CN106152143A - One way of life rubbish magnetization pyrolysis treating stations - Google Patents
One way of life rubbish magnetization pyrolysis treating stations Download PDFInfo
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- CN106152143A CN106152143A CN201610682772.7A CN201610682772A CN106152143A CN 106152143 A CN106152143 A CN 106152143A CN 201610682772 A CN201610682772 A CN 201610682772A CN 106152143 A CN106152143 A CN 106152143A
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- pyrolysis
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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
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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
- F23J15/04—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material using washing fluids
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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
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Treating Waste Gases (AREA)
Abstract
The invention discloses one way of life rubbish magnetization pyrolysis treating stations, it relates to rubbish magnetization pyrolysis art, connect on Water spray purifying box and have spray header, and be connected by spray header and the second external water tank, by the second delivery pump circulation pumping spray cleaning water, the two ends of air-introduced machine are straight-through with the level of the outlet flue of Water spray purifying box and smog diversion three-way respectively to be connected, 90 degree of threeways of smog diversion three-way are connected with water smoke treatment box, tail gas terminal processing system is set on water smoke treatment box, tail gas terminal processing system is connected with activated carbon adsorption chimney by flue gas pipeline, gas after purified treatment is discharged by activated carbon adsorption chimney.Magnetization gas flow and the flow controlling pyrolysis smoke that it is entered by regulation air magnetizator control refuse pyrolysis temperature, avoid producing two English, the flue gas that pyrolysis produces is through forcing smoke abatement tar removing and tail gas terminal processes to reclaim clarifying smoke gas, and remaining gas is discharged by blowdown stack.
Description
Technical field:
The present invention relates to one way of life rubbish magnetization pyrolysis treating stations, belong to rubbish magnetization pyrolysis technical field.
Background technology:
The yield of China's city-building and the high speed development of new countryside construction, house refuse increases increasingly, and directly landfill is not
Only expending substantial amounts of transport capacity, and account for land resource, effluent seepage and the evaporation of foul smell that landfill waste produces not only are caused harm
Currently, and leave troubles to descendants；Rural area and suburb, cities and towns use dispersion directly to burn in garbage pool, and the harmful smoke of generation is without place
Reason, causes severe contamination to air；For above-mentioned situation, country the process of house refuse has been carried out long-term and unremitting scientific research with
Dual effort in terms of enforcement, has established consumer waste incineration the facility for generating at a tier 2 cities, but large-scale
More advanced Domestic garbage treatment equipment substantially from the external technology introduced, although can be properly functioning, but build and throw
Money is big, and operating cost is high, it is difficult to popularity；The domestic technical scheme capturing house refuse is varied, has in house refuse
In processing procedure, addition coal, oil, vapour directly burn, and have and house refuse is processed into charcoal shape granule, have gasification furnace on probation
Process rubbish etc., these technology or be that investment is excessive, operating cost is high, or be that technology is immature, be not normally functioning,
Thus the original processing method that the house refuse overwhelming majority of China or employing directly fill or directly burn.
Summary of the invention:
For the problems referred to above, the technical problem to be solved in the present invention is to provide one way of life rubbish magnetization pyrolysis treating stations.
The present invention one way of life rubbish magnetization pyrolysis treating stations, it comprise feed arrangement, tank bracket, electric apparatus control apparatus,
Magnetization pyrolysis processing furnace body, pyrolysis smoke forced condensation case, water inlet pipe and water outlet pipe, the first external water tank, the first delivery pump, support
Frame, Water spray purifying box, spray header, the second external water tank, the second delivery pump, air-introduced machine, smog diversion three-way, water smoke process
Case, tail gas terminal processing system, flue gas pipeline, activated carbon adsorption chimney, feed arrangement is by lifting material feeder and horizontal helical
Rotation conveyer device composition, the side, lower section of feed arrangement is provided with tank bracket, is provided with electric apparatus control apparatus, feed arrangement in tank bracket
Lower section opposite side be provided with magnetization pyrolysis processing furnace body, magnetization pyrolysis processing furnace body be provided with pyrolysis smoke forced condensation
Case, pyrolysis smoke forced condensation case connects and has water inlet pipe and water outlet pipe and the first external water tank to be connected, water inlet pipe and water outlet pipe is provided with first
Delivery pump circulating pump, by the cooling water needed for the first delivery pump circulation pumping flue gas condensing, pyrolysis smoke forced condensation case
Lower section is provided with bracing frame, and pyrolysis smoke forced condensation case is connected with Water spray purifying box by flue gas pipeline, and Water spray purifies
Connect on case and have spray header, spray header is provided with the second external water tank, and by spray header and the second external water tank
Be connected, by the second delivery pump circulation pumping spray cleaning water, the two ends of air-introduced machine respectively with the smoke of Water spray purifying box
Mouth is straight-through with the level of smog diversion three-way to be connected, and 90 degree of threeways of smog diversion three-way are connected with water smoke treatment box, at water smoke
Setting tail gas terminal processing system on reason case, tail gas terminal processing system is connected with activated carbon adsorption chimney by flue gas pipeline, warp
Cross the gas after purified treatment to be discharged by activated carbon adsorption chimney, the operation principle of described house refuse magnetization pyrolysis treating stations
It is pyrolyzed in being transported to magnetize pyrolysis processing furnace body by the house refuse after simple sorting for: feed arrangement, pyrolysis
The harmful gas and the steam that produce make the tar in pyrolysis smoke, steam, dust through pyrolysis smoke forced condensation case, have
Evil gas separate, subsequently into Water spray purifying box, Water spray purifying box can play pyrolysis smoke is carried out chalk dust removing, cooling,
Waste gas absorption, the purpose of purification gas, then waste gas enters water smoke treatment box, and water smoke treatment box can effectively retain in waste gas
Water smoke, reduces waste gas water content, alleviates the operating pressure of follow-up tail gas terminal system, and last flue gas enters tail gas terminal processes
System, tail gas terminal processing system, in the pyrolysis tail gas after forced condensation excessively, Water spray purification, water smoke process, remains on a small quantity
Discharge thing the most up to standard finally process.
As preferably, described magnetization pyrolysis processing furnace body be internally provided with a circular refractory burner hearth, circular resistance to
The outer wrap of stove thorax has heat-insulation magnetic wall, and magnetize pyrolysis processing furnace body is provided above the octahedra poly-petticoat pipe of taper,
And fixed by several screws, the top of the octahedra poly-petticoat pipe of taper is provided with flue gas through flange pipe, and by several bolts
Fixing, magnetization pyrolysis processing furnace body is connected with pyrolysis smoke forced condensation case by flue gas through flange pipe, magnetization pyrolysis
Processing and be provided with several regulation turbulent flow valve on the bottom of furnace body, regulation turbulent flow valve is with permanent magnetism air magnetizator by screw thread even
Connect, be connected by screw threads for fastening between permanent magnetism air magnetizator with the turbulent fire grate within magnetization pyrolysis processing furnace body, magnetization
The bottom surrounding of pyrolysis processing furnace body is respectively provided with a deashing fire door, is added by rubbish in use in circular refractory burner hearth,
Ignite in deashing fire door with combustible, under conditions of each regulation turbulent flow valve is opened, organic matter rubbish pyrolytic process in burner hearth
Middle generation oxygen uptake phenomenon, permanent magnetism air magnetizator magnetic air passes through combustion-supporting in turbulent flow fire grate enters burner hearth and produces turbulent flow, adding
The thermal decomposition of speed organic matter rubbish, described circular refractory burner hearth is made up of refractory brick or refractory cement, and its effect is for rubbish
Rubbish pyrolysis provides the space of resistance to uniform temperature, and the outside of described heat-insulation magnetic wall is provided with heat-insulation layer, and heat-insulation layer is by several
Rivet is fixed on magnetization pyrolysis processing furnace body, and heat-insulation magnetic wall is made up of refractory cement and permanent magnet, and its effect is magnetic
Changing air and organic substance and have heat insulation function concurrently, described permanent magnetism air magnetizator is by not magnetic conduction hollow pipe and a permanent magnet
Composition, hollow pipe cylindrical two ends are screw thread, and one end of permanent magnet not homopolarity is placed in hollow pipe at a distance of 10 millimeters, permanent magnetism air
Magnetizator refers to the magnetized a kind of parts of air, passes to a small amount of through magnetized air in pyrolysis oven, and the part remaining stable is fired
Burning, make the combustible in the solid waste being processed and pyrolysis produce the burning of combustible part, produced heat is that solid gives up
Organic substance in thing persistently thermally decomposes, owing to magnetic air makes treated object Indirect magnetization, needed for reducing pyrolysis
Energy, thus pyrolysis can realize at a temperature of 350-550 DEG C, improves pyrolysis efficiency, thus be substantially reduced two English and generate
Amount, decreases tail gas clean-up difficulty.
As preferably, the inside of described pyrolysis smoke forced condensation case is provided with condenser pipe and flue gas streams dividing plate, cold
Solidifying pipeline is provided with spoiler, and a side bottom of pyrolysis smoke forced condensation case is provided with smoke inlet, pyrolysis smoke forced condensation
The opposite side top of case is provided with the first outlet flue, and the opposite side bottom of pyrolysis smoke forced condensation case is provided with blowoff valve, institute
The condenser pipe stated uses pipe to make, and its effect is supercooled water；Flue gas streams dividing plate and uses steel plate to make, and its effect is point
Layer separates the space in casing, makes pyrolysis smoke pass through according to the route of design；Spoiler is the metal of square central band circular hole
Plate, its effect is that flow-disturbing increases resistance, increases the contact area of cooled flue gas；Smoke inlet is the design of hollow flange coil structures, its
Effect is to allow pyrolysis smoke enter in cooling cylinder；One end of outlet flue is welded with the steel pipe of adpting flange, and its effect is smoke；Row
Dirty valve is ball valve design, and its effect is the fluid controlling to produce through forced condensation.
As preferably, described Water spray purifying box be internally provided with the first flow-disturbing dividing plate, and by the first flow-disturbing every
The inside of Water spray purifying box is divided into except mist layer and packing layer by plate, and packing layer is provided with several atomizer, several mists
Changing shower nozzle to be connected with several spiral nozzles by pipeline, several spiral nozzles are arranged in screw spraying pipeline, screw spraying pipe
Being provided with several observation window on road, one end of screw spraying pipeline is connected with Water spray purifying box, another of screw spraying pipeline
Holding and be connected with absorption pipeline, be provided with choked flow adsorption layer in absorption pipeline, one end of absorption pipeline connects abutted flange, and water sprays
Drench purifying box is provided above access panel, and the side of Water spray purifying box is provided with the second outlet flue, Water spray purifying box
Lower section is provided with several first blowdown window, Water spray purifying box by the connection of connecting pipeline and the second external water tank, described the
The effect of one flow-disturbing dividing plate is to change gas-liquid direction；Except mist layer and packing layer are all a kind of fillers, its effect be to increase respectively with
The contact of flue gas, retains water smoke in flue gas and increases contacting of flue gas and absorbing liquid；Atomizer and the effect of spiral nozzle
It is to spray absorbing liquid；Screw spraying pipeline is a kind of spiral pipeline of inside cavity, and its effect is to increase flue gas and absorption
The contact of liquid；Absorption pipeline is a kind of hollow pipe, and its effect was flue gas；Choked flow adsorption layer is a kind of filler, and its effect is
Increase resistance, increase the contact area of flue gas；Outlet flue refers to the pipeline of band adpting flange, and its effect is waste gas exhaust outlet.
As preferably, described smog diversion three-way is to be led directly to and a hollow barrel by a level being positioned at center
90 degree of threeway compositions of the two pieces at pipe and two ends, the two ends of hollow barrel pipe are respectively arranged with flange capping, and are bolted solid
Fixed, 90 degree of threeways of two pieces are connected with water smoke treatment box respectively by flange.
As preferably, described water smoke treatment box is by circular inlet flange, Pall ring filler foam-removing layer, vortex-flow and defrosting
Layer, the second flow-disturbing dividing plate, square flange of giving vent to anger, the second blowdown window, maintenance window, casing composition, circular inlet flange is positioned at casing
Top side, Pall ring filler foam-removing layer and vortex-flow and defrosting layer are positioned at the inside of casing, the second flow-disturbing dividing plate separate, square
Flange of giving vent to anger is positioned at the top side of vortex-flow and defrosting layer upper box body, and described circular inlet flange is air inlet, its effect
It is that waste gas enters from entrance；Pall ring filler foam-removing layer is a kind of filler, and its effect is to increase the contact surface with waste gas, retains useless
Foam in gas；Vortex-flow and defrosting layer is rotational flow plate defroster, and its effect is to utilize the function and rotation that spiral board change axial flow is eddy flow
The raw centrifugal force of miscarriage carries out except mist, except under droplet flow down along plate face periphery；The effect of the second flow-disturbing dividing plate is that flow-disturbing changes
Exhaust gas direction；Square flange of giving vent to anger is waste gas outlet, and its effect is the outlet of the waste gas after retaining except mist.
As preferably, described tail gas terminal processing system be by honeycomb fashion cooking fume remover, photodissociation formula cooking fume remover,
Secondary pyrolysis heater, electrostatic field case, the first flue gas pipeline and the second flue gas pipeline composition, honeycomb fashion cooking fume remover is arranged on
In electrostatic field case, electrostatic field case is arranged on square gives vent to anger on flange, electrostatic field case is provided with the first flue gas pipeline bolt and fixes
Being communicated to photodissociation formula cooking fume remover, photodissociation formula cooking fume remover is pyrolyzed by the fixing secondary that is communicated to of the second flue gas pipeline bolt
Heater；During high-voltage electrostatic field, under the effect of high voltage electric field, soot gas ionizes, and mist of oil is charged, and major part is degraded charcoal
Changing, small part oil or fat particles moves to the positive/negative plate of electric field under the electric field force and airflow function of absorption electric field and is collected in pole
Flowing to draw-off tray on plate and under the effect of self gravitation, discharge through oil drain passage, remaining micron order mist of oil is degraded by electric field
Becoming carbon dioxide and water, simultaneously under the effect of high tension generator, in electric field, air produces ozone, eliminates major part in flue gas
Abnormal smells from the patient, by the gas after static electric field process by flue gas pipeline enter photodissociation formula cooking fume remover, at Ultraviolet-C wave band
The lower strand changing tail gas oil of the effect of light, produces ozone with after oxygen reaction simultaneously, and ozone is by cold for oil molecule burning
Rear generation water and ozone, the abnormal flavour in flue gas eliminates the most therewith simultaneously, and the tail gas after process is entered secondary pyrolysis by flue gas pipeline
Heater, its operating temperature of electric heating control is used for post bake at 1000-1200 DEG C and gas residence time (about 3 seconds), high
Temperature removes harmful gas in flue gas, and the effect of described honeycomb fashion cooking fume remover is electrostatic precipitation degasification taste；Photodissociation formula oil smoke
The effect purified is that deodorization eliminates the unusual smell；The effect of secondary pyrolysis heater is to remove harmful gas in flue gas by high temperature；Electrostatic
The effect of field case is to place honeycomb fashion cooking fume remover；
As preferably, the inside of described activated carbon adsorption chimney is filled with activated carbon, and activated carbon adsorption chimney is arranged on
The side of secondary pyrolysis heater, activated carbon adsorption chimney and secondary pyrolysis heater are supported fixing by bracing frame.
Beneficial effects of the present invention: the magnetization gas flow that it is entered by regulation air magnetizator and control pyrolysis smoke
Flow control refuse pyrolysis temperature, it is to avoid producing two English, the flue gas that pyrolysis produces is through forcing smoke abatement tar removing and tail
Gas terminal processes reclaims clarifying smoke gas, and remaining gas is discharged by blowdown stack, uses house refuse to burn house refuse
Form, once lights a fire, and need not add any fuel, and low cost is taken up an area little, and Operation and Maintenance maintenance is simple, and pyrolysis decrement is notable, can
Lasting pyrolysis processing house refuse, energy-conserving and environment-protective, can effective realize the harmful gas such as deodorize and suppression two English and
The discharge of flue dust.
Accompanying drawing illustrates:
For ease of explanation, the present invention is embodied as and accompanying drawing is described in detail by following.
Fig. 1 is the front axonometric drawing of the present invention；
Fig. 2 is the rear axonometric drawing of the present invention；
Fig. 3 is the structural representation magnetizing pyrolysis processing furnace body in the present invention；
Fig. 4 is the sectional view magnetizing pyrolysis processing furnace body in the present invention；
Fig. 5 is the structural representation of pyrolysis smoke forced condensation case in the present invention；
Fig. 6 is the structural representation of Water spray purifying box in the present invention；
Fig. 7 is the attachment structure schematic diagram of Water spray purifying box and the second external water tank in the present invention；
Fig. 8 is the structural representation of smog diversion three-way in the present invention；
Fig. 9 is the structural representation of water smoke treatment box in the present invention；
Figure 10 is the top view of water smoke treatment box in the present invention；
Figure 11 is the structural representation of tail gas terminal processing system in the present invention；
Figure 12 is the sectional view of tail gas terminal processing system in the present invention；
Figure 13 is the structural representation of permanent magnetism air magnetizator in the present invention.
1-feed arrangement；2-lifting material feeder；3-flat spin conveyer device；4-tank bracket；5-electric apparatus control apparatus；6-
Magnetization pyrolysis processing furnace body；6-1-circle refractory burner hearth；6-2-heat-insulation magnetic wall；6-2-1-heat-insulation layer；6-3-octahedron is bored
The poly-petticoat pipe of shape；6-4-flue gas through flange pipe；6-5-regulation turbulent flow valve；6-6-permanent magnetism air magnetizator；6-7-turbulent flow fire grate；6-
8-deashing fire door；7-pyrolysis smoke forced condensation case；7-1-condenser pipe；7-2-flue gas streams dividing plate；7-3-spoiler；7-4-
Smoke inlet；7-5-the first outlet flue；7-6-blowoff valve；8-water inlet pipe and water outlet pipe；9-the first external water tank；10-the first delivery pump；11-
Bracing frame；12-Water spray purifying box；12-1-the first flow-disturbing dividing plate；12-2-removes mist layer；12-3-packing layer；12-4-is atomized spray
Head；12-5-spiral nozzle；12-6-screw spraying pipeline；12-7-observation window；12-8-adsorbs pipeline；12-9-choked flow adsorption layer；
12-10-abutted flange；12-11-access panel；12-12-the second outlet flue；12-13-the first blowdown window；12-14-connecting pipeline；
13-spray header；14-the second external water tank；15-the second delivery pump；16-air-introduced machine；17-smog diversion three-way；17-1-level
Straight-through；17-2-hollow barrel pipe；17-3-90 degree threeway；17-4-flange covers；18-water smoke treatment box；18-1-circle air inlet method
Blue；18-2-Pall ring filler foam-removing layer；18-3-vortex-flow and defrosting layer；18-4-the second flow-disturbing dividing plate；The square flange of giving vent to anger of 18-5-；
18-6-the second blowdown window；18-7-maintenance window；18-8-casing；19-tail gas terminal processing system；19-1-honeycomb fashion fume purifying
Device；19-2-photodissociation formula cooking fume remover；Bis-pyrolysis heaters of 19-3-；19-4-electrostatic field case；19-5-the first flue gas pipeline；
19-6-the second flue gas pipeline；20-flue gas pipeline；21-activated carbon adsorption chimney；22-bracing frame.
Detailed description of the invention:
As shown in Fig. 1-Figure 13, this detailed description of the invention by the following technical solutions: it comprise feed arrangement 1, tank bracket 4,
Electric apparatus control apparatus 5, magnetization pyrolysis processing furnace body 6, pyrolysis smoke forced condensation case 7, water inlet pipe and water outlet pipe the 8, first external water tank
9, the first delivery pump 10, bracing frame 11, Water spray purifying box 12, spray header the 13, second external water tank the 14, second delivery pump
15, air-introduced machine 16, smog diversion three-way 17, water smoke treatment box 18, tail gas terminal processing system 19, flue gas pipeline 20, activated carbon
Absorption chimney 21, feed arrangement 1 is made up of lifting material feeder 2 and flat spin conveyer device 3, the lower section of feed arrangement 1
Side is provided with tank bracket 4, is provided with electric apparatus control apparatus 5 in tank bracket 4, and the lower section opposite side of feed arrangement 1 is provided with magnetization heat
Solution processes furnace body 6, and magnetization pyrolysis processing furnace body 6 is provided with pyrolysis smoke forced condensation case 7, pyrolysis smoke forced condensation case
Connecting on 7 has water inlet pipe and water outlet pipe 8 to be connected with the first external water tank 9, water inlet pipe and water outlet pipe 8 is provided with the first delivery pump 10, by first
Cooling water needed for delivery pump 10 circulation pumping flue gas condensing, the lower section of pyrolysis smoke forced condensation case 7 is provided with bracing frame 11,
Pyrolysis smoke forced condensation case 7 is connected with Water spray purifying box 12 by flue gas pipeline, and Water spray purifying box 12 connects spray
Spray pipe 13, and be connected with the second external water tank 14 by spray header 13, spray header 13 is provided with the second delivery pump 15,
By the second delivery pump 15 circulation pumping spray cleaning water, the two ends of air-introduced machine 16 respectively with the smoke of Water spray purifying box 12
Mouth is straight-through with the level of smog diversion three-way 17 to be connected, and 90 degree of threeways of smog diversion three-way 17 are connected with water smoke treatment box 18,
Setting tail gas terminal processing system 19 on water smoke treatment box 18, tail gas terminal processing system 19 is inhaled with activated carbon by flue gas pipeline 20
Attached chimney 21 connects, and the gas after purified treatment is discharged by activated carbon adsorption chimney 21, described house refuse magnetization heat
The operation principle solving treating stations is: the house refuse after simple sorting is transported to magnetize pyrolysis processing stove by feed arrangement 1
Being pyrolyzed in body of heater 6, harmful gas and steam that pyrolysis produces make in pyrolysis smoke through pyrolysis smoke forced condensation case 7
Tar, steam, dust, harmful gas separate, subsequently into Water spray purifying box 12, it is right that Water spray purifying box 12 can play
Pyrolysis smoke carries out chalk dust removing, cooling, waste gas absorption, the purpose of purification gas, and then waste gas enters water smoke treatment box 18, water smoke
Treatment box 18 can effectively retain the water smoke in waste gas, reduces waste gas water content, alleviates the work of follow-up tail gas terminal system
Pressure, last flue gas enters tail gas terminal processing system 19, and tail gas terminal processing system 19 is to clean through forced condensation, Water spray
In pyrolysis tail gas after change, water smoke process, the discharge thing the most up to standard of a small amount of residual finally processes.
As preferably, described magnetization pyrolysis processing furnace body 6 be internally provided with a circular refractory burner hearth 6-1, circle
The outer wrap of shape refractory burner hearth 6-1 has heat-insulation magnetic wall 6-2, and magnetize pyrolysis processing furnace body 6 is provided above octahedron
Taper poly-petticoat pipe 6-3, and fixed by several screws, the top of octahedra taper poly-petticoat pipe 6-3 is provided with flue gas through flange
Pipe 6-4, and fixed by several bolts, magnetization pyrolysis processing furnace body 6 is strong with pyrolysis smoke by flue gas through flange pipe 6-4
Cooling cylinder 7 processed is connected, and the bottom of magnetization pyrolysis processing furnace body 6 is provided with several regulation turbulent flow valve 6-5, regulation turbulent flow valve
6-5 is threaded connection with permanent magnetism air magnetizator 6-6, and permanent magnetism air magnetizator 6-6 is internal with magnetization pyrolysis processing furnace body 6
Turbulent fire grate 6-7 between connected by screw threads for fastening, magnetization pyrolysis processing furnace body 6 bottom surrounding be respectively provided with a deashing
Fire door 6-8, adds rubbish in circular refractory burner hearth 6-1 in use, ignites with combustible, respectively in deashing fire door 6-8
Under conditions of regulation turbulent flow valve 6-5 opens, producing oxygen uptake phenomenon in burner hearth in organic matter rubbish pyrolytic process, permanent magnetism air magnetizes
Device 6-6 magnetic air passes through combustion-supporting in turbulent flow fire grate 6-7 enters burner hearth and produces turbulent flow, accelerates the thermal decomposition of organic matter rubbish,
Described circular refractory burner hearth 6-1 is made up of refractory brick or refractory cement, and its effect is to provide a resistance to constant temperature for refuse pyrolysis
The space of degree, it is solid by several rivets that the outside of described heat-insulation magnetic wall 6-2 is provided with heat-insulation layer 6-2-1, heat-insulation layer 6-2-1
Being scheduled on magnetization pyrolysis processing furnace body 6, heat-insulation magnetic wall 6-2 is made up of refractory cement and permanent magnet, and its effect is magnetization
Air and organic substance have heat insulation function concurrently, and described permanent magnetism air magnetizator 6-6 is by not magnetic conduction hollow pipe and a permanent magnetism
Ferrum forms, and hollow pipe cylindrical two ends are screw thread, and one end of permanent magnet not homopolarity is placed in hollow pipe at a distance of 10 millimeters, and permanent magnetism is empty
Gas magnetizing device 6-6 refers to the magnetized a kind of parts of air, passes to a small amount of through magnetized air, maintain stable portion in pyrolysis oven
Part burning, makes the combustible in the solid waste being processed and pyrolysis produce the burning of combustible part, and produced heat is admittedly
Organic substance in body refuse persistently thermally decomposes, and owing to magnetic air makes treated object Indirect magnetization, reduces pyrolysis institute
The energy needed, thus pyrolysis can realize at a temperature of 350-550 DEG C, improves pyrolysis efficiency, thus is substantially reduced two English
Growing amount, decreases tail gas clean-up difficulty.
As preferably, the inside of described pyrolysis smoke forced condensation case 7 is provided with condenser pipe 7-1 and flue gas streams dividing plate
7-2, condenser pipe 7-1 are provided with spoiler 7-3, and a side bottom of pyrolysis smoke forced condensation case 7 is provided with smoke inlet 7-4,
The opposite side top of pyrolysis smoke forced condensation case 7 is provided with the second outlet flue 7-5, another of pyrolysis smoke forced condensation case 7
Side lower part is provided with blowoff valve 7-6, described condenser pipe 7-1 and uses pipe to make, and its effect is supercooled water；Flue gas streams
Dividing plate 7-2 uses steel plate to make, and its effect is the space that layering separates in casing, makes pyrolysis smoke lead to according to the route of design
Cross；Spoiler 7-3 is the metallic plate of square central band circular hole, and its effect is that flow-disturbing increases resistance, increases the contact of cooled flue gas
Area；Smoke inlet 7-4 is the design of hollow flange coil structures, and its effect is to allow pyrolysis smoke enter in cooling cylinder；Outlet flue 7-5's
One end is welded with the steel pipe of adpting flange, and its effect is smoke；Blowoff valve 7-6 is ball valve design, and its effect is to control through forcing
The fluid that condensation produces.
As preferably, described Water spray purifying box 12 be internally provided with the first flow-disturbing dividing plate 12-1, and by first
The inside of Water spray purifying box 12 is divided into except mist layer 12-2 and packing layer 12-3 by flow-disturbing dividing plate 12-1, and packing layer 12-3 sets
It is equipped with several atomizer 12-4, several atomizer 12-4 to be connected with several spiral nozzle 12-5 by pipeline, several spirals
Shower nozzle 12-5 is arranged in screw spraying pipeline 12-6, and screw spraying pipeline 12-6 is provided with several observation window 12-7, spiral
One end of spray piping 12-6 is connected with Water spray purifying box 12, the other end of screw spraying pipeline 12-6 and absorption pipeline 12-8
Connecting, be provided with choked flow adsorption layer 12-9 in absorption pipeline 12-8, one end of absorption pipeline 12-8 connects abutted flange 12-
10, Water spray purifying box 12 be provided above access panel 12-11, the side of Water spray purifying box 12 is provided with outlet flue 12-
12, the lower section of Water spray purifying box 12 is provided with several first blowdown window 12-13, and Water spray purifying box 12 passes through connecting pipeline
12-14 and the second external water tank 14 connect, and the effect of the first described flow-disturbing dividing plate 12-1 is to change gas-liquid direction；Except mist layer
12-2 and packing layer 12-3 is all a kind of filler, and its effect is to increase and the contacting of flue gas respectively, retain the water smoke in flue gas and
Increase flue gas contacts with absorbing liquid；The effect of atomizer 12-4 and spiral nozzle 12-5 is to spray absorbing liquid；Screw spraying
Pipeline 12-6 is a kind of spiral pipeline of inside cavity, and its effect is to increase contacting of flue gas and absorbing liquid；Absorption pipeline
12-8 is a kind of hollow pipe, and its effect was flue gas；Choked flow adsorption layer 12-9 is a kind of filler, and its effect is to increase resistance,
Increase the contact area of flue gas；Outlet flue 12-12 refers to the pipeline of band adpting flange, and its effect is waste gas exhaust outlet.
As preferably, described smog diversion three-way 17 is to be led directly to 17-1 and one by a level being positioned at center
90 degree of threeway 17-3 compositions of the two pieces at hollow barrel pipe 17-2 and two ends, the two ends of hollow barrel pipe 17-2 are respectively arranged with flange capping
17-4, and it is bolted fixing, 90 degree of threeway 17-3 of two pieces are connected with water smoke treatment box 18 respectively by flange.
As preferably, described water smoke treatment box 18 be by circular inlet flange 18-1, Pall ring filler foam-removing layer 18-2,
Vortex-flow and defrosting layer 18-3, the second flow-disturbing dividing plate 18-4, the square flange 18-5 that gives vent to anger, the second blowdown window 18-6, maintenance window 18-7, case
Body 18-8 forms, and circular inlet flange 18-1 is positioned at the top side of casing 18-8, Pall ring filler foam-removing layer 18-2 and eddy flow
Except mist layer 18-3 is positioned at the inside of casing 18-8, the second flow-disturbing dividing plate 18-4 separating, the square flange 18-5 that gives vent to anger is positioned at eddy flow
Except the top side of mist layer 18-3 upper box body 18-8, described circular inlet flange 18-1 is air inlet, and its effect is useless
Gas enters from entrance；Pall ring filler foam-removing layer 18-2 is a kind of filler, and its effect is to increase the contact surface with waste gas, retains useless
Foam in gas；Vortex-flow and defrosting layer 18-3 is rotational flow plate defroster, and its effect is to utilize spiral board to become the function that axial flow is eddy flow
The centrifugal force produced with eddy flow carries out except mist, except under droplet flow down along plate face periphery；The effect of the second flow-disturbing dividing plate 18-4 is
Flow-disturbing changes exhaust gas direction；The square flange 18-5 that gives vent to anger is waste gas outlet, and its effect is the outlet of the waste gas after retaining except mist.
As preferably, described tail gas terminal processing system 19 is by honeycomb fashion cooking fume remover 19-1, photodissociation formula oil smoke
Depurator 19-2, secondary pyrolysis heater 19-3, electrostatic field case 19-4, the first flue gas pipeline 19-5 and the second flue gas pipeline 19-6
Composition, honeycomb fashion cooking fume remover 19-1 is arranged in electrostatic field case 19-4, and electrostatic field case 19-4 is arranged on square flange of giving vent to anger
On 18-5, electrostatic field case 19-4 is provided with the first flue gas pipeline 19-5 bolt is fixing is communicated to photodissociation formula cooking fume remover 19-
2, photodissociation formula cooking fume remover 19-2 are communicated to secondary pyrolysis heater 19-3 by the second flue gas pipeline 19-6 bolt is fixing；High
During pressure electrostatic field, under the effect of high voltage electric field, soot gas ionizes, and mist of oil is charged, and major part is degraded carbonization, small part
Oil or fat particles move to the positive/negative plate of electric field under the absorption electric field force of electric field and airflow function be collected on pole plate and
Flowing to draw-off tray under the effect of self gravitation, discharge through oil drain passage, remaining micron order mist of oil is degraded into titanium dioxide by electric field
Carbon and water, simultaneously under the effect of high tension generator, in electric field, air produces ozone, eliminates most abnormal smells from the patient in flue gas,
Photodissociation formula cooking fume remover 19-2 is entered by flue gas pipeline 19-5, at Ultraviolet-C wave band by the gas after static electric field process
The lower strand changing tail gas oil of the effect of light, produces ozone with after oxygen reaction simultaneously, and ozone is by cold for oil molecule burning
Rear generation water and ozone, the abnormal flavour in flue gas eliminates the most therewith simultaneously, and the tail gas after process is entered secondary by flue gas pipeline 19-6
Pyrolysis heater 19-3, its operating temperature of electric heating control is used for secondary at 1000-1200 DEG C and gas residence time (about 3 seconds)
Heating, high temperature removes harmful gas in flue gas, and the effect of described honeycomb fashion cooking fume remover 19-1 is electrostatic precipitation degasification taste；
The effect of photodissociation formula cooking fume remover 19-2 is that deodorization eliminates the unusual smell；The effect of secondary pyrolysis heater 19-3 is to be removed by high temperature
Harmful gas in flue gas；The effect of electrostatic field case 19-4 is to place honeycomb fashion cooking fume remover 19-1；
As preferably, the inside of described activated carbon adsorption chimney 21 is filled with activated carbon, and activated carbon adsorption chimney 21 is pacified
It is contained in the side of secondary pyrolysis heater 19-3, activated carbon adsorption chimney 21 and secondary pyrolysis heater 19-3 by bracing frame 22
Support is fixing.
This detailed description of the invention uses the most advanced rational technological process, simple sorting, magnetization pyrolysis processing stove, pyrolysis cigarette
The purification of gas forced condensation, Water spray, the process of water smoke filler, electrostatic precipitation deodorization, photodissociation deodourizing, temperature control secondary are pyrolyzed, live
Property charcoal absorption chimney, garbage disposal rate reaches more than 95%, during refuse pyrolysis fume treatment produce tar, condense water, become silted up
Filler in mud and purifier, through precipitation clarifying treatment, the water after clarification can condense or spray cleaning water uses, and condenses
Thing can be sent magnetization pyrolysis processing stove back to and be processed, and non-secondary pollution does not produce waste water, do not produces waste residue (after a small amount of high temperature
Harmless lime-ash), energy consumption is low, is not spiked with any fuel, and gas discharge is up to state standards.
This detailed description of the invention is by regulation air magnetizator the magnetization gas flow entered and the stream controlling pyrolysis smoke
Amount controls refuse pyrolysis temperature, it is to avoid produce two English, and the flue gas that pyrolysis produces is through forcing smoke abatement tar removing and tail gas eventually
End processes and reclaims clarifying smoke gas, and remaining gas is discharged by blowdown stack, uses house refuse to burn the form of house refuse,
Once lighting a fire, need not add any fuel, low cost is taken up an area little, and Operation and Maintenance maintenance is simple, and pyrolysis decrement is notable, continuable
Pyrolysis processing house refuse, energy-conserving and environment-protective, effective can realize the harmful gas such as deodorize and suppression two English and flue dust
Discharge.
The ultimate principle of the present invention and principal character and advantages of the present invention have more than been shown and described.The technology of the industry
Personnel, it should be appreciated that the present invention is not restricted to the described embodiments, simply illustrating this described in above-described embodiment and description
The principle of invention, without departing from the spirit and scope of the present invention, the present invention also has various changes and modifications, and these become
Change and improvement both falls within scope of the claimed invention.Claimed scope by appending claims and
Equivalent defines.
Claims (8)
1. one way of life rubbish magnetization pyrolysis treating stations, it is characterised in that: it comprises feed arrangement (1), tank bracket (4), electrical equipment control
Device processed (5), magnetization pyrolysis processing furnace body (6), pyrolysis smoke forced condensation case (7), water inlet pipe and water outlet pipe (8), the first external water
Case (9), the first delivery pump (10), bracing frame (11), Water spray purifying box (12), spray header (13), the second external water tank
(14), the second delivery pump (15), air-introduced machine (16), smog diversion three-way (17), water smoke treatment box (18), tail gas terminal processes system
System (19), flue gas pipeline (20), activated carbon adsorption chimney (21), feed arrangement (1) is by lifting material feeder (2) and horizontal helical
Rotation conveyer device (3) composition, the side, lower section of feed arrangement (1) is provided with tank bracket (4), and tank bracket is provided with electrical equipment control in (4)
Device (5), the lower section opposite side of feed arrangement (1) is provided with magnetization pyrolysis processing furnace body (6), magnetizes pyrolysis processing furnace body
(6) being provided with pyrolysis smoke forced condensation case (7), the upper connection of pyrolysis smoke forced condensation case (7) has water inlet pipe and water outlet pipe (8) and first
External water tank (9) is connected, and water inlet pipe and water outlet pipe (8) is provided with the first delivery pump (10), by the first delivery pump (10) circulation pumping cigarette
The solidifying required cooling water of air cooling, the lower section of pyrolysis smoke forced condensation case (7) is provided with bracing frame (11), and pyrolysis smoke is forced cold
Solidifying case (7) is connected with Water spray purifying box (12) by flue gas pipeline, and the upper connection of Water spray purifying box (12) has spray header
(13), and being connected with the second external water tank (14) by spray header (13), spray header is provided with the second delivery pump on (13)
(15), and pumping spray cleaning water by the second delivery pump (15) circulation, the two ends of air-introduced machine (16) are clean with Water spray respectively
Change that the level of the outlet flue of case (12) and smog diversion three-way (17) is straight-through to be connected, 90 degree of threeways of smog diversion three-way (17) and
Water smoke treatment box (18) is connected, and water smoke treatment box (18) sets tail gas terminal processing system (19), tail gas terminal processing system
(19) being connected with activated carbon adsorption chimney (21) by flue gas pipeline (20), the gas after purified treatment is by activated carbon adsorption
Chimney (21) is discharged, and the operation principle of described house refuse magnetization pyrolysis treating stations is: feed arrangement (1) will be through simple point
House refuse after picking is pyrolyzed in being transported to magnetize pyrolysis processing furnace body (6), and harmful gas and water that pyrolysis produces steam
Gas makes the tar in pyrolysis smoke, steam, dust, harmful gas separate through pyrolysis smoke forced condensation case (7), then enters
Enter Water spray purifying box (12), Water spray purifying box (12) can play pyrolysis smoke is carried out chalk dust removing, cooling, waste gas absorption,
Purifying the purpose of gas, then waste gas enters water smoke treatment box (18), and water smoke treatment box (18) can effectively retain in waste gas
Water smoke, reduces waste gas water content, alleviates the operating pressure of follow-up tail gas terminal system, and last flue gas enters tail gas terminal processes
System (19), tail gas terminal processing system (19) is to the pyrolysis tail gas after forced condensation, Water spray purification, water smoke process
In, the discharge thing the most up to standard of a small amount of residual finally processes.
One way of life rubbish the most according to claim 1 magnetization pyrolysis treating stations, it is characterised in that: described magnetization pyrolysis
Processing the circular refractory burner hearth (6-1) that is internally provided with of furnace body (6), the outer wrap of circular refractory burner hearth (6-1) has
Heat-insulation magnetic wall (6-2), magnetize pyrolysis processing furnace body (6) is provided above the octahedra poly-petticoat pipe of taper (6-3), and passes through
Several screws are fixed, and the top of the octahedra poly-petticoat pipe of taper (6-3) is provided with flue gas through flange pipe (6-4), and by several
Bolt is fixed, and magnetization pyrolysis processing furnace body (6) is by flue gas through flange pipe (6-4) and pyrolysis smoke forced condensation case (7)
It is connected, the bottom of magnetization pyrolysis processing furnace body (6) is provided with several regulation turbulent flow valve (6-5), regulation turbulent flow valve (6-5)
It is threaded connection with permanent magnetism air magnetizator (6-6), permanent magnetism air magnetizator (6-6) and magnetization pyrolysis processing furnace body (6)
Being connected by screw threads for fastening between internal turbulent fire grate (6-7), the bottom surrounding of magnetization pyrolysis processing furnace body (6) is respectively provided with
One deashing fire door (6-8), adds rubbish in circular refractory burner hearth (6-1), in use with combustible from deashing fire door (6-
8) ignite in, under conditions of each regulation turbulent flow valve (6-5) is opened, organic matter rubbish pyrolytic process produces oxygen uptake existing in burner hearth
As, permanent magnetism air magnetizator (6-6) magnetic air passes through combustion-supporting in turbulent flow fire grate (6-7) enters burner hearth and produces turbulent flow, accelerates
The thermal decomposition of organic matter rubbish, described circular refractory burner hearth (6-1) is made up of refractory brick or refractory cement, its effect be for
Refuse pyrolysis provides the space of resistance to uniform temperature, and the outside of described heat-insulation magnetic wall (6-2) is provided with heat-insulation layer (6-2-1),
Heat-insulation layer (6-2-1) is fixed in magnetization pyrolysis processing furnace body (6) by several rivets, and heat-insulation magnetic wall (6-2) is by resistance to
Fire cement and permanent magnet composition, its effect is magnetic air and organic substance has heat insulation function, described permanent magnetism air magnetization concurrently
Device (6-6) by one not magnetic conduction hollow pipe and permanent magnet form, hollow pipe cylindrical two ends are screw thread, the one of permanent magnet not homopolarity
End is placed in hollow pipe at a distance of 10 millimeters, and permanent magnetism air magnetizator (6-6) refers to the magnetized a kind of parts of air, at pyrolysis oven
Inside pass to a small amount of through magnetized air, maintain stable fractional combustion, make the combustible in the solid waste being processed and pyrolysis
Producing the burning of combustible part, produced heat is that the organic substance in solid waste persistently thermally decomposes, due to magnetization
Air makes treated object Indirect magnetization, reduces the energy needed for pyrolysis, thus pyrolysis can be real at a temperature of 350-550 DEG C
Existing, improve pyrolysis efficiency, thus be substantially reduced two English growing amounts, decrease tail gas clean-up difficulty.
One way of life rubbish the most according to claim 1 magnetization pyrolysis treating stations, it is characterised in that: described pyrolysis smoke
The inside of forced condensation case (7) is provided with condenser pipe (7-1) and flue gas streams dividing plate (7-2), and condenser pipe (7-1) is provided with resistance
Stream plate (7-3), a side bottom of pyrolysis smoke forced condensation case (7) is provided with smoke inlet (7-4), pyrolysis smoke forced condensation case
(7) opposite side top is provided with the first outlet flue (7-5), and the opposite side bottom of pyrolysis smoke forced condensation case (7) is provided with
Blowoff valve (7-6), described condenser pipe (7-1) uses pipe to make, and its effect is supercooled water；Flue gas streams dividing plate (7-
2) using steel plate to make, its effect is the space that layering separates in casing, makes pyrolysis smoke pass through according to the route of design；Choked flow
Plate (7-3) is the metallic plate of square central band circular hole, and its effect is that flow-disturbing increases resistance, increases the contact area of cooled flue gas；
Smoke inlet (7-4) is the design of hollow flange coil structures, and its effect is to allow pyrolysis smoke enter in cooling cylinder；Outlet flue (7-5)
One end is welded with the steel pipe of adpting flange, and its effect is smoke；Blowoff valve (7-6) is ball valve design, and its effect is to control through strong
The solidifying fluid produced of refrigeration.
One way of life rubbish the most according to claim 1 magnetization pyrolysis treating stations, it is characterised in that: described Water spray is clean
Change the first flow-disturbing dividing plate (12-1) that is internally provided with of case (12), and by the first flow-disturbing dividing plate (12-1) by Water spray purifying box
(12) inside is divided into except mist layer (12-2) and packing layer (12-3), and packing layer (12-3) is provided with several atomizer
(12-4), several atomizers (12-4) are connected with several spiral nozzles (12-5) by pipeline, several spiral nozzles (12-5)
Being arranged in screw spraying pipeline (12-6), screw spraying pipeline (12-6) is provided with several observation window (12-7), spiral sprays
The one end in shower pipe road (12-6) is connected with Water spray purifying box (12), the other end of screw spraying pipeline (12-6) and absorption pipeline
(12-8) connecting, be provided with choked flow adsorption layer (12-9) in absorption pipeline (12-8), one end of absorption pipeline (12-8) connects to be had
Abutted flange (12-10), Water spray purifying box (12) be provided above access panel (12-11), Water spray purifying box (12)
Side is provided with the second outlet flue (12-12), and the lower section of Water spray purifying box (12) is provided with several first blowdown window (12-
13), Water spray purifying box (12) is connected with the second external water tank (14) by connecting pipeline (12-14), the first described flow-disturbing
The effect of dividing plate (12-1) is to change gas-liquid direction；Except mist layer (12-2) and packing layer (12-3) they are all a kind of fillers, its effect
It is to increase respectively and the contacting of flue gas, retains the water smoke in flue gas and increase contacting of flue gas and absorbing liquid；Atomizer (12-
4) and the effect of spiral nozzle (12-5) is to spray absorbing liquid；Screw spraying pipeline (12-6) be a kind of inside cavity in the shape of a spiral
Pipeline, its effect is to increase contacting of flue gas and absorbing liquid；Absorption pipeline (12-8) is a kind of hollow pipe, and its effect was
Flue gas；Choked flow adsorption layer (12-9) is a kind of filler, and its effect is to increase resistance, increases the contact area of flue gas；Outlet flue
(12-12) referring to the pipeline of band adpting flange, its effect is waste gas exhaust outlet.
One way of life rubbish the most according to claim 1 magnetization pyrolysis treating stations, it is characterised in that: described smog shunting
Threeway (17) is by a level straight-through (17-1) being positioned at center and a hollow barrel pipe (17-2) and the two pieces at two ends
90 degree of threeway (17-3) compositions, the two ends of hollow barrel pipe (17-2) are respectively arranged with flange capping (17-4), and are connected by bolt
Connecing fixing, 90 degree of threeways (17-3) of two pieces are connected with water smoke treatment box (18) respectively by flange.
One way of life rubbish the most according to claim 1 magnetization pyrolysis treating stations, it is characterised in that: described water smoke processes
Case (18) is by circular inlet flange (18-1), Pall ring filler foam-removing layer (18-2), vortex-flow and defrosting layer (18-3), the second flow-disturbing
Dividing plate (18-4), square flange of giving vent to anger (18-5), the second blowdown window (18-6), maintenance window (18-7), casing (18-8) form, circle
Shape inlet flange (18-1) is positioned at the top side of casing (18-8), Pall ring filler foam-removing layer (18-2) and vortex-flow and defrosting layer
(18-3) being positioned at the inside of casing (18-8), the second flow-disturbing dividing plate (18-4) separate, square flange of giving vent to anger (18-5) is positioned at rotation
Stream is except the top side of mist layer (18-3) upper box body (18-8), and described circular inlet flange (18-1) is air inlet, its
Effect is that waste gas enters from entrance；Pall ring filler foam-removing layer (18-2) is a kind of filler, and its effect is to increase and the connecing of waste gas
Contacting surface, retains the foam in waste gas；Vortex-flow and defrosting layer (18-3) is rotational flow plate defroster, and its effect is to utilize spiral board to become axial flow
The centrifugal force produced for the function of eddy flow and eddy flow carries out except mist, except under droplet flow down along plate face periphery；Second flow-disturbing dividing plate
(18-4) effect is that flow-disturbing changes exhaust gas direction；Square flange of giving vent to anger (18-5 is) waste gas outlet, its effect is to remove through retaining
The outlet of the waste gas after mist.
One way of life rubbish the most according to claim 1 magnetization pyrolysis treating stations, it is characterised in that: described tail gas terminal
Processing system (19) is by honeycomb fashion cooking fume remover (19-1), photodissociation formula cooking fume remover (19-2), secondary pyrolysis heater
(19-3), electrostatic field case (19-4), the first flue gas pipeline (19-5) and the second flue gas pipeline (19-6) composition, honeycomb fashion oil smoke is clean
Changing device (19-1) to be arranged in electrostatic field case (19-4), electrostatic field case (19-4) is arranged on square flange of giving vent to anger (18-5), quiet
It is provided with on electric field case (19-4) that the first flue gas pipeline (19-5) bolt is fixing is communicated to photodissociation formula cooking fume remover (19-2), light
Solution formula cooking fume remover (19-2) is communicated to secondary pyrolysis heater (19-by the second flue gas pipeline (19-6) bolt is fixing
3), during high-voltage electrostatic field, under the effect of high voltage electric field, soot gas ionizes, and mist of oil is charged, and major part is degraded carbonization,
Small part oil or fat particles moves to the positive/negative plate of electric field under the electric field force and airflow function of absorption electric field and is collected in pole plate
Above and flowing to draw-off tray under the effect of self gravitation, discharge through oil drain passage, remaining micron order mist of oil is degraded into by electric field
Carbon dioxide and water, simultaneously under the effect of high tension generator, in electric field, air produces ozone, eliminates in flue gas most
Abnormal smells from the patient, is entered photodissociation formula cooking fume remover (19-2) by the gas after static electric field process by flue gas pipeline (19-5), in ultraviolet
The lower strand changing tail gas oil of the effect of the light of line-C-band, produces ozone with after oxygen reaction simultaneously, and ozone is by oil
Generating water and ozone after the cold burning of molecule, the abnormal flavour in flue gas eliminates the most therewith simultaneously, and the tail gas after process is by flue gas pipeline
(19-6) entering secondary pyrolysis heater (19-3), its operating temperature of electric heating control is when 1000-1200 DEG C and flue gas stop
Between be used for post bake, high temperature removes harmful gas in flue gas, and the effect of described honeycomb fashion cooking fume remover (19-1) is quiet
Electric precipitation degasification taste；The effect of photodissociation formula cooking fume remover (19-2) is that deodorization eliminates the unusual smell；Secondary pyrolysis heater (19-3)
Effect is to remove harmful gas in flue gas by high temperature；The effect of electrostatic field case (19-4) is to place honeycomb fashion cooking fume remover
(19-1)。
One way of life rubbish the most according to claim 1 magnetization pyrolysis treating stations, it is characterised in that: described activated carbon is inhaled
The inside of attached chimney (21) is filled with activated carbon, and activated carbon adsorption chimney (21) is arranged on the side of secondary pyrolysis heater (19-3)
Face, activated carbon adsorption chimney (21) and secondary pyrolysis heater (19-3) are supported fixing by bracing frame (22).
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