CN106402898A - Dioxin treatment system of hazardous waste incineration furnace - Google Patents
Dioxin treatment system of hazardous waste incineration furnace Download PDFInfo
- Publication number
- CN106402898A CN106402898A CN201610954778.5A CN201610954778A CN106402898A CN 106402898 A CN106402898 A CN 106402898A CN 201610954778 A CN201610954778 A CN 201610954778A CN 106402898 A CN106402898 A CN 106402898A
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- CN
- China
- Prior art keywords
- dioxin
- tower
- treatment system
- treatment
- carbon powder
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/44—Details; Accessories
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J15/00—Arrangements of devices for treating smoke or fumes
- F23J15/02—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J15/00—Arrangements of devices for treating smoke or fumes
- F23J15/02—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material
- F23J15/022—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material for removing solid particulate material from the gasflow
- F23J15/025—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material for removing solid particulate material from the gasflow using filters
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J15/00—Arrangements of devices for treating smoke or fumes
- F23J15/02—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material
- F23J15/04—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material using washing fluids
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J2215/00—Preventing emissions
- F23J2215/30—Halogen; Compounds thereof
- F23J2215/301—Dioxins; Furans
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J2217/00—Intercepting solids
- F23J2217/10—Intercepting solids by filters
- F23J2217/101—Baghouse type
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J2217/00—Intercepting solids
- F23J2217/50—Intercepting solids by cleaning fluids (washers or scrubbers)
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J2219/00—Treatment devices
- F23J2219/10—Catalytic reduction devices
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J2219/00—Treatment devices
- F23J2219/20—Non-catalytic reduction devices
- F23J2219/201—Reducing species generators, e.g. plasma, corona
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Treating Waste Gases (AREA)
Abstract
The invention discloses a dioxin treatment system of a hazardous waste incineration furnace. The dioxin treatment system comprises a pretreatment system, an incineration system and a smoke purification system. The incineration system comprises a rotary kiln and a secondary combustion chamber. A dry reactor is arranged between a smoke outlet of a quench tower and a bag type dust collector of the smoke purification system, and lime activated carbon is jet in the dry reactor. A plasma dioxin removing tower is arranged behind the bag type dust collector. An activated carbon powder adding device is arranged in a circulating pond, and water mixed with activated carbon powder enters a wet deacidification tower to be sprayed. Multiple equipment and process controlling points are set in the whole hazardous waste incineration furnace, dioxin type substances are effectively adsorbed and controlled, and it is ensured that tail gas emission meets the standard. The dioxin treatment system is good in treatment effect, wide in treatment range, good in universality, high in treatment depth and high in operation stability and impact resistance, and the treatment effect is good in winter and summer.
Description
Technical field
The present invention relates to field of environment protection equipment, especially a kind of dioxin treatment system of danger waste burning stove.
Background technology
Dioxin is the serious liposoluble substance of a kind of colorless and odorless, toxicity, is a class extremely toxic substance.In atmospheric environment
Dioxin source is complicated, and smelting iron and steel, non-ferrous metal metallurgy, vehicle exhaust, burning produce(Including pharmaceutical wastewater burning, chemical industry
The incineration of waste of factory, consumer waste incineration, coal-burning power plant etc.)Dioxin all can be produced, wherein danger waste waste incineration produces two
The mechanism disliking English is more complicated, thus concerned degree highest.Existing danger waste burning stove is less to the process of dioxin or adopts
Process dioxin with single equipment, thus environmental requirement can not be met.
Content of the invention
The applicant be directed to above-mentioned existing danger waste burning stove weaker to the process of dioxin the shortcomings of, provide a kind of structure to close
The dioxin treatment system of the danger waste burning stove of reason, such that it is able to reach preferable dioxin treatment effect it is ensured that exhaust emissions
Up to standard.
The technical solution adopted in the present invention is as follows:
A kind of dioxin treatment system of danger waste burning stove, including pretreatment system, CIU and system for cleaning fume,
Described CIU includes rotary kiln and dual firing chamber;The exhanst gas outlet of the chilling tower in described system for cleaning fume is to cloth bag
It is provided with dry type reactor between cleaner unit, carry out the injection of Activity of Lime charcoal wherein;It is provided with after sack cleaner
Plasma removes dioxin tower;Circulating water pool is provided with active carbon powder adding apparatus, and the water of mixing and doping active carbon powder is again
Enter in wet method extracting tower and sprayed.
Improvement further as technique scheme:
In described dual firing chamber, spray into air and combustion gas or fuel oil so as to abundant burn, and ensure flue gas 1100 DEG C in dual firing chamber
The temperatures above area time of staying is more than 2 seconds.
It is secondary device that described plasma removes dioxin tower, and the first order is high energy electron ionized region, and the second level is that catalysis is inhaled
Attached area.
Beneficial effects of the present invention are as follows:
The present invention passes through setting many places equipment and technology in whole danger waste burning furnace system and controls, and reaches the effect processing dioxin
Really.In dual firing chamber, fully burn and dioxin is destroyed by fire with high temperature by spraying into air and combustion gas or fuel oil.Flue gas in chilling tower
It is exported on the pipeline between sack cleaner and spray into active carbon powder, the dioxin to the heavy metal in flue gas and possible regeneration
Class material is adsorbed.Removing in dioxin tower in plasma makes electronics, ion, free radical and neutral grain using high energy electron ray
Son bombards dioxin macromole at a high speed repeatedly, and realizes reacting further using catalysis and absorption.The present invention is by active carbon powder
Add circulating water pool and mix, the water being doped with active carbon powder is sprayed in wet method extracting tower, thus more effectively
Absorption and control dioxin-like chemical are it is ensured that exhaust emissions is up to standard.High treating effect of the present invention, process range is wide, and versatility is good,
Process depth height, operation stability and strong shock resistance, all there is good treatment effect summer in winter.
Brief description
Fig. 1 is the schematic diagram of the present invention.
In figure:1st, hydraulic pressure material-pulling device;2nd, rotary kiln;3rd, dual firing chamber;4th, waste heat boiler;5th, chilling tower;6th, dry type reaction
Device;7th, sack cleaner;8th, plasma removes dioxin tower;9th, first order wet method extracting tower;10th, second level wet method extracting tower;11、
Smoke re-heater;12nd, chimney;13rd, circulating water pool;14th, active carbon powder.
Specific embodiment
Below in conjunction with the accompanying drawings, the specific embodiment of the present invention is described.
As shown in figure 1, danger waste burning furnace system generally includes waste pretreatment system, feeding system, CIU, flue gas
Several part such as cleaning treatment system.Waste pretreatment system includes pretreatment and the feed process of waste, and industrial hazard is discarded
Thing is transported to the center of disposal storehouse by special-purpose vehicle, and the broken material of needs is grabbed to hang by driving after crusher in crushing, compatibility and sent
Enter kiln hood charging aperture on operating platform, sent into back by hydraulic pressure material-pulling device 1 after two-stage hydraulic pressure insertion plate door in kiln hood charging aperture
Rotary kiln 2.
CIU by rotary kiln 2 and dual firing chamber 3, slag tap and control system forms;Rotary kiln 2 burns the flue gas producing and enters
Enter dual firing chamber 3, in dual firing chamber 3, spray into air and combustion gas or fuel oil so as to abundant burn, and ensure flue gas in dual firing chamber 3
1100 DEG C of temperatures above area time of staying are more than 2 seconds, destroy dioxin by fire with high temperature.
System for cleaning fume is absorbed by waste heat recovery, chilling, dry type reactor 6 and cleaner, sour gas, cigarette
Gas reheating, except dioxin equipment composition.The high-temperature flue gas that dual firing chamber 3 produces enter waste heat boiler 4, and recovery section energy production is steamed
Vapour, steam is available for factory steam and other vapour by gas-distributing cylinder.The sedimentation interior entering waste heat boiler 4 in flue gas is provided with de-
Nitre system is it is ensured that the index of exhaust emissions NOX.Flue gas temperature after waste heat boiler 4 drops to 500 DEG C~550 DEG C, and flue gas directly enters
In chilling tower 5, spray cooling water, completes to be down to 200 DEG C of chilling in 1 second from 500 DEG C, ensure that flue gas purification system fortune
The stability of row and reliability.It is provided with dry type reactor 6 between the exhanst gas outlet of chilling tower 5 is to sack cleaner 7, at it
In carry out the injection of Activity of Lime charcoal, the heavy metal in activated carbon powder foot couple flue gas and may the dioxin-like chemical of regeneration carrying out
Absorption, Calx carries out the sour gas in moisture absorption and absorption flue gas, and the dust after absorption and absorption enters sack cleaner 7,
Deliver to plasma after being purified by sack cleaner 7 and remove dioxin tower 8 under being drawn of air-introduced machine, then the flue gas entrance first order is wet
Carry out deacidification once again, after flue gas reheat, gas up to standard passes through smoke re-heater 11 in method extracting tower 9, second level wet method extracting tower 10
Enter air with chimney 12.Active carbon powder 14 is added circulating water pool 13 and mixes by the present invention, will be doped with active carbon powder
14 water is passed through in wet method extracting tower and is sprayed, thus more effectively adsorbing and controlling dioxin-like chemical it is ensured that tail gas is arranged
Unconventional and unrestrained mark.
It is secondary device that the plasma that the present invention is arranged after sack cleaner 7 removes dioxin tower 8, and the first order is high energy
Electron ionization area, the second level is catalytic adsorption area.High energy electron ionized region makes electronics, ion, freedom using high energy electron ray
Base and neutral particle bombard at a high speed dioxin macromole, activation, ionization, each component cracking in waste gas repeatedly, are allowed to oxygen
The chemical reaction of the series of complexes such as change.High treating effect, process range is wide, and versatility is good, processes depth high.Pass through rear one again
The catalysis of level and absorption, can react the plasma oxygen not reacted further, improve the utilization rate of plasma oxygen, etc.
Ion coefficient of oxygen utilization substantially achieves 100%, reduces generator power, and the consumption of electric energy is few, reduces operating cost.At two grades
Reason design improves the operation stability of system, strong shock resistance, and all there is good treatment effect summer in winter.On market
Other reactor ratios, reactor volume is moderate, has the rational time of staying, and reaction is completely.
Above description is explanation of the invention, is not the restriction to invention, without departing from the spirit of the invention,
The present invention can make any type of modification.
Claims (3)
1. a kind of dioxin treatment system of danger waste burning stove, including pretreatment system, CIU and gas cleaning processing system
System it is characterised in that:Described CIU includes rotary kiln(2)With dual firing chamber(3);Urgency in described system for cleaning fume
Cold tower(5)Exhanst gas outlet to sack cleaner(7)Between be provided with dry type reactor(6), carry out Activity of Lime charcoal wherein
Injection;In sack cleaner(7)It is provided with plasma afterwards and remove dioxin tower(8);Circulating water pool(13)It is provided with activated carbon
Powder(14)Adding apparatus, mixing and doping active carbon powder(14)Water enter back in wet method extracting tower and sprayed.
2. according to described in claim 1 danger waste burning stove dioxin treatment system it is characterised in that:Described dual firing chamber(3)
In, spray into air and combustion gas or fuel oil so as to abundant burn, and ensure flue gas in dual firing chamber(3)Interior 1100 DEG C of temperatures above areas
The time of staying is more than 2 seconds.
3. according to described in claim 1 danger waste burning stove dioxin treatment system it is characterised in that:Described plasma removes two
Dislike Integrata(8)For secondary device, the first order is high energy electron ionized region, and the second level is catalytic adsorption area.
Priority Applications (1)
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CN201610954778.5A CN106402898B (en) | 2016-11-03 | 2016-11-03 | The dioxin treatment system of dangerous waste incinerator |
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CN201610954778.5A CN106402898B (en) | 2016-11-03 | 2016-11-03 | The dioxin treatment system of dangerous waste incinerator |
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CN106402898A true CN106402898A (en) | 2017-02-15 |
CN106402898B CN106402898B (en) | 2019-01-04 |
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Cited By (5)
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CN107983126A (en) * | 2018-01-22 | 2018-05-04 | 天津市美好生活科技有限公司 | Incineration flue gas minimum discharge purifying treatment method and its processing system |
CN110006050A (en) * | 2019-03-20 | 2019-07-12 | 浙江大维高新技术股份有限公司 | Dangerous waste incineration flue gas purification system and technique |
CN110180356A (en) * | 2019-03-20 | 2019-08-30 | 浙江大维高新技术股份有限公司 | The processing unit and method of Cremation Machine incineration flue gas |
CN110793338A (en) * | 2019-11-29 | 2020-02-14 | 中国科学院过程工程研究所 | Flue gas purification and waste heat utilization system and method |
CN112594728A (en) * | 2020-12-07 | 2021-04-02 | 安徽欣创节能环保科技股份有限公司 | Domestic waste incineration fly ash classification treatment system |
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Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
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CN107983126A (en) * | 2018-01-22 | 2018-05-04 | 天津市美好生活科技有限公司 | Incineration flue gas minimum discharge purifying treatment method and its processing system |
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CN110180356A (en) * | 2019-03-20 | 2019-08-30 | 浙江大维高新技术股份有限公司 | The processing unit and method of Cremation Machine incineration flue gas |
CN110793338A (en) * | 2019-11-29 | 2020-02-14 | 中国科学院过程工程研究所 | Flue gas purification and waste heat utilization system and method |
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CN112594728A (en) * | 2020-12-07 | 2021-04-02 | 安徽欣创节能环保科技股份有限公司 | Domestic waste incineration fly ash classification treatment system |
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