CN110307547A - Microwave catalysis incinerator - Google Patents
Microwave catalysis incinerator Download PDFInfo
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- CN110307547A CN110307547A CN201910701153.1A CN201910701153A CN110307547A CN 110307547 A CN110307547 A CN 110307547A CN 201910701153 A CN201910701153 A CN 201910701153A CN 110307547 A CN110307547 A CN 110307547A
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- 238000006555 catalytic reaction Methods 0.000 title claims abstract description 19
- 238000001816 cooling Methods 0.000 claims abstract description 37
- 238000007599 discharging Methods 0.000 claims abstract description 11
- 238000010438 heat treatment Methods 0.000 claims abstract description 10
- 238000000197 pyrolysis Methods 0.000 claims abstract description 8
- 239000007789 gas Substances 0.000 claims description 29
- 239000000203 mixture Substances 0.000 claims description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 16
- 239000012774 insulation material Substances 0.000 claims description 11
- 238000000034 method Methods 0.000 claims description 9
- 238000002485 combustion reaction Methods 0.000 claims description 8
- 238000010583 slow cooling Methods 0.000 claims description 8
- 239000000498 cooling water Substances 0.000 claims description 6
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 6
- 229910010293 ceramic material Inorganic materials 0.000 claims description 3
- 238000005260 corrosion Methods 0.000 claims description 3
- 230000007797 corrosion Effects 0.000 claims description 3
- 238000000605 extraction Methods 0.000 claims description 3
- 230000008676 import Effects 0.000 claims description 3
- 239000003345 natural gas Substances 0.000 claims description 3
- 230000006641 stabilisation Effects 0.000 claims description 3
- 238000011105 stabilization Methods 0.000 claims description 3
- 239000010935 stainless steel Substances 0.000 claims description 3
- 229910001220 stainless steel Inorganic materials 0.000 claims description 3
- 238000009825 accumulation Methods 0.000 claims description 2
- 238000012545 processing Methods 0.000 abstract description 7
- 239000000463 material Substances 0.000 description 21
- 239000000126 substance Substances 0.000 description 19
- 229910000975 Carbon steel Inorganic materials 0.000 description 4
- 239000010962 carbon steel Substances 0.000 description 4
- 239000002737 fuel gas Substances 0.000 description 4
- 238000001035 drying Methods 0.000 description 3
- 238000005265 energy consumption Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 239000002671 adjuvant Substances 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- 230000003197 catalytic effect Effects 0.000 description 2
- 238000009833 condensation Methods 0.000 description 2
- 230000005494 condensation Effects 0.000 description 2
- 238000004134 energy conservation Methods 0.000 description 2
- 150000003384 small molecules Chemical class 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- GALOTNBSUVEISR-UHFFFAOYSA-N molybdenum;silicon Chemical compound [Mo]#[Si] GALOTNBSUVEISR-UHFFFAOYSA-N 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 230000001360 synchronised effect Effects 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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
- F23G5/02—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
- F23G5/027—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage
-
- 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
- F23G5/02—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
- F23G5/04—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment drying
-
- 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
- F23G5/08—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating
- F23G5/10—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating electric
-
- 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
-
- 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
- F23G5/50—Control or safety arrangements
-
- H—ELECTRICITY
- H05—ELECTRIC TECHNIQUES NOT OTHERWISE PROVIDED FOR
- H05B—ELECTRIC HEATING; ELECTRIC LIGHT SOURCES NOT OTHERWISE PROVIDED FOR; CIRCUIT ARRANGEMENTS FOR ELECTRIC LIGHT SOURCES, IN GENERAL
- H05B6/00—Heating by electric, magnetic or electromagnetic fields
- H05B6/64—Heating using microwaves
- H05B6/80—Apparatus for specific applications
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Electromagnetism (AREA)
- Gasification And Melting Of Waste (AREA)
- Incineration Of Waste (AREA)
Abstract
The present invention relates to burning processing equipment technical fields, more particularly to microwave catalysis incinerator, including being made of charging cabin, preheating section, dryer section, slow warming-up section, pyrolysis section, burning zone, cooling system, microwave heating system, electric-control system, discharging cabin, automatic conveying system, entire incinerator is supported by rack.The present invention provides microwave incinerators can play the effect that burning is abundant, thermal inertia is small, controllability is high using multi-segment structure, and the incinerator has the characteristics that capacity usage ratio is high, tail gas yield is small.
Description
Technical field
The present invention relates to substance burning disposal equipment technical field more particularly to a kind of microwave catalysis incinerators.
Technical background
With the development of the society, people's lives level steps up, consumption substance increase simultaneously, arrange in production
The substance also synchronous increase put or generated in living, handles these substances or has become an extremely urgent difficulty of entire society
Topic.The method of existing treated substance generally uses: landfill method and incineration method.The mode of landfill is increasingly not suitable with existing substance
On the one hand processing occupies limited land resource, on the one hand not can solve substance processing problem and only problem is stepped back, both wasted
There is pollution environment in soil.So incineration method is substance processing using more and more extensive, but conventional incineration method treated substance mistake
Occur much being difficult to overcome the problems, such as in journey: 1. equipment investment is big, and operation cost is high, land occupation is more, 2. burns the tail gas of generation
More with solid particle, what is 3. burnt is insufficient, is easy to produce more toxic and harmful gas.
Catalytic Technique of Microwave obtains everybody concern in substance processing as a kind of free of contamination clean technologies.Due to existing
Microwave technology is limited in substance processing with the presence of the problems such as microwave technology energy consumption is high, conversion ratio is low, processing capacity is limited
Using.Make processed substance that there is wave-sucking performance there are water or in substance addition sensitizer (inhaling wave substance) in substance, mentions
Rise microwave treatment ability.
Presently, there are the problem of: 1 conventional incinerator burning is insufficient；2 conventional combustion furnaces, which cannot be opened, to stop；3 energy consumptions are high,
Tail is large-minded；4 controllabilities are poor.
Summary of the invention
The purpose of the present invention is to solve above-mentioned technical problems existing for catalytic burning furnace in the prior art, and propose
Microwave catalysis incinerator.
To achieve the goals above, present invention employs following technical solutions:
Designing microwave catalysis incinerator includes charging cabin, preheating section, dryer section, slow warming-up section, pyrolysis section, burning zone, cooling
System, microwave heating system, electric-control system, discharging cabin, automatic conveying system composition, entire incinerator are supported by rack.
Further, the material of main part of the incinerator rack is carbon steel.
Further, the charging cabin and discharging cabin are equipped with two seals door, and outside is connected with automatic conveying system, interior
Portion is connected with preheating chamber and sub-cooled room respectively.In charging or discharging, two seals door cannot be opened simultaneously, and maintain furnace chamber
Interior each section stable gas pressure distribution.
Further, the preheating section is mainly by furnace body, bell, burner hearth, thermal insulation material, high-temperature gas air inlet, thermometric
The composition such as mouth, condensate water discharging mouth, preheating section furnace body two sides are equipped with microwave feed-in mouth, connect microwave generator.
Further, burning zone high-temperature gas is introduced into preheating section by the preheating section high-temperature gas air inlet, described cold
Condensate drain pipe port is the cold energy water row's discharge for generating preheating section.
Further, the dryer section is mainly made of furnace body, bell, burner hearth, thermal insulation material, temperature-measuring port etc., described dry
Dry section is equipped with microwave feed-in mouth with the furnace body two sides for decomposing section, connects microwave generator.Dryer section, which mainly uses, inhales wave in material
Substance under the irradiation of microwave, can gasify rapidly, achieve the purpose that dry.
Further, the dryer section has a exhaust port, for the gas of dry generation to be discharged.
Further, the decomposition section is mainly made of furnace body, bell, burner hearth, thermal insulation material, temperature-measuring port etc..In furnace body
Two sides are equipped with microwave feed-in mouth.High wave of inhaling in material absorbs microwave, the part formed a little is high up to thousands of degree in microwave field
Temperature is pyrolyzed material.
Further, the burning zone mainly by furnace body, bell, burner hearth, thermal insulation material, temperature-measuring port, open fire burning device,
The composition such as air inlet, suction opening；For the open fire burning device by outer for liquefied gas or combustion of natural gas, guarantee to generate in furnace can
Combustion gas body burns in time, prevent high concentration accumulation cause to dodge it is quick-fried.
Further, the cooling section include High-temperature cooling section, Slow cooling section and sub-cooled section, cooling section mainly by
The composition such as furnace body, bell, burner hearth, temperature-measuring port, air inlet and air outlet；The bottom of the High-temperature cooling section is into cooling wind, top
Preheating cooling wind extraction is imported in burning zone furnace body；The bottom of the sub-cooled section is into cooling wind, and top is by the cold of preheating
But wind imports preheating section.
Further, the furnace body is welded by heat-resistance stainless steel；The burner hearth uses high temperature ceramic material saggar
A tunnel furnace chamber is constituted, prevents corrosive goods confrontation furnace body from generating corrosion；The temperature-measuring port is connected with temperature sensor, is used for
Measure real-time temperature in each section of furnace chamber.
Further, the inlet and outlet of the furnace body is equipped with microwave anti-leak real time warning device.
Further, the microwave heating system is mainly made of microwave source and magnetron cooling water system, by automatically controlled system
System control.
Further, the peak power output of the microwave source is 1KW.
Further, the magnetron cooling system uses water cooling, and independent cooling water all the way, packet is arranged in each magnetron
Include inlet valve.
Further, the electric-control system is by programmable controller (PLC), touch screen, temperature controller and other
Control circuit composition；Can be completed on the touch screen parameters setting, display, warning message is shown and operating function.
Further, the warning message shows to include to have instruction function, overcurrent alarm, undercurrent to each magnetron
The function of alarm and overtemperature alarm.
Further, the automatic conveying system is made of automatic outer circulation transportation system and propulsion system, all using certainly
Hydrodynamic pressure device, the running speed of adjustable systems, to guarantee reasonable process adjustments range, the automatic outer circulation is with carbon steel
For main body support frame.
Further, there are two zero-pressure control plane, zero-pressure control planes by setting for the slow warming-up section and Slow cooling section
The stabilization of two eutral margins is controlled by two induced draft fans.
Microwave catalysis incinerator of the invention by adopting the above technical scheme, can achieve following beneficial effect.
1) multisection type furnace structure keeps burning more abundant, combustible material can be made to decompose under the conditions of environment temperature is lower
At small molecule combustible, make combustible full combustion, produces CO2And water, keep exhaust emissions clean, environmentally friendly.
2) thermal inertia is small, and heating and cooling velocity are fast in furnace body, realizes to open and stop.
3) controllability is good, and microwave energy is dispersed in outside furnace body, realizes the accurate power input control of subsection, can more not
The performance of commaterial inputs adaptable microwave power.
4) energy saving, exhaust emissions is few, and it is few that tail gas takes away heat, and compared to conventional incinerators using natural gas or fuel oil as energy
Source, capacity usage ratio is high, and tail gas takes away little energy.Microwave heating itself does not generate tail gas, energy conservation and environmental protection, while saving at tail gas
Manage section equipment cost.
Detailed description of the invention
The present invention will be further described in detail below with reference to the accompanying drawings and specific embodiments.
Fig. 1 is schematic diagram of the invention.
The present invention will be further described in detail with reference to the accompanying drawing.
Such as Fig. 1, this implementation column microwave catalysis incinerator, including charging cabin, preheating section, dryer section, slow warming-up section, pyrolysis
Section, burning zone, cooling system, microwave heating system, electric-control system, discharging cabin, automatic conveying system composition, entire incinerator by
Rack support.
In the present embodiment, rack is material by carbon steel, supports entire incinerator system, provides a stable operation ring
Border.
In the present embodiment, charging cabin is made of two seals door, doorframe, cylinder etc., and first of hermatic door and outside are automatic
Transportation system is connected, and second hermatic door is connected with preheating chamber.
When it is implemented, first of hermatic door is opened, and second hermatic door closes when burning substance and sending to designated position
It closes, saggar promotes charging cabin；First of hermatic door is closed, and second hermatic door is opened, and saggar promotes in furnace body.
In the present embodiment, preheating section is by furnace body, bell, burner hearth, thermal insulation material, high-temperature gas air inlet, temperature-measuring port, condensation
The composition such as water discharge outlet, preheating section furnace body two sides are equipped with microwave feed-in mouth, connect microwave generator.
In specific embodiment, high-temperature gas air inlet is used to burning zone high-temperature gas being introduced into preheating section, assists with microwave
Same-action will be heated newly into the material in furnace；Temperature-measuring port then is used to measure the instant preheating temperature of material；Contain in high-temperature gas
Vapor during preheating cold material, due to temperature decline, dew condensation water, from condensate water discharging mouth be discharged.
In the present embodiment, dryer section is mainly made of furnace body, bell, burner hearth, thermal insulation material, temperature-measuring port etc., the drying
Section and the furnace body two sides for decomposing section are equipped with microwave feed-in mouth, connect microwave generator.
In specific embodiment, for the material containing moisture under the irradiation of microwave, the dielectric constant of water is big, inhales wave energy
By force, under the irradiation of microwave, the water in dangerous waste gasifies rapidly and is discharged by exhaust port, reaches drying purpose；For not
Containing water or material under the radiation of microwave, need to be added sensitizer and absorb energy, making in material can low-boiling point material volatilization
And discharged by exhaust port, achieve the purpose that dry.
In the present embodiment, decomposes section and be mainly made of furnace body, bell, burner hearth, thermal insulation material, temperature-measuring port etc..In furnace body two
Side is equipped with microwave feed-in mouth.
In specific embodiment, the high wave of inhaling in material absorbs microwave, the part formed a little is high up to thousands of degree in microwave field
Temperature, making material pyrolysis is small-molecule substance.
In the present embodiment, burning zone is by furnace body, bell, burner hearth, thermal insulation material, temperature-measuring port, open fire burning device, air inlet
The composition such as mouth, suction opening.
In specific embodiment, sensitizer reacts with fuel gas, forms furnace high-temperature, carries out high temperature to material and forges
It burns, is pyrolyzed the fuel gas of generation by the timely pilot combustion of open fire burning device, prevents fuel gas from accumulating in furnace and cause
It dodges quick-fried.
In the present embodiment, cooling section includes High-temperature cooling section, Slow cooling section and sub-cooled section, and cooling section is mainly by furnace
The composition such as body, bell, burner hearth, temperature-measuring port, air inlet and air outlet.
In specific embodiment, into cooling wind, top will preheat cooling wind extraction and import burning zone for the bottom of High-temperature cooling section
In furnace body；The cooling wind of preheating is imported preheating section into cooling wind, top by the bottom of sub-cooled section.
In the present embodiment, microwave incinerator body and burner hearth constitute the primary structure of entire incinerator theme, and pass through survey
Warm mouth tests each section of temperature.
In specific embodiment, furnace body is welded by heat-resistance stainless steel；Burner hearth is constituted using high temperature ceramic material saggar
One tunnel furnace chamber prevents corrosive goods confrontation furnace body from generating corrosion；Temperature-measuring port is connected with temperature sensor, for measuring each section
Real-time temperature in furnace chamber.
In specific embodiment, temperature sensor is thermocouple, and when temperature-measuring range is lower than 600 DEG C, protection sleeve pipe material is not
Become rusty steel, and when temperature-measuring range is higher than 600 DEG C, protection sleeve pipe material is silicon molybdenum tube.
In the present embodiment, the inlet and outlet of furnace body is equipped with microwave anti-leak real time warning device.
In specific embodiment, when the inlet and outlet microwave from leakage amount of furnace body is exceeded, automatic alarm.
In the present embodiment, microwave heating system is mainly made of multiple microwave sources and magnetron cooling water system.
In specific embodiment, the peak power output of each microwave source is 1KW, can be individually or more by electric control system controls
A starting, stopping；Magnetron cooling system uses water cooling, and independent cooling water all the way, including inlet valve is arranged in each magnetron
Flow switch is arranged by electric control system controls, water route in door, and no-cooling-water microwave cannot start.
In the present embodiment, electric-control system is by programmable controller (PLC), touch screen, temperature controller and other controls
Circuit composition processed.
Can be completed in specific embodiment, on touch screen parameters setting, display, warning message is shown and operating work
Energy.
In specific embodiment, warning message shows to include to have instruction function, overcurrent alarm, undercurrent to each magnetron
The function of alarm and overtemperature alarm.
In the present embodiment, automatic conveying system is made of automatic outer circulation transportation system and propulsion system.
In specific embodiment, automatic conveying system uses automatic hydraulic device, the running speed of adjustable systems, to guarantee
Reasonable process adjustments range；Automatic outer circulation is with carbon steel for main body support frame.
In the present embodiment, there are two zero-pressure control planes by setting for slow warming-up section and Slow cooling section.
In specific embodiment, the gas of slow warming-up section is flowed in eutral margin two sides point to both sides, low temperature side containing water vapor
More gas flow dryer sections, high temperature side multithread containing pyrolysis gas is to burning zone；Gas in slow cooling section is high in eutral margin two sides
Warm side gas flows to burning zone in furnace, cooks combustion adjuvant, and low temperature side gas passes through pipeline flow-direction preheating section outside furnace, preheating newly into
Material realizes energy conservation.
In specific embodiment, control the stabilization of two eutral margins by two induced draft fans, control pyrolysis fuel gas and
The olderly flowage of dry vapor.
In conclusion material is packed into saggar, power by mixing with sensitizer by means of above-mentioned technical proposal of the invention
Push rod pushes away people's charging cabin, successively passes through preheating, drying, heating, pyrolysis, burning, High-temperature cooling, slow cooling, sub-cooled, releases furnace
It is interior.The tail gas being discharged in dryer section is low temperature exhaust gas, and dry moisture or low-boiling point gas are discharged from here；High-temperature cooling section produces
Raw hot-air flows to burning zone from furnace as combustion adjuvant, and the hot-air that sub-cooled generates is transported to preheating from furnace Outer Tube
Section, to newly being preheated into material in furnace.
The present invention provides a kind of microwave catalysis incinerator, and it is insufficient to solve 1 conventional incinerator burning；2 conventional combustion furnaces
It cannot open and stop；3 energy consumptions are high, and tail is large-minded；The problem of 4 controllabilities difference.
Although specific embodiments of the present invention have been described above, those skilled in the art should be appreciated that this
It is merely illustrative of, various changes or modifications can be made to present embodiment, without departing from the principle and substance of the present invention,
Protection scope of the present invention is only limited by the claims that follow.
Claims (10)
1. microwave catalysis incinerator, which is characterized in that including by charging cabin, preheating section, dryer section, slow warming-up section, pyrolysis section,
Burning zone, cooling system, microwave heating system, electric-control system, discharging cabin, automatic conveying system composition, entire incinerator is by machine
Frame support.
2. microwave catalysis incinerator according to claim 1, which is characterized in that the charging cabin and discharging cabin are equipped with two
Road hermatic door, in charging or discharging, two seals door cannot be opened simultaneously, and maintain each section stable gas pressure distribution in furnace chamber.
3. microwave catalysis incinerator according to claim 1, which is characterized in that the preheating section is mainly by furnace body, furnace
The composition such as lid, burner hearth, thermal insulation material, high-temperature gas air inlet, temperature-measuring port, condensate water discharging mouth；Preheating section furnace body two sides
It is equipped with microwave feed-in mouth, connects microwave generator.
4. microwave catalysis incinerator according to claim 1, which is characterized in that the dryer section and decompose section mainly by
The composition such as furnace body, bell, burner hearth, thermal insulation material, temperature-measuring port, the dryer section and the furnace body two sides for decomposing section are equipped with microwave feed-in
Mouthful, connect microwave generator.
5. microwave catalysis incinerator according to claim 1, which is characterized in that the burning zone mainly by furnace body, bell,
The composition such as burner hearth, thermal insulation material, temperature-measuring port, open fire burning device, air inlet, suction opening；The open fire burning device is by outer confession
Liquefied gas or combustion of natural gas, guarantee furnace in generate organic combustible gas burn in time, prevent high concentration accumulation cause to dodge it is quick-fried.
6. microwave catalysis incinerator according to claim 1, which is characterized in that the cooling section include High-temperature cooling section,
Slow cooling section and sub-cooled section, cooling section is mainly by groups such as furnace body, bell, burner hearth, temperature-measuring port, air inlet and air outlets
At；The bottom of the High-temperature cooling section will preheat cooling wind extraction and import in burning zone furnace body into cooling wind, top；The low temperature
The cooling wind of preheating is imported preheating section into cooling wind, top by the bottom of cooling section.
7. according to claim 1 to microwave catalysis incinerator described in 6, which is characterized in that the furnace body is welded by heat-resistance stainless steel
It connects；The burner hearth constitutes a tunnel furnace chamber using high temperature ceramic material saggar, prevents corrosive goods confrontation furnace body from producing
Raw corrosion；The temperature-measuring port is connected with temperature sensor.
8. microwave catalysis incinerator according to claim 1, which is characterized in that the microwave heating system is mainly by microwave
Source and magnetron cooling water system composition, by electric control system controls；The magnetron cooling system uses water cooling；The automatically controlled system
System is made of programmable controller (PLC), touch screen, temperature controller and other control circuits；It can on the touch screen
To complete, parameters setting, display, warning message is shown and operating function.
9. microwave catalysis incinerator according to claim 1, which is characterized in that the automatic conveying system is followed by automatically outer
Ring transportation system and propulsion system composition, all use automatic hydraulic device, and the running speed of adjustable systems is reasonable to guarantee
Process adjustments range.
10. microwave catalysis incinerator according to claim 1, which is characterized in that the slow warming-up section and Slow cooling
For section by setting there are two zero-pressure control plane, zero-pressure control plane controls the stabilization of two eutral margins by two induced draft fans.
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| CN201910701153.1A CN110307547A (en) | 2019-07-31 | 2019-07-31 | Microwave catalysis incinerator |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112254510A (en) * | 2020-09-22 | 2021-01-22 | 山东义科节能科技股份有限公司 | Kiln wind path circulation system and kiln |
| CN113803978A (en) * | 2021-09-06 | 2021-12-17 | 昆明理工大学 | Automatic production system for continuously producing high-added-value metal |
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| CA2073213A1 (en) * | 1992-07-06 | 1994-01-07 | Won Sam Kim | Incinerator |
| US5397551A (en) * | 1992-07-09 | 1995-03-14 | Daesung Industrial Co., Ltd. | Incinerator |
| WO2015127699A1 (en) * | 2014-02-25 | 2015-09-03 | 北京建筑材料科学研究总院有限公司 | High-temperature pyrolysis experiment system and method therefor |
| CN106152144A (en) * | 2015-04-05 | 2016-11-23 | 南京凯盛国际工程有限公司 | Domestic waste incineration |
| CN206055638U (en) * | 2016-08-01 | 2017-03-29 | 北京北控环保工程技术有限公司 | For the cracking incinerator of waste process of endangering |
| CN106765172A (en) * | 2017-01-13 | 2017-05-31 | 安徽未名鼎和环保有限公司 | A kind of multi-chamber separating treatment refuse burning system |
| CN106838933A (en) * | 2017-01-24 | 2017-06-13 | 山东大学 | A kind of pyrolyzing sludge method of disposal being quenched based on microwave |
| CN109579554A (en) * | 2019-01-05 | 2019-04-05 | 黄冈市中洲安信窑炉有限公司 | Chemical catalyst calcining and decomposition gas burn all-in-one oven |
| CN211119362U (en) * | 2019-07-31 | 2020-07-28 | 深圳市弘玮环境技术有限公司 | Microwave catalytic incinerator |
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| CN112254510A (en) * | 2020-09-22 | 2021-01-22 | 山东义科节能科技股份有限公司 | Kiln wind path circulation system and kiln |
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