horizontal chamber, and in horizontal chamber, is provided with crossbeam type chain-grate (2);
Described crossbeam type chain-grate (2) comprise front end be provided with solid waste feed hopper (2.1), with gear-driven front axle (2.2), with compositions such as the air compartments (2.6) of gear-driven rear axle (2.3), chain (2.4), fire grate segment (2.5), multiple isobaric balanced ventilations, front axle (2.2) or rear axle (2.3) all can be arranged decelerator, drag fire grate move backward from front axle (2.2) by electric machine rotation;
Described crossbeam type chain-grate (2) top is provided with primary zone's burner (6);
Described crossbeam type chain-grate (2) end is provided with the water-cooled slag remover (3) for solidfied material after cooling and conveying reaction;
Described cyclone separator (4) is communicated with the waste gas outlet of upper end, primary zone (1) by pipeline;
Described cyclone separator (4) separates solidfied material and exports the material returning device (13) being provided with primary zone (1) internal communication;
Described secondary combustion chamber (5) is communicated with cyclone separator (4) gas vent by pipeline, and secondary combustion chamber (5) inside is provided with secondary burner (9);
Described secondary combustion chamber (5) port of export is provided with exhaust pass (10).
2. a kind of waste gas according to claim 1, waste liquid, useless solid " three wastes " integrated incinerator, is characterized in that: on the pipeline for delivery of high-temperature gas, be provided with expansion joint (11).
3. a kind of waste gas according to claim 1, waste liquid, useless solid " three wastes " integrated incinerator, is characterized in that: described primary zone (1) wall is by incinerator outer wall layer (1.1), and middle heat-insulation layer (1.2) and refractory lining (1.3) form.
4. a kind of waste gas according to claim 1, waste liquid, solid " three wastes " integrated incinerator that gives up, is characterized in that: described material returning device (13) bottom is furnished with separates and enter the feeding wind ascending pipe (14) that dipleg (16) solid dust prevents the loose metal wind ascending pipe (15) of heap pressure assembly and the solid dust in material returning device (13) sent back to burner hearth cyclone separator (4).
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| CN201410139257.5A CN103868076B (en) | 2014-04-08 | 2014-04-08 | A kind of waste gas, waste liquid, useless solid integration incinerator |
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| CN201410139257.5A CN103868076B (en) | 2014-04-08 | 2014-04-08 | A kind of waste gas, waste liquid, useless solid integration incinerator |
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Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN105823060A (en) * | 2016-03-28 | 2016-08-03 | 张家港市昇泰能源有限公司 | Incineration device and method for conducting incineration treatment on gaseous, solid and liquid waste simultaneously |
| CN106311265A (en) * | 2016-08-03 | 2017-01-11 | 荆楚理工学院 | Device for catalytic incineration of hazardous wastes and the use method thereof |
| CN107120665A (en) * | 2017-07-04 | 2017-09-01 | 大连海伊特重工股份有限公司 | A kind of salt bearing liquid wastes processing unit and method |
| CN107218607A (en) * | 2017-06-28 | 2017-09-29 | 郑文敬 | Saliferous dangerous waste incinerator molten slag Cyclonic separating apparatus and its separating technology |
| CN109798528A (en) * | 2018-12-06 | 2019-05-24 | 上海金山环境再生能源有限公司 | Feed device for waste incinerator |
| CN109899796A (en) * | 2019-04-02 | 2019-06-18 | 上海多灵环保工程设备有限公司 | A kind of multi-function incinerator |
| CN109974009A (en) * | 2019-04-26 | 2019-07-05 | 北京科太亚洲生态科技股份有限公司 | A kind of three wastes integrated reactor and the method for nitrous gas disposal |
| CN112555864A (en) * | 2020-12-10 | 2021-03-26 | 中化环境科技工程有限公司 | Incineration process method for simultaneously treating high-salt organic wastewater and solid wastes |
| CN113137605A (en) * | 2020-01-17 | 2021-07-20 | 北京航天石化技术装备工程有限公司 | Multi-fuel burner for treating garbage pyrolysis products for solid heat carrier furnace |
| CN113137608A (en) * | 2020-01-17 | 2021-07-20 | 北京航天石化技术装备工程有限公司 | Oil gas solid multi-fuel solid heat carrier furnace |
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| CN107218607A (en) * | 2017-06-28 | 2017-09-29 | 郑文敬 | Saliferous dangerous waste incinerator molten slag Cyclonic separating apparatus and its separating technology |
| CN107120665A (en) * | 2017-07-04 | 2017-09-01 | 大连海伊特重工股份有限公司 | A kind of salt bearing liquid wastes processing unit and method |
| CN109798528A (en) * | 2018-12-06 | 2019-05-24 | 上海金山环境再生能源有限公司 | Feed device for waste incinerator |
| CN109899796A (en) * | 2019-04-02 | 2019-06-18 | 上海多灵环保工程设备有限公司 | A kind of multi-function incinerator |
| CN109974009A (en) * | 2019-04-26 | 2019-07-05 | 北京科太亚洲生态科技股份有限公司 | A kind of three wastes integrated reactor and the method for nitrous gas disposal |
| CN109974009B (en) * | 2019-04-26 | 2024-01-30 | 北京科太亚洲生态科技股份有限公司 | Three-waste integrated reactor and method for treating nitrous gases |
| CN113137605A (en) * | 2020-01-17 | 2021-07-20 | 北京航天石化技术装备工程有限公司 | Multi-fuel burner for treating garbage pyrolysis products for solid heat carrier furnace |
| CN113137608A (en) * | 2020-01-17 | 2021-07-20 | 北京航天石化技术装备工程有限公司 | Oil gas solid multi-fuel solid heat carrier furnace |
| CN112555864A (en) * | 2020-12-10 | 2021-03-26 | 中化环境科技工程有限公司 | Incineration process method for simultaneously treating high-salt organic wastewater and solid wastes |
| CN112555864B (en) * | 2020-12-10 | 2023-05-30 | 中化环境科技工程有限公司 | Incineration process method for simultaneously treating high-salt-content organic wastewater and solid waste |
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Effective date of registration: 20161228 Address after: 116031 18-4 District, Ganjingzi, Liaoning, spring B4 District No. Patentee after: DALIAN HANGHUA ENERGY EQUIPMENT CO., LTD. Address before: 116031 30-1 District, Ganjingzi, Liaoning, spring D4 District No. Patentee before: Yu Chuanlin |