CN204141592U - A kind of incinerator processing solid waste liquid - Google Patents
A kind of incinerator processing solid waste liquid Download PDFInfo
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- CN204141592U CN204141592U CN201420364395.9U CN201420364395U CN204141592U CN 204141592 U CN204141592 U CN 204141592U CN 201420364395 U CN201420364395 U CN 201420364395U CN 204141592 U CN204141592 U CN 204141592U
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- incinerator
- waste liquid
- solid waste
- processing solid
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Abstract
The utility model provides a kind of incinerator processing solid waste liquid, comprise incinerator, incinerator is connected with secondary combustion chamber, secondary combustion chamber is connected with high-temperature cyclone dust extractor, high-temperature cyclone dust extractor is connected with waste heat boiler, waste heat boiler is connected with sack cleaner, and sack cleaner is connected with air-introduced machine, and air-introduced machine is connected with chimney.A kind of incinerator processing solid waste liquid of the utility model, coordinate smelting furnace to carry out burning subsequent treatment to solid waste liquid, alternative traditional is direct to fixedly carrying out burning disposal, reduces cost of investment, maintenance cost and operating cost, enhances stability simultaneously.
Description
Technical field
The utility model relates to a kind of incinerator processing solid waste liquid, belongs to field of environment protection equipment.
Background technology
At present, along with the quickening of process of industrialization, the demand of solids treatment is increasing, and traditional mode is all process with rotary kiln, but this mode is invested greatly, poor stability, maintenance cost are high, operating cost is also high.
Utility model content
The technical problems to be solved in the utility model overcomes existing defect, provides a kind of incinerator processing solid waste liquid, reduces cost of investment, maintenance cost and operating cost, strengthen stability simultaneously.
In order to solve the problems of the technologies described above, the utility model provides following technical scheme:
A kind of incinerator processing solid waste liquid, comprise incinerator, described incinerator is connected with secondary combustion chamber, described secondary combustion chamber is connected with high-temperature cyclone dust extractor, described high-temperature cyclone dust extractor is connected with waste heat boiler, described waste heat boiler is connected with sack cleaner, and described sack cleaner is connected with air-introduced machine, and described air-introduced machine is connected with chimney.
Further, thermal storage ceramic is provided with in described incinerator.
Further, flame-proof thermal insulation material is provided with in described high-temperature cyclone dust extractor.
Further, described waste heat boiler adopts film water cold wall structure.
Further, economizer is provided with between described waste heat boiler and sack cleaner.
Further, described sack cleaner adopts glass overlay film acupuncture filter bag.
A kind of incinerator processing solid waste liquid of the utility model, coordinate smelting furnace to carry out burning subsequent treatment to solid waste liquid, alternative traditional is direct to fixedly carrying out burning disposal, reduces cost of investment, maintenance cost and operating cost, enhances stability simultaneously.
Accompanying drawing explanation
Accompanying drawing is used to provide further understanding of the present utility model, and forms a part for description, is used from explanation the utility model, does not form restriction of the present utility model with embodiment one of the present utility model.In the accompanying drawings:
Fig. 1 is a kind of structural representation processing the incinerator of solid waste liquid of the utility model.
Detailed description of the invention
Below in conjunction with accompanying drawing, preferred embodiment of the present utility model is described, should be appreciated that preferred embodiment described herein is only for instruction and explanation of the utility model, and be not used in restriction the utility model.
As shown in Figure 1, a kind of incinerator processing solid waste liquid, comprise incinerator 1, incinerator 1 is connected with secondary combustion chamber 2, secondary combustion chamber 2 is connected with high-temperature cyclone dust extractor 3, and high-temperature cyclone dust extractor 3 is connected with waste heat boiler 4, and waste heat boiler 4 is connected with sack cleaner 5, sack cleaner 5 is connected with air-introduced machine 6, and air-introduced machine 6 is connected with chimney 7.
Be provided with thermal storage ceramic in incinerator, be used for reducing burning and consume.
Be provided with flame-proof thermal insulation material in high-temperature cyclone dust extractor, make the time of staying of high-temperature flue gas longer, material oxidation Decomposition is more abundant.
Waste heat boiler adopts film water cold wall structure, to strengthen the dust removing effects of waste heat boiler.
Be provided with economizer 8 between waste heat boiler and sack cleaner, be used for reclaiming heat, utilize fume afterheat further.
Sack cleaner adopts glass overlay film acupuncture filter bag, extends the service life of filter bag.
Compared with existing rotary system, incinerator of the present utility model also has following characteristics:
1, be provided with Chang Minghuo, UV flame detector in stove, just start Waste liquid atomization system when guaranteeing there is naked light in stove, prevent the detonation of catching fire in stove.
2, body of heater burning is according to the design of 3T1E (temperature, time, eddy current, coefficient of excess) principle, guarantee that waste liquid is fully oxidized in furnace body combustion chamber, pyrolysis, burning, make organic destruction clearance reach more than 99.99%.
3, body of heater adopts tangential atomising device-internal mix formula dual-flow atomizer nozzle.Its mixability, atomizing effect, burning velocity and ultrahigh in efficiency, excess air coefficient is low, can save a large amount of fuel.Atomizer bore is large, less demanding to the viscosity of fluid, impurity content, not easily blocks.Adopt low pressure atomizing mode, higher pressure torch-type safety, not easy to wear, not easily fault, combustion efficiency is good.
4, security is high.Do not get rid of the function that explosion hazard gases just can not be lighted a fire before being provided with startup, with gas explosion-proof, be provided with flame detector in stove, once there is flame-out or loss of ignition in stove, automatically cut off waste liquid supply immediately, warning system is perfect, safe and reliable.
The course of work: it is liquid that solid is melted by steam tracing, sends into incinerator, light burning through diesel fuel burner by steam atomization.Guarantee Waste liquid atomization burning produce flue gas in burner hearth the time of staying >=2s, flue gas temperature of hearth outlet 1100 DEG C.
Incinerator high-temperature flue gas out enters secondary combustion chamber and is oxidized further, then, enters the dust in high-temperature cyclone dust extractor removing flue gas, ensures the normal operation of follow-up equipment.
Then flue gas is through waste heat boiler and economizer, and after flue gas and boiler feedwater heat exchange, produce the 1.1Mpa meeting need of production, the saturated vapor of 187 DEG C, flue-gas temperature is reduced to about 200 DEG C simultaneously.
Enter sack cleaner with the flue gas compared with fine grain dust, flue gas is by outer through filter bag, and the dust in flue gas is trapped within filter bag outer surface thus is purified, and flue gas Venturi tube in deduster enters upper box, discharges from outlet.Attached collection constantly increases at the dust of filter bag outer surface, dust remover resistance is increased, maintain in the scope of restriction for making equipment resistance, must regularly eliminate the dust being attached to filter bag surface: by controller by regular sequence trigger switch each control valve unbalanced pulse valve, gas bag compressed air is made to spray (title First air) by injection tube eyelet, pass through Venturi tube, the surrounding air (title Secondary Air) that induction is several times as much as First air enters filter bag, filter bag is sharply being expanded in a flash, and along with the acting in opposition of air-flow, shake off dust, make dust emission in flue gas can reach national environmental standard requirement.Sack cleaner is provided with by-pass flue, deduster inlet temperature not in limits time, cloth bag bypass solenoid valve is opened, and flue gas is discharged by by-pass flue, does not form fatal damages when guaranteeing cigarette temperature abnormality to cloth bag.Flue gas after dedusting is extracted out by air-introduced machine, and by smoke stack emission in air.
A kind of incinerator processing solid waste liquid of the utility model, coordinate smelting furnace to carry out burning subsequent treatment to solid waste liquid, alternative traditional is direct to fixedly carrying out burning disposal, reduces cost of investment, maintenance cost and operating cost, enhances stability simultaneously.
Last it is noted that the foregoing is only preferred embodiment of the present utility model, be not limited to the utility model, although be described in detail the utility model with reference to previous embodiment, for a person skilled in the art, it still can be modified to the technical scheme described in foregoing embodiments, or carries out equivalent replacement to wherein portion of techniques feature.All within spirit of the present utility model and principle, any amendment done, equivalent replacement, improvement etc., all should be included within protection domain of the present utility model.
Claims (6)
1. one kind processes the incinerator of solid waste liquid, it is characterized in that: comprise incinerator, described incinerator is connected with secondary combustion chamber, described secondary combustion chamber is connected with high-temperature cyclone dust extractor, described high-temperature cyclone dust extractor is connected with waste heat boiler, described waste heat boiler is connected with sack cleaner, and described sack cleaner is connected with air-introduced machine, and described air-introduced machine is connected with chimney.
2. a kind of incinerator processing solid waste liquid according to claim 1, is characterized in that: be provided with thermal storage ceramic in described incinerator.
3. a kind of incinerator processing solid waste liquid according to claim 1, is characterized in that: be provided with flame-proof thermal insulation material in described high-temperature cyclone dust extractor.
4. a kind of incinerator processing solid waste liquid according to claim 1, is characterized in that: described waste heat boiler adopts film water cold wall structure.
5. a kind of incinerator processing solid waste liquid according to claim 1, is characterized in that: be provided with economizer between described waste heat boiler and sack cleaner.
6. a kind of incinerator processing solid waste liquid according to claim 1, is characterized in that: described sack cleaner adopts glass overlay film acupuncture filter bag.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420364395.9U CN204141592U (en) | 2014-07-02 | 2014-07-02 | A kind of incinerator processing solid waste liquid |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420364395.9U CN204141592U (en) | 2014-07-02 | 2014-07-02 | A kind of incinerator processing solid waste liquid |
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| Publication Number | Publication Date |
|---|---|
| CN204141592U true CN204141592U (en) | 2015-02-04 |
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| CN201420364395.9U Active CN204141592U (en) | 2014-07-02 | 2014-07-02 | A kind of incinerator processing solid waste liquid |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106838910A (en) * | 2017-02-14 | 2017-06-13 | 西安山岳环保科技有限公司 | One kind useless solid and liquid waste incineration and exhaust heat recovering method |
| CN111578803A (en) * | 2020-05-26 | 2020-08-25 | 中国人民解放军32181部队 | TNT explosive spray destroying method |
-
2014
- 2014-07-02 CN CN201420364395.9U patent/CN204141592U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106838910A (en) * | 2017-02-14 | 2017-06-13 | 西安山岳环保科技有限公司 | One kind useless solid and liquid waste incineration and exhaust heat recovering method |
| CN111578803A (en) * | 2020-05-26 | 2020-08-25 | 中国人民解放军32181部队 | TNT explosive spray destroying method |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |