CN106352344A - Magnetized rubbish pyrolysis station - Google Patents
Magnetized rubbish pyrolysis station Download PDFInfo
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- CN106352344A CN106352344A CN201611006444.1A CN201611006444A CN106352344A CN 106352344 A CN106352344 A CN 106352344A CN 201611006444 A CN201611006444 A CN 201611006444A CN 106352344 A CN106352344 A CN 106352344A
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- pyrolysis
- furnace body
- rubbish
- tank
- furnace
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- 238000000197 pyrolysis Methods 0.000 title claims abstract description 78
- 239000010813 municipal solid waste Substances 0.000 title abstract description 24
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 55
- 230000005415 magnetization Effects 0.000 claims abstract description 16
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Substances [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 claims abstract description 13
- 230000007246 mechanism Effects 0.000 claims abstract description 10
- 239000002131 composite material Substances 0.000 claims abstract description 7
- 229910052697 platinum Inorganic materials 0.000 claims abstract description 7
- 229910000831 Steel Inorganic materials 0.000 claims abstract description 4
- 239000010959 steel Substances 0.000 claims abstract description 4
- 238000009833 condensation Methods 0.000 claims description 17
- 230000005494 condensation Effects 0.000 claims description 17
- 230000003028 elevating effect Effects 0.000 claims description 8
- 239000011248 coating agent Substances 0.000 claims description 6
- 238000000576 coating method Methods 0.000 claims description 6
- 239000003063 flame retardant Substances 0.000 claims description 6
- RNFJDJUURJAICM-UHFFFAOYSA-N 2,2,4,4,6,6-hexaphenoxy-1,3,5-triaza-2$l^{5},4$l^{5},6$l^{5}-triphosphacyclohexa-1,3,5-triene Chemical compound N=1P(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP=1(OC=1C=CC=CC=1)OC1=CC=CC=C1 RNFJDJUURJAICM-UHFFFAOYSA-N 0.000 claims description 5
- 238000009413 insulation Methods 0.000 claims description 5
- 229910052761 rare earth metal Inorganic materials 0.000 claims description 5
- 150000002910 rare earth metals Chemical class 0.000 claims description 4
- 235000019504 cigarettes Nutrition 0.000 claims description 3
- 239000000779 smoke Substances 0.000 abstract description 8
- 239000000428 dust Substances 0.000 abstract description 3
- 238000004519 manufacturing process Methods 0.000 abstract description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 22
- 239000003546 flue gas Substances 0.000 description 22
- 238000004056 waste incineration Methods 0.000 description 7
- 230000000694 effects Effects 0.000 description 5
- 238000005516 engineering process Methods 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- 239000007789 gas Substances 0.000 description 4
- 230000008569 process Effects 0.000 description 4
- 238000012545 processing Methods 0.000 description 3
- 239000002910 solid waste Substances 0.000 description 3
- 238000005979 thermal decomposition reaction Methods 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 230000005183 environmental health Effects 0.000 description 2
- 238000002309 gasification Methods 0.000 description 2
- 239000005416 organic matter Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 206010019233 Headaches Diseases 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 230000002159 abnormal effect Effects 0.000 description 1
- 239000006096 absorbing agent Substances 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000009264 composting Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 230000009977 dual effect Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005367 electrostatic precipitation Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000000796 flavoring agent Substances 0.000 description 1
- 235000019634 flavors Nutrition 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 231100000869 headache Toxicity 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000004531 microgranule Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000032696 parturition Effects 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000002195 soluble material Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 239000002351 wastewater 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
-
- 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
- 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
-
- 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
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2201/00—Pretreatment
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2201/00—Pretreatment
- F23G2201/30—Pyrolysing
-
- 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
-
- 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)
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Processing Of Solid Wastes (AREA)
- Treating Waste Gases (AREA)
Abstract
The invention discloses a magnetized rubbish pyrolysis station. The magnetized rubbish pyrolysis station comprises a pyrolysis furnace, a feeding mechanism and a control cabinet. The magnetized rubbish pyrolysis station is characterized in that a condensate water tank, a water bath tank, a demisting tank, a plasma dust and smell removal tank and a secondary pyrolysis chamber are sequentially installed on a smoke exhaust pipeline of the pyrolysis furnace, a turbulent flow tube is arranged in a furnace body of the pyrolysis furnace, an insulating layer and a fireproof layer are arranged on the inner wall of the furnace body, and a high-platinum composite magnetization wall is arranged on the outer wall of the furnace body; the condensate water tank is arranged on the top of the furnace body of the pyrolysis furnace, the demisting tank is a tank internally provided with multiple PVC plates, and the secondary pyrolysis chamber is a tank internally provided with multiple steel plates. The magnetized rubbish pyrolysis station is simple in structure, low in production cost and running time and convenient to use; when rubbish is incinerated, no dense smoke is generated, harmful gas in the smoke can be effectively removed, the smoke generated when the rubbish is incinerated is effectively purified, no serious secondary pollution is caused to the atmosphere any more, and emission of the smoke reaches national relevant standards.
Description
Technical field
The present invention relates to refuse treatment plant, specially a kind of magnetization that can more preferably purify flue gas produced by waste incineration
Refuse pyrolysis station.
Background technology
Yield with the high speed development of China's city-building and new countryside construction, house refuse increases increasingly, directly fills out
Bury and not only expend substantial amounts of transport capacity, and the land resource of the preciousness that accounts for, allow the seepage of sewage and smelly of people's headache the most
The evaporation of gas, the world is all contaminated, not only causes harm current, and leaves troubles to descendants.
Rural area and suburb are directly burned using dispersion in refuse bin, and often black smoke billows, and air is caused with serious dirt
Dye.For above-mentioned situation, country has put into substantial amounts of manpower financial capacity, and the process to house refuse has carried out long-term and unremitting scientific research
With the dual effort of enforcement aspect, consumer waste incineration the facility for generating electricity are established in tier 2 cities.But it is big
The more advanced Domestic garbage treatment equipment of type is substantially although can normally run from the technology introduced Europe, the United States, day, but
Construction investment is big, operating cost high it is difficult to popularity.The domestic technical scheme capturing house refuse is varied, has and is giving birth to
Add coal, oil, vapour directly to burn in rubbish alive, have and house refuse is processed into charcoal shape granule, have gasification furnace on probation to locate
Reason rubbish etc..Or these technology are investment, and excessive, operating cost is high, or being that technology is immature, being not normally functioning.Cause
And the house refuse overwhelming majority of China or the original processing method using directly landfill or directly burning, but directly fill meeting
Land occupation resource, directly burns and often black smoke can billow and produce a large amount of harmful gass again, if not dealt carefully with, can be right
Air causes serious secondary pollution.
Content of the invention
The invention reside in providing a kind of magnetization refuse pyrolysis station that can more preferably purify flue gas produced by waste incineration, to solve
The certainly shortcoming in the presence of background technology and deficiency.
Technical problem solved by the invention employs the following technical solutions to realize:
A kind of magnetization refuse pyrolysis station, including pyrolysis oven, feed mechanism, switch board it is characterised in that the flue gas of described pyrolysis oven
Condensation water tank, water bath are sequentially installed with discharge tube, remove fog chamber, plasma dedusting deodouring case, secondary pyrolysis chamber, described heat
The furnace interior of solution stove is provided with turbulated tube, and turbulated tube porch is provided with a rare earth permanent magnet magnetizator, inboard wall of furnace body surrounding
It is provided with heat-insulation layer and flame retardant coating, furnace body outer wall surrounding is provided with high platinum composite magnetization wall, described condensation water tank is arranged
Connect in the top of pyrolysis furnace body and with space in pyrolysis furnace body, and connected with water bath by pipeline, described demisting
Case is the casing of closing, and box house is provided with polylith pvc plate, the two ends of casing pass through pipeline respectively with water bath and plasma
Dedusting deodouring case connects, and described secondary pyrolysis chamber is the casing being internally provided with plurality of steel plates.
For the present invention, the top of described pyrolysis oven is provided with a poly- petticoat pipe connecting with space in pyrolysis furnace body,
Condensation water tank is arranged at the top of poly- petticoat pipe and is connected with poly- petticoat pipe.
For the present invention, described feed mechanism is mainly made up of charging barrel, charging barrel running track and elevating hopper, described
Charging barrel the side of pyrolysis oven is installed on by bracket and is connected with pyrolysis oven top by pipeline.
For the present invention, described water bath is further equipped with water pump, and the work for water bath provides water under high pressure.
Beneficial effect: present configuration is simple, and production cost is low with operating cost, easy to use, by each technological means,
Make waste incineration not only will not produce thick smoke, and the harmful gass in flue gas effectively can be removed, and the cigarette producing
Gas is not in serious abnormal flavour and stink, has accomplished the effective purification to flue gas produced by waste incineration, no longer to air
Cause serious secondary pollution, make the discharge of flue gas reach relevant national standard.
Brief description
Fig. 1 is the forward sight perspective view of the present invention；
Fig. 2 is the rear perspective structural representation of the present invention；
Fig. 3 is the perspective view of the pyrolysis oven of the present invention.
In figure: 1- pyrolysis oven, 2- switch board, 3- condensation water tank, 4- water bath, 5- removes fog chamber, 6- plasma dedusting taste removal
Case, bis- pyrolysis chambers of 7-, 8- turbulated tube, 9- turbulent flow valve, 10- rare earth permanent magnet magnetizator, 11- heat-insulation layer, 12- flame retardant coating, 13- is high
Platinum composite magnetizes wall, the poly- petticoat pipe of 14-, 15- charging barrel, 16- running track, 17- elevating hopper, 18- bracket, 19- delivery pipe
Road.
Specific embodiment
Below in conjunction with the accompanying drawings the specific embodiment of the present invention is described in detail as follows:
Referring to shown in accompanying drawing 1-3, one kind magnetizes refuse pyrolysis station, and including pyrolysis oven 1, feed mechanism, switch board 2, its feature exists
In, the flue gas exhausting pipe line 19 of described pyrolysis oven is sequentially installed with condensation water tank 3, water bath 4, remove fog chamber 5, plasma dedusting
Deodouring case 6, secondary pyrolysis chamber 7, the specific structural features of each part and its function are as follows:
Pyrolysis oven: as shown in Figure 3, the furnace interior of described pyrolysis oven is provided with turbulated tube 8, and the porch of turbulated tube is provided with
In order to control the turbulent valve 9 of turbulated tube switch, turbulated tube porch is provided with a rare earth permanent magnet magnetizator 10, inboard wall of furnace body four
It is provided with heat-insulation layer 11 and flame retardant coating 12 week, furnace body outer wall surrounding is provided with high platinum composite magnetization wall 13, the top of pyrolysis oven
Portion is provided with a poly- petticoat pipe 14 connecting with space in pyrolysis furnace body.Pyrolysis furnace bottom need to raise certain altitude.Turbulated tube
Effect be during waste incineration, open turbulent valve, make to produce oxygen uptake phenomenon in body of heater, and produce turbulent flow in body of heater
Air-flow, make the speed of waste incineration with hgher efficiency.The effect of rare earth permanent magnet magnetizator is to enter the air sucking from turbulated tube
Row magnetization, passes in pyrolysis oven that a small amount of (effect that high platinum composite magnetizes wall is also by furnace air through magnetized air
And rubbish suitably magnetizes, high platinum composite magnetization wall is fixed on pyrolysis furnace body by screw), make processed solid waste
In combustible and pyrolysis produce the burning of combustible part, produced heat is that organic substance in solid waste carries out continuing
Thermal decomposition, because magnetic air makes treated object Indirect magnetization, reduces the required energy of pyrolysis, improve pyrolysis efficiency thus
Pyrolytic gasification can be realized in a low temperature of 350 DEG C, thus substantially avoid the generation of two English.Flame retardant coating is arranged in body of heater
Outermost, prevents furnace high-temperature from leading to body of heater deformation even to be melted, heat-insulation layer is then arranged between flame retardant coating and furnace body wall, can
With incineration temperature in effective holding furnace.The effect of poly- petticoat pipe is then to be assembled burning the rising flue gas producing and entered condensation
In water tank.
The operation principle of pyrolysis oven: rubbish is poured in garbage pyrolysis furnace, is ignited in rubbish furnace bottom with combustible.Each
Under conditions of barometric damper is opened, produce oxygen uptake phenomenon in organic matter rubbish pyrolytic process in cavity, air is through oxygen-adding tube
Road magnetization enters combustion-supporting in rubbish thermal decomposition chamber and produces turbulent flow, accelerates the thermal decomposition of organic matter rubbish.
Feed mechanism: described feed mechanism is mainly made up of charging barrel 15, charging barrel running track 16 and elevating hopper 17,
Charging barrel is installed on the side of pyrolysis oven by bracket 18 and is connected with pyrolysis oven top by pipeline.Rubbish is put into pyrolysis oven
When inside being burned, first rubbish is poured in charging barrel, then start the motor being connected with feed mechanism, charging barrel is electronic
Under the traction of machine, it is lifted up along its dynamic row track, when charging barrel rises to elevating hopper position, automatically the rubbish in bucket is fallen
Enter in elevating hopper, elevating hopper passes through pipeline again and sends into rubbish in pyrolysis oven, is provided with this pipeline and the connector of pyrolysis oven
Switch, during pyrolysis oven work, this opening is in closure state.Meanwhile, the rubbish in elevating hopper can be by inclination
Pipeline freely falling body enters pyrolysis oven it is also possible to be pushed in pyrolysis oven by hydraulic cylinder by parallel pipeline.
Switch board: switch board, in order to control the operation of feed mechanism and whole equipment, is connected with each part by circuit
And each part is implemented with operation operation.
Flue gas exhausting pipe line: flue gas exhausting pipe line is closed conduit, and corrosion-resistant and high-temperature resistant, is sequentially connected condensed water
Case, water bath, remove fog chamber, plasma dedusting deodouring case, secondary pyrolysis chamber, the junction of pipeline and each part adopts flange closure
Connect it is ensured that flue gas will not leak outside in each junction.
Condensation water tank: described condensation water tank is using common conventional common condensation water tank on the market.Condensation water tank is arranged
In the top of pyrolysis furnace body, its one end is connected with space in pyrolysis furnace body by poly- petticoat pipe, and the other end passes through pipeline and water
Bath cabinet connects.Condensation water tank, built with water body, burns the flue gas producing and enters from one end of condensation water tank, and the other end is discharged and passed through
Pipeline enters in water bath, and in the process, the water body of condensation water tank is lowered the temperature to burning the high-temperature flue gas producing, simultaneously right
In flue gas, water-soluble material carries out absorption cleaning.
Water bath: described water bath adopts common conventional common water bath on the market, water bath, equipped with water pump, is
The work of water bath provides water under high pressure.Water under high pressure purifies to material soluble in water in flue gas, simultaneously to the sulfur in flue gas
The harmful substances such as phosphorus are absorbed, and reach the effect of double purification flue gas.The installation site of water bath is less than condensation water tank position.
Except fog chamber: the described casing being closing except fog chamber, box house is provided with polylith pvc plate, and the two ends of casing lead to
Piping is connected with water bath and plasma dedusting deodouring case respectively.Pvc plate attracts the water spray haze in flue gas, and flue gas is carried out only
Change.
Plasma dedusting deodouring case: described dedusting deodouring case, built with forceful electric power pole, can produce highfield, and highfield makes dust
Particle charge, when it passes through electrodes for removing dust, the microgranule with positive/negative electric charge is adsorbed by positive negative battery lead plate respectively, that is, reach to cigarette
Gas carries out dedusting purpose.
Secondary pyrolysis chamber: described secondary pyrolysis chamber is the casing being internally provided with plurality of steel plates.Secondary pyrolysis chamber passes through
Pipeline is in parallel with the discharge duct of pyrolysis oven, and carries out secondary pyrolysis to through the flue gas that multiple working procedure is changed after net, after purifying
Flue gas enters in air after being pyrolyzed again.
The present invention is using more advanced technological process: the vertical heater+pyrolysis chamber that feeds intake/be pyrolyzed+flue gas forced cooling device+water
Bath treatment box+packed absorber+electrostatic precipitation+secondary pyrolysis+microwave purifying device+activated carbon adsorption chimney.Garbage disposal rate
Reach 95%, do not produce waste water, do not produce waste residue (the harmless grit after a small amount of high temperature), energy consumption is low, not miserable fuel, gas discharge reaches
To national standard.
Product purpose: the composting that unit is voluntarily collected is produced by environmental health collect or house refuse.Can be straight
Tap into and carry out pyrolysis processing into rubbish heat treatment station.By environmental health collect clothing processing, food processing and other
For the property of the industry generation of the urban life service general industrial solid waste close with house refuse.
Ultimate principle and principal character and the advantages of the present invention of the present invention have been shown and described above.The skill of the industry
Art personnel it should be appreciated that the present invention is not restricted to the described embodiments, without departing from the spirit and scope of the present invention, this
Invention also has various changes and modifications, and these changes and improvements both fall within claimed scope.The guarantor of application claims
Shield scope is by appending claims and its equivalent thereof.
Claims (4)
1. a kind of magnetization refuse pyrolysis station, including pyrolysis oven, feed mechanism, switch board it is characterised in that the cigarette of described pyrolysis oven
Condensation water tank, water bath are sequentially installed with gas discharge tube, remove fog chamber, plasma dedusting deodouring case, secondary pyrolysis chamber, described
The furnace interior of pyrolysis oven is provided with turbulated tube, and turbulated tube porch is provided with a rare earth permanent magnet magnetizator, inboard wall of furnace body four
It is provided with heat-insulation layer and flame retardant coating week, furnace body outer wall surrounding is provided with high platinum composite magnetization wall, described condensation water tank sets
It is placed in the top of pyrolysis furnace body and connects with space in pyrolysis furnace body, and connected with water bath by pipeline, described removes
Fog chamber is the casing of closing, and box house is provided with polylith pvc plate, the two ends of casing pass through pipeline respectively with water bath and wait from
Sub- dedusting deodouring case connection, described secondary pyrolysis chamber is the casing being internally provided with plurality of steel plates.
2. a kind of magnetization refuse pyrolysis station according to claim 1 is it is characterised in that the top of described pyrolysis oven is provided with
One poly- petticoat pipe connecting with space in pyrolysis furnace body, condensation water tank is arranged at the top of poly- petticoat pipe and is connected with poly- petticoat pipe.
3. a kind of magnetization refuse pyrolysis station according to claim 1 is it is characterised in that described feed mechanism is mainly by upper
Charging basket, charging barrel running track and elevating hopper are constituted, and described charging barrel is installed on the side of pyrolysis oven by bracket and passes through
Pipeline is connected with pyrolysis oven top.
4. a kind of magnetization refuse pyrolysis station according to claim 1 is it is characterised in that described water bath is further equipped with water
Pump, the work for water bath provides water under high pressure.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611006444.1A CN106352344A (en) | 2016-11-16 | 2016-11-16 | Magnetized rubbish pyrolysis station |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611006444.1A CN106352344A (en) | 2016-11-16 | 2016-11-16 | Magnetized rubbish pyrolysis station |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106352344A true CN106352344A (en) | 2017-01-25 |
Family
ID=57862673
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201611006444.1A Pending CN106352344A (en) | 2016-11-16 | 2016-11-16 | Magnetized rubbish pyrolysis station |
Country Status (1)
| Country | Link |
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| CN (1) | CN106352344A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113210395A (en) * | 2021-03-16 | 2021-08-06 | 杭州三得农业科技有限公司 | Ultra-large type intermediate frequency sintering household garbage treatment system and process flow thereof |
| WO2023167581A1 (en) * | 2022-03-01 | 2023-09-07 | Nano Silver Manufacturing Sdn Bhd | A thermal decomposition reactor for decomposing waste material and a thermal decomposition system |
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| WO2009015575A1 (en) * | 2007-07-27 | 2009-02-05 | Zefeng Chen | Double-loop double-pyrogenation incinerator for garbage harmless treatment and its usage method |
| CN205579579U (en) * | 2015-11-13 | 2016-09-14 | 陈树华 | Heat energy refuse treatment machine |
| CN106152143A (en) * | 2016-08-17 | 2016-11-23 | 湖南润漠环保科技发展有限公司 | One way of life rubbish magnetization pyrolysis treating stations |
| CN106196086A (en) * | 2016-09-21 | 2016-12-07 | 北京迅洁环保科技有限公司 | One way of life garbage pyrolysis furnace |
| CN206207423U (en) * | 2016-11-16 | 2017-05-31 | 株洲仁仁研环保研究所有限公司 | One kind magnetization refuse pyrolysis station |
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2016
- 2016-11-16 CN CN201611006444.1A patent/CN106352344A/en active Pending
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| WO2009015575A1 (en) * | 2007-07-27 | 2009-02-05 | Zefeng Chen | Double-loop double-pyrogenation incinerator for garbage harmless treatment and its usage method |
| CN205579579U (en) * | 2015-11-13 | 2016-09-14 | 陈树华 | Heat energy refuse treatment machine |
| CN106152143A (en) * | 2016-08-17 | 2016-11-23 | 湖南润漠环保科技发展有限公司 | One way of life rubbish magnetization pyrolysis treating stations |
| CN106196086A (en) * | 2016-09-21 | 2016-12-07 | 北京迅洁环保科技有限公司 | One way of life garbage pyrolysis furnace |
| CN206207423U (en) * | 2016-11-16 | 2017-05-31 | 株洲仁仁研环保研究所有限公司 | One kind magnetization refuse pyrolysis station |
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