CN206037060U - Domestic waste magnetization pyrolysis treatment station - Google Patents

Abstract

The utility model discloses a domestic waste magnetization pyrolysis treatment station, it relates to rubbish magnetization pyrolysis field, be connected with the spray header on the water spraying purification case, and link to each other through spray header and the 2nd external water tank, through second delivery pump circulation pump sending spraying purification water, the both ends of draught fan are direct continuous with the outlet flue and the smog reposition of redundant personnel three -way level of water spraying purification case respectively, 90 degrees tee bends of smog reposition of redundant personnel three -way link to each other with water smoke processing case, establish tail gas terminal handling system on the water smoke processing case, tail gas terminal handling system passes through flue gas line and is connected with the active carbon adsorption chimney, gas behind purification treatment is discharged by the active carbon adsorption chimney. It controls the garbage pyrolytic temperature through the magnetization gas flow that the conditioning air magnetizer got into with the flow of control pyrolysis smoke, avoids producing the dioxin, and flue gas that the pyrolysis produced is through force the smoke abatement to remove tar and tail gas terminal handling retrieves the smoke and dust purge gas, and all the other gases are discharged by exhaust stacks.

Description

A kind of house refuse magnetization pyrolysis treating stations

Technical field：

This utility model is related to a kind of house refuse magnetization pyrolysis treating stations, belongs to rubbish magnetization pyrolysis technical field.

Background technology：

The high speed development of China's city-building and new countryside construction, the yield of house refuse increase increasingly, directly fill not Substantial amounts of transport capacity is only expended, and accounts for land resource, the evaporation of effluent seepage and foul smell that landfill waste is produced not only is caused harm Currently, and leave troubles to descendants；, using the dispersion directly burning in garbage pool, the harmful smoke of generation is without place for rural area and cities and towns suburb Reason, causes severe contamination to air；For above-mentioned situation, processs of the country to house refuse carried out long-term and unremitting scientific research and Dual effort in terms of enforcement, has established consumer waste incineration the facility for generating in tier 2 cities, but large-scale More advanced Domestic garbage treatment equipment substantially from the external technology introduced, although can normally run, but build and throw Money is big, and operating cost is high, it is difficult to popularity；The technical scheme that the country captures house refuse is varied, has in house refuse Add coal, oil, vapour directly to burn in processing procedure, have and house refuse is processed into charcoal shape granule, have gasification furnace on probation Process rubbish etc., or these technologies are investment, excessive, operating cost is high, or being that technology is immature, being not normally functioning, Thus the house refuse overwhelming majority of China is still using directly landfill or the original processing method directly burned.

The content of the invention：

For the problems referred to above, the technical problems to be solved in the utility model is to provide a kind of house refuse magnetization pyrolysis processing Stand.

A kind of house refuse magnetization pyrolysis treating stations of the present utility model, it includes feed arrangement, tank bracket, electrical equipment control dress Put, magnetize pyrolysis treatment furnace body of heater, pyrolysis smoke forced condensation case, water inlet pipe and water outlet pipe, the first external water tank, the first delivery pump, At support, Water spray purifying box, spray header, the second external water tank, the second delivery pump, air-introduced machine, smog diversion three-way, water smoke Reason case, tail gas terminal processing system, flue gas pipeline, activated carbon adsorption chimney, feed arrangement is by lifting material feeder and level Helix transporting device is constituted, and the lower section side of feed arrangement is provided with tank bracket, is provided with electric apparatus control apparatus, charging dress in tank bracket The lower section opposite side put is provided with magnetization pyrolysis treatment furnace body of heater, and magnetization pyrolysis treatment furnace body of heater is provided with pyrolysis smoke and forces cold Solidifying case, is connected with water inlet pipe and water outlet pipe on pyrolysis smoke forced condensation case and is connected with the first external water tank, and be provided with water inlet pipe and water outlet pipe First delivery pump, circulates the cooling water needed for pumping flue gas condensing by the first delivery pump, under pyrolysis smoke forced condensation case Side is provided with bracing frame, and pyrolysis smoke forced condensation case is connected with Water spray purifying box by flue gas pipeline, Water spray purifying box On be connected with spray header, and be connected with the second external water tank by spray header, on spray header, be provided with the second delivery pump Circulating pump, by the second delivery pump circulation pumping spray cleaning water, the two ends of air-introduced machine are gone out with Water spray purifying box respectively 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, water smoke Tail gas terminal processing system is set on treatment box, and 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.

Preferably, described magnetization is pyrolyzed the circular refractory burner hearth that is internally provided with for the treatment of furnace body of heater, it is circular resistance to The outer wrap of stove thorax has heat-insulation magnetic wall, is provided with the poly- petticoat pipe of octahedra taper above magnetization pyrolysis treatment furnace body of heater, And fixed by several screws, flue gas through flange pipe is provided with the top of the poly- petticoat pipe of octahedra taper, and passes through several bolts Fixed, magnetization pyrolysis treatment furnace body of heater is connected with pyrolysis smoke forced condensation case by flue gas through flange pipe, magnetization pyrolysis The turbulent valve of several regulations is provided with the bottom for processing furnace body, adjusts turbulent valve with permanent magnetism air magnetizator by screw thread company Connect, connected by screw threads for fastening between the turbulent fire grate of permanent magnetism air magnetizator and magnetization pyrolysis treatment furnace furnace interior, magnetization The bottom surrounding of pyrolysis processing furnace body is respectively provided with a deashing fire door, adds rubbish in circular refractory burner hearth when in use, Ignited from deashing fire door with combustible, under conditions of the turbulent valve of each regulation is opened, organic matter rubbish pyrolytic process in burner hearth Middle generation oxygen uptake phenomenon, permanent magnetism air magnetizator magnetic air are entered combustion-supporting in burner hearth through turbulent fire grate and produce turbulent flow, plus The thermal decomposition of fast organic matter rubbish.

Preferably, described circular refractory burner hearth is made up of refractory brick or refractory cement, its effect is for rubbish heat Solution provides the space of resistance to uniform temperature.

Preferably, the outside of described heat-insulation magnetic wall is provided with heat-insulation layer, heat-insulation layer is fixed on by several rivets On magnetization pyrolysis treatment furnace body of heater, heat-insulation magnetic wall is into its effect is magnetic air and has by refractory cement with permanent magnet group Machine material has heat insulation function concurrently.

Preferably, described permanent magnetism air magnetizator be by one not magnetic conduction hollow pipe and permanent magnet group into 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 air magnetizator is referred to A kind of magnetized part of air, passes to the magnetized air of a small amount of Jing in pyrolysis oven, maintains stable fractional combustion, makes to be processed Solid waste in combustible and pyrolysis produce the burning of combustible part, produced heat is the Organic substance in solid waste Matter is persistently thermally decomposed, and as magnetic air makes treated object Indirect magnetization, is reduced the energy needed for pyrolysis, thus is pyrolyzed Can realize at a temperature of 350-550 DEG C, improve pyrolysis efficiency, so as to substantially reduce two English growing amounts, reduce tail gas Purification difficulty.

Preferably, the inside of described pyrolysis smoke forced condensation case is provided with condenser pipe and flue gas streams dividing plate, it is 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 Another upper lateral part of case is provided with the first outlet flue, and another side lower part of pyrolysis smoke forced condensation case is provided with blowoff valve.

Preferably, described condenser pipe is made using pipe, its effect is supercooled water；Flue gas streams dividing plate employing Steel plate is made, and its effect is the space that layering separates in casing, pyrolysis smoke is passed through according to the route of design；Spoiler is side The metallic plate of shape center band circular hole, its effect are that flow-disturbing increases resistance, increase the contact area of cooled flue gas；Smoke inlet is hollow Flange coil structures are designed, and its effect is to allow pyrolysis smoke to enter in cooling cylinder；One end of outlet flue is welded with the steel of adpting flange Pipe, its effect is smoke；Blowoff valve is ball valve design, and its effect is to control the fluid that Jing forced condensations are produced.

Preferably, described Water spray purifying box is 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 demisting layer and packing layer by plate, is provided with several atomizers, several mists on packing layer Change shower nozzle to be connected with several spiral nozzles by pipeline, several spiral nozzles are arranged in screw spraying pipeline, screw spraying pipe Be provided with several observation windows on road, one end of screw spraying pipeline is connected with Water spray purifying box, screw spraying pipeline it is another End is connected with absorption pipeline, is provided with choked flow adsorption layer in absorption pipeline, and the one end for adsorbing pipeline is connected with abutted flange, water spray Drenching and access panel is provided with above purifying box, 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 windows, and Water spray purifying box is connected with the second external water tank by connecting pipeline.

Preferably, the effect of the first described flow-disturbing dividing plate is to change gas-liquid direction；Demisting layer and packing layer are one Filler is planted, its effect is to increase the contact with flue gas respectively, retain the water smoke in flue gas and increase contact of the flue gas with absorbing liquid； The effect of atomizer and spiral nozzle is sprinkling absorbing liquid；Screw spraying pipeline is a kind of spiral pipe of inside cavity Road, its effect are to increase contact of the flue gas with absorbing 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 to increase resistance, increases the contact area of flue gas；Outlet flue refers to the pipe with adpting flange Road, its effect are waste gas discharge outlets.

Preferably, described smog diversion three-way is led directly to and a hollow barrel by a level for being located at center 90 degree of threeway compositions of 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.

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 outlet flange, the second blowdown window, maintenance window, casing composition, circular inlet flange are located at casing Top side, Pall ring filler foam-removing layer and vortex-flow and defrosting layer are located at the inside of casing, are separated by the second flow-disturbing dividing plate, square Outlet flange is located at the top side of vortex-flow and defrosting layer upper box body.

Preferably, described circular inlet flange is air inlet, its effect is that waste gas is entered from entrance；Pall ring is filled out Material foam-removing layer is a kind of filler, and its effect is the contact surface of increase and waste gas, retains the foam in waste gas；Vortex-flow and defrosting layer is rotation Stream plate demister, its effect are that the centrifugal force produced using the function and eddy flow that spiral board change axle stream is eddy flow carries out demisting, are removed 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 outlet flange is useless Gas is exported, and its effect is the outlet of the waste gas Jing after retention demisting.

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 are arranged on In electrostatic field case, electrostatic field case is arranged on square outlet flange, is provided with the first flue gas pipeline bolt and fixes on electrostatic field case Photodissociation formula cooking fume remover is communicated to, photodissociation formula cooking fume remover is fixed by the second flue gas pipeline bolt and is communicated to secondary pyrolysis Heater；During high-voltage electrostatic field, in the presence of high voltage electric field, soot gas ionization, mist of oil are charged, and major part is able to charcoal of degrading Change, small part oil or fat particles are moved to the positive/negative plate of electric field under the electric field force and airflow function of absorption electric field and are collected in pole Flow on plate and in the presence of self gravitation and arrive draw-off tray, Jing oil drain passages are discharged, and remaining micron order mist of oil is degraded by electric field Into carbon dioxide and water, while in the presence of high tension generator, air produces ozone in electric field, major part in flue gas is eliminated Abnormal smells from the patient, the gas after static electric field process by flue gas pipeline enter photodissociation formula cooking fume remover, in Ultraviolet-C wave band Change the strand of tail gas oil in the presence of light, at the same with oxygen reaction after produce ozone, ozone is by oily molecule cold burning Water and ozone is generated afterwards, while the abnormal flavour in flue gas is also eliminated therewith, the tail gas after process enters secondary pyrolysis by flue gas pipeline Heater, its operating temperature of electric heating control are used for post bake for (about 3 seconds) in 1000-1200 DEG C and gas residence time, high Temperature removes harmful gass in flue gas.

Preferably, the effect of described honeycomb fashion cooking fume remover is electrostatic precipitation removes abnormal smells from the patient；Photodissociation formula fume purifying Effect be that deodorization eliminates the unusual smell；The effect of secondary pyrolysis heater is to remove harmful gass in flue gas by high temperature；Electrostatic field case Effect be place honeycomb fashion cooking fume remover；

Preferably, the inside of described activated carbon adsorption chimney is filled with activated carbon, activated carbon adsorption chimney is arranged on The side of secondary pyrolysis heater, activated carbon adsorption chimney and secondary pyrolysis heater are supported by bracing frame and are fixed.

The beneficial effects of the utility model：It is by adjusting the magnetization gas flow and control pyrolysis that air magnetizator is entered The flow of flue gas is controlling refuse pyrolysis temperature, it is to avoid produce two English, is pyrolyzed the flue gas for producing through forcing smoke abatement tar removing Clarifying smoke gas is reclaimed with tail gas terminal processes, and remaining gas are discharged by blowdown stack, burn life rubbish using house refuse The form of rubbish, once lights a fire, and without adding any fuel, low cost occupation of land is little, and Operation and Maintenance maintenance is simple, and pyrolysis decrement shows Write, continuable pyrolysis processing house refuse, energy-conserving and environment-protective, what energy was effective realizes deodorize and suppress harmful gas such as two English The discharge of body and flue dust.

Description of the drawings：

For ease of explanation, this utility model is embodied as and accompanying drawing is described in detail by following.

Fig. 1 is front axonometric drawing of the present utility model；

Fig. 2 is rear axonometric drawing of the present utility model；

Fig. 3 is the structural representation of magnetization pyrolysis treatment furnace body of heater in this utility model；

Fig. 4 is the sectional view of magnetization pyrolysis treatment furnace body of heater in this utility model；

Fig. 5 is the structural representation of pyrolysis smoke forced condensation case in this utility model；

Fig. 6 is the structural representation of Water spray purifying box in this utility model；

Fig. 7 is the attachment structure schematic diagram of Water spray purifying box and the second external water tank in this utility model；

Fig. 8 is the structural representation of smog diversion three-way in this utility model；

Fig. 9 is the structural representation of water smoke treatment box in this utility model；

Figure 10 is the top view of water smoke treatment box in this utility model；

Figure 11 is the structural representation of tail gas terminal processing system in this utility model；

Figure 12 is the sectional view of tail gas terminal processing system in this utility model；

Figure 13 is the structural representation of permanent magnetism air magnetizator in this utility model.

1- feed arrangements；2- lifting material feeders；3- flat spin conveyer devices；4- tank brackets；5- electric apparatus control apparatus；6- Magnetization pyrolysis treatment furnace body of heater；6-1- circle refractory burner hearths；6-2- heat-insulation magnetic walls；6-2-1- heat-insulation layers；The octahedra cones of 6-3- The poly- petticoat pipe of shape；6-4- flue gas through flange pipes；6-5- adjusts turbulent valve；6-6- permanent magnetism air magnetizators；6-7- turbulent flow fire grates；6- 8- deashing fire doors；7- pyrolysis smoke forced condensation casees；7-1- condenser pipes；7-2- flue gases stream dividing plate；7-3- spoilers；7-4- Smoke inlet；The first outlet flues of 7-5-；7-6- blowoff valves；8- water inlet pipe and water outlet pipes；The first external water tanks of 9-；The first delivery pumps of 10-；11- Bracing frame；12- Water spray purifying boxs；12-1- the first flow-disturbing dividing plates；12-2- demisting layers；12-3- packing layers；12-4- atomization sprays Head；12-5- spiral nozzles；12-6- screw spraying pipelines；12-7- observation windows；12-8- adsorbs pipeline；12-9- choked flow adsorption layers； 12-10- abutted flanges；12-11- access panels；The second outlet flues of 12-12-；12-13- the first blowdown windows；12-14- connecting pipelines； 13- spray headers；The second external water tanks of 14-；The second delivery pumps of 15-；16- air-introduced machines；17- smog diversion three-ways；17-1- levels It is straight-through；17-2- hollow barrel pipes；17-3-90 degree threeways；17-4- flanges are covered；18- water smoke treatment boxes；18-1- circle air inlet methods It is blue；18-2- Pall ring filler foam-removing layers；18-3- vortex-flow and defrosting layers；18-4- the second flow-disturbing dividing plates；The square outlet flanges of 18-5-； 18-6- the second blowdown windows；18-7- maintenance windows；18-8- casings；19- tail gas terminal processing systems；19-1- honeycomb fashion fume purifyings Device；19-2- photodissociation formula cooking fume removers；Bis- pyrolysis heaters of 19-3-；19-4- electrostatic field casees；The first flue gas pipelines of 19-5-； The second flue gas pipelines of 19-6-；20- flue gas pipelines；21- activated carbon adsorption chimneys；22- bracing frames.

Specific embodiment：

As shown in Fig. 1-Figure 13, this specific embodiment is employed the following technical solutions：It comprising feed arrangement 1, tank bracket 4, Electric apparatus control apparatus 5, magnetization pyrolysis treatment furnace body of heater 6, pyrolysis smoke forced condensation case 7, water inlet pipe and water outlet pipe 8, the first external water tank 9th, 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 15th, 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 are 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 treatment furnace body of heater 6 is provided with pyrolysis smoke forced condensation case 7, pyrolysis smoke forced condensation case It is connected with water inlet pipe and water outlet pipe 8 to be connected with the first external water tank 9 on 7, is provided with the first delivery pump 10 on water inlet pipe and water outlet pipe 8, by first Cooling water needed for the circulation pumping flue gas condensing of delivery pump 10, the lower section of pyrolysis smoke forced condensation case 7 are provided with bracing frame 11, Pyrolysis smoke forced condensation case 7 is connected with Water spray purifying box 12 by flue gas pipeline, is connected with spray on Water spray purifying box 12 Spray pipe 13, and be connected with the second external water tank 14 by spray header 13, the second delivery pump 15 is provided with spray header 13, By the circulation pumping spray cleaning water of the second delivery pump 15, the smoke respectively with Water spray purifying box 12 of the two ends of air-introduced machine 16 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, Tail gas terminal processing system 19 is set on water smoke treatment box 18, and 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.

Preferably, described magnetization is pyrolyzed the circular refractory burner hearth 6-1 that is internally provided with for the treatment of furnace body of heater 6, it is round The top that the outer wrap of shape refractory burner hearth 6-1 has heat-insulation magnetic wall 6-2, magnetization pyrolysis treatment furnace body of heater 6 is provided with octahedron The poly- petticoat pipe 6-3 of taper, and being fixed by several screws, is provided with flue gas through flange at the top of the poly- petticoat pipe 6-3 of octahedra taper Pipe 6-4, and fixed by several bolts, magnetization pyrolysis treatment furnace body of heater 6 is strong with pyrolysis smoke by flue gas through flange pipe 6-4 Cooling cylinder processed 7 is connected, and is provided with the turbulent valve 6-5 of several regulations, adjusts turbulent valve on the bottom of magnetization pyrolysis treatment furnace body of heater 6 6-5 is threaded connection with permanent magnetism air magnetizator 6-6, and permanent magnetism air magnetizator 6-6 is pyrolyzed inside treatment furnace body of heater 6 with magnetization Turbulent fire grate 6-7 between connected by screw threads for fastening, the bottom surrounding of magnetization pyrolysis treatment furnace body of heater 6 is respectively provided with a deashing Fire door 6-8, adds rubbish in circular refractory burner hearth 6-1 when in use, is ignited with combustible, each from deashing fire door 6-8 Under conditions of adjusting turbulent valve 6-5 unlatchings, oxygen uptake phenomenon, the magnetization of permanent magnetism air in burner hearth, in organic matter rubbish pyrolytic process, is produced Device 6-6 magnetic airs are entered combustion-supporting in burner hearth through turbulent fire grate 6-7 and produce turbulent flow, accelerate the thermal decomposition of organic matter rubbish.

Preferably, described circular refractory burner hearth 6-1 is made up of refractory brick or refractory cement, its effect is for rubbish Pyrolysis provides the space of resistance to uniform temperature.

Preferably, 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 by number Individual rivet is fixed on magnetization pyrolysis treatment furnace body of heater 6, and heat-insulation magnetic wall 6-2 is into its work by refractory cement with permanent magnet group With being that magnetic air and organic substance have heat insulation function concurrently.

Preferably, described permanent magnetism air magnetizator 6-6 be by one not magnetic conduction hollow pipe and permanent magnet group into hollow Cylindrical two ends are managed for screw thread, one end of permanent magnet not homopolarity is placed in hollow pipe at a distance of 10 millimeters, permanent magnetism air magnetizator 6-6 Refer to a kind of magnetized part of air, pass to the magnetized air of a small amount of Jing in pyrolysis oven, maintain stable fractional combustion, make by Combustible in the solid waste of process and pyrolysis produce the burning of combustible part, and produced heat is having in solid waste Machine material is persistently thermally decomposed, and as magnetic air makes treated object Indirect magnetization, reduces the energy needed for pyrolysis, thus Pyrolysis can be realized at a temperature of 350-550 DEG C, improve pyrolysis efficiency, so as to substantially reduce two English growing amounts, reduce Tail gas clean-up difficulty.

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, Another upper lateral part of pyrolysis smoke forced condensation case 7 is provided with the second outlet flue 7-5, pyrolysis smoke forced condensation case 7 it is another Side lower part is provided with blowoff valve 7-6.

Preferably, described condenser pipe 7-1 is made using pipe, its effect is supercooled water；Flue gas streams dividing plate 7-2 is made using steel plate, and its effect is the space that layering separates in casing, pyrolysis smoke is passed through according to the route of design；Resistance Stream plate 7-3 is metallic plate of the square central with circular hole, and its effect is that flow-disturbing increases resistance, increases the contact area of cooled flue gas； Smoke inlet 7-4 is designed for hollow flange coil structures, and its effect is to allow pyrolysis smoke to enter in cooling cylinder；One end of outlet flue 7-5 The steel pipe of adpting flange is welded with, its effect is smoke；Blowoff valve 7-6 is ball valve design, and its effect is control Jing forced condensations The fluid of generation.

Preferably, described Water spray purifying box 12 is internally provided with the first flow-disturbing dividing plate 12-1, and pass through first The inside of Water spray purifying box 12 is divided into demisting layer 12-2 and packing layer 12-3 by flow-disturbing dividing plate 12-1, is set on packing layer 12-3 Several atomizer 12-4 are equipped with, several atomizer 12-4 are connected with several spiral nozzle 12-5 by pipeline, several spirals Shower nozzle 12-5 is arranged in screw spraying pipeline 12-6, is provided with several observation window 12-7, spiral on screw spraying pipeline 12-6 One end of spray piping 12-6 is connected with Water spray purifying box 12, the other end and the absorption pipeline 12-8 of screw spraying pipeline 12-6 Connection, is provided with choked flow adsorption layer 12-9 in absorption pipeline 12-8, and the one end for adsorbing pipeline 12-8 is connected with abutted flange 12- 10, the top of Water spray purifying box 12 is provided with access panel 12-11, and 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 is connected with the second external water tank 14.

Preferably, the effect of the first described flow-disturbing dividing plate 12-1 is to change gas-liquid direction；Demisting layer 12-2 and filler Layer 12-3 is a kind of filler, and its effect is to increase contact with flue gas respectively, retain the water smoke in flue gas and increase flue gas and The contact of absorbing liquid；The effect of atomizer 12-4 and spiral nozzle 12-5 is sprinkling absorbing liquid；Screw spraying pipeline 12-6 is A kind of spiral pipeline of inside cavity, its effect are to increase contact of the flue gas with absorbing liquid；Absorption pipeline 12-8 is a kind of Hollow pipe, its effect was flue gas；Choked flow adsorption layer 12-9 is a kind of filler, and its effect is to increase resistance, increases flue gas Contact area；Outlet flue 12-12 refers to the pipeline with adpting flange, and its effect is waste gas discharge outlet.

Preferably, described smog diversion three-way 17 is straight-through 17-1 and one by a level for being located at center 90 degree of threeway 17-3 compositions of 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 fixation is bolted, 90 degree of threeway 17-3 of two pieces are connected with water smoke treatment box 18 respectively by flange.

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, square outlet flange 18-5, the second blowdown window 18-6, maintenance window 18-7, case Body 18-8 is constituted, and circular inlet flange 18-1 is located at the top side of casing 18-8, Pall ring filler foam-removing layer 18-2 and eddy flow Demisting layer 18-3 is separated by the second flow-disturbing dividing plate 18-4 positioned at the inside of casing 18-8, and square outlet flange 18-5 is located at eddy flow The top side of demisting layer 18-3 upper box body 18-8.

Preferably, described circular inlet flange 18-1 is air inlet, its effect is that waste gas is entered from entrance；Bauer Ring filler foam-removing layer 18-2 is a kind of filler, and its effect is the contact surface of increase and waste gas, retains the foam in waste gas；Eddy flow is removed Mist layer 18-3 is rotational flow plate defroster, and its effect is the centrifugal force of the function using spiral board change axle stream into eddy flow and eddy flow generation Demisting is carried out, the droplet except under is flowed down along plate face periphery；The effect of the second flow-disturbing dividing plate 18-4 is that flow-disturbing changes exhaust gas direction；Side Shape outlet flange 18-5 is waste gas outlet, and its effect is the outlet of the waste gas Jing after retention demisting.

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, in electrostatic field case 19-4, electrostatic field case 19-4 is arranged on square outlet flange to honeycomb fashion cooking fume remover 19-1 On 18-5, the fixation of the first flue gas pipeline 19-5 bolts is provided with electrostatic field case 19-4 and is communicated to photodissociation formula cooking fume remover 19- 2, photodissociation formula cooking fume remover 19-2 are fixed by the second flue gas pipeline 19-6 bolts and are communicated to secondary pyrolysis heater 19-3；It is high During pressure electrostatic field, in the presence of high voltage electric field, soot gas ionization, mist of oil are charged, and major part is able to carbonization of degrading, small part Oil or fat particles absorption electric field electric field force and airflow function under move to the positive/negative plate of electric field be collected on pole plate and In the presence of self gravitation, to draw-off tray, the discharge of Jing oil drain passages, remaining micron order mist of oil are degraded into titanium dioxide by electric field to stream Carbon and water, while in the presence of high tension generator, in electric field, air produces ozone, eliminates most abnormal smells from the patient in flue gas, Gas after static electric field process enters photodissociation formula cooking fume remover 19-2 by flue gas pipeline 19-5, in Ultraviolet-C wave band Change the strand of tail gas oil in the presence of light, at the same with oxygen reaction after produce ozone, ozone is by oily molecule cold burning Water and ozone is generated afterwards, while the abnormal flavour in flue gas is also eliminated therewith, the tail gas after process enters secondary by flue gas pipeline 19-6 Pyrolysis heater 19-3, its operating temperature of electric heating control are used for secondary for (about 3 seconds) in 1000-1200 DEG C and gas residence time Heating, high temperature remove harmful gass in flue gas.

Preferably, the effect of described honeycomb fashion cooking fume remover 19-1 is electrostatic precipitation removes abnormal smells from the patient；Photodissociation formula oil smoke The effect of depurator 19-2 is that deodorization eliminates the unusual smell；The effect of secondary pyrolysis heater 19-3 is to remove in flue gas to be harmful to by high temperature Gas；The effect of electrostatic field case 19-4 is to place honeycomb fashion cooking fume remover 19-1；

Preferably, the inside of described activated carbon adsorption chimney 21 is filled with activated carbon, activated carbon adsorption chimney 21 is pacified It is mounted in the side of secondary pyrolysis heater 19-3, activated carbon adsorption chimney 21 and secondary pyrolysis heater 19-3 are by bracing frame 22 Support is fixed.

This specific embodiment adopts more advanced rational technological process, simple sorting, magnetization pyrolysis treatment furnace, pyrolysis cigarette Gas forced condensation, Water spray purification, the process of water smoke filler, electrostatic precipitation deodorization, photodissociation deodourizing, the secondary pyrolysis of temperature control, work Property charcoal absorption chimney, up to more than 95%, the tar produced during refuse pyrolysis fume treatment, condensate become silted up garbage disposal rate Filler in mud and purifier, Jing precipitation clarifying treatment, the water after clarification can be condensed or spray cleaning water is used, and condense Thing can be sent magnetization pyrolysis treatment furnace back to and be processed, and non-secondary pollution does not produce waste water, does not produce 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 specific embodiment is by adjusting the stream for magnetizing gas flow and control pyrolysis smoke that air magnetizator is entered Measure to control refuse pyrolysis temperature, it is to avoid produce two English, the flue gas for producing is pyrolyzed through pressure smoke abatement tar removing and tail gas end End processes to reclaim clarifying smoke gas, and remaining gas are discharged by blowdown stack, in the form of house refuse burns house refuse, Once light a fire, without adding any fuel, low cost occupation of land is little, and Operation and Maintenance maintenance is simple, and pyrolysis decrement is significantly, continuable Pyrolysis processing house refuse, energy-conserving and environment-protective effective can be realized deodorize and suppress the harmful gass such as two English and flue dust Discharge.

Ultimate principle of the present utility model and principal character and advantage of the present utility model has been shown and described above.One's own profession The technical staff of industry it should be appreciated that this utility model is not restricted to the described embodiments, described in above-described embodiment and description Simply illustrate principle of the present utility model, on the premise of without departing from this utility model spirit and scope, this utility model is also Various changes and modifications are had, these changes and improvements are both fallen within the range of claimed this utility model.This utility model Claimed scope is by appending claims and its equivalent thereof.

Claims (7)

1. a kind of house refuse magnetization is pyrolyzed treating stations, it is characterised in that：It includes feed arrangement (1), tank bracket (4), electrical equipment control Device (5) processed, magnetization pyrolysis treatment furnace body of heater (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 spiral shell Rotation conveyer device (3) composition, the lower section side of feed arrangement (1) are provided with tank bracket (4), tank bracket (4) and are provided with electrical equipment control Device (5), the lower section opposite side of feed arrangement (1) are provided with magnetization pyrolysis treatment furnace body of heater (6), magnetization pyrolysis treatment furnace body of heater (6) pyrolysis smoke forced condensation case (7) is provided with, water inlet pipe and water outlet pipe (8) and first on pyrolysis smoke forced condensation case (7), is connected with External water tank (9) is connected, and is provided with the first delivery pump (10) on water inlet pipe and water outlet pipe (8), under pyrolysis smoke forced condensation case (7) Side is provided with bracing frame (11), and pyrolysis smoke forced condensation case (7) is connected with Water spray purifying box (12) by flue gas pipeline, water Spray header (13) is connected with spray cleaning case (12), and is connected with the second external water tank (14) by spray header (13), It is provided with the second delivery pump (15) on spray header (13), the two ends of air-introduced machine (16) are gone out with Water spray purifying box (12) respectively Mouth is straight-through with the level of smog diversion three-way (17) to be connected, 90 degree of threeways and the water smoke treatment box of smog diversion three-way (17) (18) it is connected, on water smoke treatment box (18), sets tail gas terminal processing system (19), tail gas terminal processing system (19) passes through flue gas Pipeline (20) is connected with activated carbon adsorption chimney (21), and described magnetization pyrolysis treatment furnace body of heater (6) is internally provided with one Circular refractory burner hearth (6-1), the outer wrap of circular refractory burner hearth (6-1) have heat-insulation magnetic wall (6-2), magnetization pyrolysis treatment furnace The poly- petticoat pipe of octahedra taper (6-3) is provided with above body of heater (6), and is fixed by several screws, the poly- petticoat pipe of octahedra taper (6-3) flue gas through flange pipe (6-4) is provided with the top of, and is fixed by several bolts, magnetization pyrolysis treatment furnace body of heater (6) It is connected with pyrolysis smoke forced condensation case (7) by flue gas through flange pipe (6-4), magnetization pyrolysis treatment furnace body of heater (6) The turbulent valve (6-5) of several regulations is provided with bottom, adjusts turbulent valve (6-5) with permanent magnetism air magnetizator (6-6) by screw thread Connection, passes through spiral shell between the internal turbulent fire grate (6-7) of permanent magnetism air magnetizator (6-6) and magnetization pyrolysis treatment furnace body of heater (6) Stricture of vagina is fastenedly connected, and the bottom surrounding of magnetization pyrolysis treatment furnace body of heater (6) is respectively provided with a deashing fire door (6-8), described circle Refractory burner hearth (6-1) is made up of refractory brick or refractory cement, 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 treatment furnace body of heater (6) by several rivets, heat-insulation magnetic wall (6- 2) it is by a not magnetic conduction hollow pipe and forever by refractory cement and permanent magnet group into, described permanent magnetism air magnetizator (6-6) to be Magnet is constituted, and the cylindrical two ends of hollow pipe are screw thread, and one end of permanent magnet not homopolarity is placed in hollow pipe at a distance of 10 millimeters.

2. a kind of house refuse magnetization according to claim 1 is pyrolyzed 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) are provided with smoke inlet (7-4), pyrolysis smoke forced condensation case (7) another upper lateral part is provided with the first outlet flue (7-5), and another side lower part of pyrolysis smoke forced condensation case (7) is provided with Blowoff valve (7-6), described condenser pipe (7-1) are made using pipe, and flue gas streams dividing plate (7-2) to be made using steel plate, resistance Stream plate (7-3) is metallic plate of the square central with circular hole, and smoke inlet (7-4) is that hollow flange coil structures are designed, blowoff valve (7-6) For ball valve design.

3. a kind of house refuse magnetization according to claim 1 is pyrolyzed treating stations, it is characterised in that：Described Water spray is net Change the first flow-disturbing dividing plate (12-1) that is internally provided with of case (12), and pass through the first flow-disturbing dividing plate (12-1) by Water spray purifying box (12) inside is divided into demisting layer (12-2) and packing layer (12-3), is provided with several atomizers on packing layer (12-3) (12-4), several atomizer (12-4) are connected with several spiral nozzles (12-5) by pipeline, several spiral nozzle (12-5) It is arranged in screw spraying pipeline (12-6), on screw spraying pipeline (12-6), is provided with several observation windows (12-7), spiral spray The one end in shower pipe road (12-6) is connected with Water spray purifying box (12), the other end and the absorption pipeline of screw spraying pipeline (12-6) (12-8) connect, in absorption pipeline (12-8), be provided with choked flow adsorption layer (12-9), the one end for adsorbing pipeline (12-8) is connected with Abutted flange (12-10), is provided with access panel (12-11) above Water spray purifying box (12), Water spray purifying box (12) Side is provided with the second outlet flue (12-12), is provided with several first blowdown window (12- below Water spray purifying box (12) 13), Water spray purifying box (12) is connected with the second external water tank (14) by connecting pipeline (12-14).

4. a kind of house refuse magnetization according to claim 1 is pyrolyzed treating stations, it is characterised in that：Described smog shunting Threeway (17) is the two pieces by a level for being located at center straight-through (17-1) and a hollow barrel pipe (17-2) and 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 Fixation is connect, 90 degree of threeways (17-3) of two pieces are connected with water smoke treatment box (18) respectively by flange.

5. a kind of house refuse magnetization according to claim 1 is pyrolyzed treating stations, it is characterised in that：Described water smoke is processed 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 outlet flange (18-5), the second blowdown window (18-6), maintenance window (18-7), casing (18-8) composition, circle Shape inlet flange (18-1) is located at the top side of casing (18-8), Pall ring filler foam-removing layer (18-2) and vortex-flow and defrosting layer (18-3) positioned at the inside of casing (18-8), separated by the second flow-disturbing dividing plate (18-4), square outlet flange (18-5) is located at rotation The top side of stream demisting layer (18-3) upper box body (18-8).

6. a kind of house refuse magnetization according to claim 1 is pyrolyzed 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 are net Change device (19-1) to be arranged in electrostatic field case (19-4), electrostatic field case (19-4) is on square outlet flange (18-5), quiet The fixation of the first flue gas pipeline (19-5) bolt is provided with electric field case (19-4) is communicated to photodissociation formula cooking fume remover (19-2), light Solution formula cooking fume remover (19-2) is fixed by the second flue gas pipeline (19-6) bolt and is communicated to secondary pyrolysis heater (19-3).

7. a kind of house refuse magnetization according to claim 1 is pyrolyzed 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 by bracing frame (22) and are fixed.