CN203893189U - Incineration cracking type garbage harmless treatment device - Google Patents
Incineration cracking type garbage harmless treatment device Download PDFInfo
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- CN203893189U CN203893189U CN201420261627.8U CN201420261627U CN203893189U CN 203893189 U CN203893189 U CN 203893189U CN 201420261627 U CN201420261627 U CN 201420261627U CN 203893189 U CN203893189 U CN 203893189U
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- 239000010813 municipal solid waste Substances 0.000 title claims abstract description 68
- 238000005336 cracking Methods 0.000 title claims abstract description 58
- 238000002485 combustion reaction Methods 0.000 claims abstract description 92
- 239000007789 gas Substances 0.000 claims description 22
- 238000012545 processing Methods 0.000 claims description 19
- 238000010304 firing Methods 0.000 claims description 16
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 12
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- Incineration Of Waste (AREA)
Abstract
The utility model relates to the technical field of garbage treatment devices of environmental protection equipment, in particular to an incineration cracking type garbage harmless treatment device. The outlet of a mixed smoke output pipe of a primary cracking furnace is communicated with the inner cavity of a secondary combustion chamber, a blowing pipe for flowing fresh air into the inner cavity of the secondary combustion chamber and a blower disposed on the blowing pipe are arranged on the lateral wall of the secondary combustion chamber, and the lower portion of the secondary combustion chamber is provided with an exhaust port and a slagging port. The incineration cracking type garbage harmless treatment device has the advantages that household garbage, industrial wastes, medical wastes and sludge and biomass thereof are cracked, gasified and incinerated, and reutilization, reduction and harmlessness of solid wastes are achieved.
Description
Technical field
The utility model relates to the technical field of the refuse disposal installation of environmental protection equipment, especially relate to and a kind of house refuse, trade waste, Biohazard Waste, mud and living beings thereof etc. are carried out to pyrolysis gasification burning disposal, make it reach solid waste resource recovery, minimizing, innoxious burning cracking type rubbish processing to be harmless device.
Background technology
Along with the development of national Promoting Urbanization scale, urbanization brings densely populated, thereby bring a large amount of house refuses and the generation of trade waste, had a strong impact on the development in city and the restriction present situation that creates civilized communities, become serious social effects of pollution problem.
At present, the basic mode of processing house refuse mainly contains three kinds: composting process, landfill method, burning method.The defect that these three kinds of processing modes exist is: 1, composting process can not make the complete harmless treatment of discarded object, can only process a part wherein, is difficult to adapt to the needs of current social development; 2, landfill method has not only taken a large amount of soils, decomposes slowly, and the time cycle is long, and easily pollutes the ecological environment of periphery; 3, burning method is that in three kinds of methods, effect is best, easily make the processing of solid waste realize resource, minimizing, innoxious requirement, also be a kind of method that innoxious degree is the highest simultaneously, mainly that its solid waste is placed in to high temperature furnace, making wherein combustible component reduce under high temperature anaerobic condition can burning fume, and in a kind of method of dual firing chamber and the abundant mixed combustion of excess air, and the high-temperature flue gas producing is absorbed heat for generating or is heated by waste heat boiler.
Therefore, in some developed countries, wide model has adopted solid waste incineration disposal method, and adopts larger grate furnace or the vulcanization bed waste incineration complete set of equipments technology of day output, also has some small and medium cities pyrolyzing, gasifying and incinerating complete set of equipments technology.And incineration technology in above-mentioned roughly has following three kinds:
(1) grate incinerator operation principle: rubbish enters the fire grate (fire grate is divided into dry section, combustion zone, burning-out zone) under being tilted to by feed hopper, due to the crisscross motion between fire grate, rubbish is promoted downwards, make rubbish successively by the regional on fire grate (when rubbish You Yige district enters into another district, play an effect of standing up greatly), until after-flame is discharged burner hearth.The advantage of this technology is that feasibility is large, but extremely uneconomical, not only invest high, floor space is large, and operation energy consumption is high, cost is large, it is the waste to social device resource, because of grate furnace complicated in mechanical structure, spoilage is high again, and maintenance is large, grate furnace cost and maintenance cost are high, make it difficult applying of China.
(2) fluidized bed incinerator operation principle: body of heater is made up of multihole distributor adds a large amount of quartz sand in burner hearth, quartz sand is heated to more than 600 DEG C, and blasts more than 200 DEG C hot blasts at furnace bottom, hot sand is seethed with excitement, then drop into rubbish.Rubbish seethes with excitement together with hot sand, and rubbish is dried very soon, catches fire, burns.Unburnt rubbish proportion is lighter, continues Boiling Combustion, and the rubbish proportion of after-flame is larger, falls furnace bottom, after water-cooled, with screening installation, thick slag, thin slag is delivered to outside factory, and a small amount of medium slag and quartz sand are sent back in stove and continued to use by lifting means.Shortcoming: fluidized bed combustion is abundant, in stove, burning is controlled better, but in flue gas, amount of dust is large, complicated operation, and operating cost is higher, higher to fuel granularity uniformity requirement, needs powerful breaker, and quartz sand is serious to equipment attrition, and plant maintenance amount is large.
(3) incinerator for thermal decomposition operation principle: the mode that rubbish can continuous and quantitative enters incinerator, experience heating---dry---pyrolysis---gasification---process of solid combustible after-flame.In the flue gas producing in first-stage firing chamber, contain a large amount of fuel gas, then enter dual firing chamber and fully mix with the excess air adding, implement oxygen-excess combustion, the pernicious gas of rubbish generation is thoroughly decomposed.It is a kind of novel refuse treatment plant, because it has the features such as compact conformation, operating cost is low, exhaust emissions is effective.Shortcoming: waste incineration day output is little, and pyrolysis is insufficient, visible high temperature naked light in incinerator, easily coking at the middle and upper levels in stove, overhauls ordinaryly, and maintenance workload is large.In addition, arranging of rotary fire grate is equally also for dispersed rubbish, but in the time that the solid waste things such as rubbish are larger by the volume of the residue thing after burning, just easily occur the phenomenon that fire grate is stuck, thereby affect the continuous use of incinerator.
Summary of the invention
The deficiency existing for above-mentioned prior art, that the purpose of this utility model is to provide is a kind of efficient, energy-saving and environmental protection and sustainable work, and makes solid waste resource recovery, minimizing, innoxious burning cracking type rubbish processing to be harmless device and rubbish processing to be harmless technique thereof.
For realizing above-mentioned object, the utility model provides following technical scheme:
A kind of cracking type rubbish processing to be harmless device that burns, comprise one-level cracking funace, one-level cracking funace comprises gear chamber, be located at body of heater and the feed pipe on gear chamber top, the mixed flue gas efferent duct that the scum pipe of body of heater downside and body of heater top are communicated with body of heater inner chamber, gear motor in gear chamber drives driving gearshaft to rotate by travelling gear, bottom-up residue fire grate and the fire grate of being respectively equipped with in close furnace bottom position in described body of heater, described residue fire grate is connected with the driving gearshaft stretching in body of heater from the axis hole at gear chamber top, on the sidewall of described lower portion of furnace body, be respectively equipped with fire hole, thermometer hole, peep hole, described feed pipe is located on the lateral wall of upper of furnace body and is communicated with body of heater inner chamber, in feed pipe, be provided with to be driven to move back and forth by piston motor material is pushed to the feed ram in body of heater, the outlet of described mixed flue gas efferent duct is communicated with the inner chamber of secondary combustion chamber, on the sidewall of secondary combustion chamber, be provided with to secondary combustion chamber's inner chamber and be blown into the gas blow pipe of fresh air and be arranged on the hair-dryer on gas blow pipe, the bottom of secondary combustion chamber is provided with exhaust outlet and slag-drip opening.
The utility model is further set to: described secondary combustion chamber comprises the first combustion chamber of horizontally set and the second combustion chamber vertically arranging, one end of the first combustion chamber is communicated with the body of heater inner chamber top of one-level cracking funace by tube connector, the other end of the first combustion chamber is communicated with by transition conduit with the top of the second combustion chamber, in transition conduit, be connected with the air exhauster that the gas producing in body of heater is extracted into the first combustion chamber and is delivered to the second combustion chamber, described exhaust outlet and slag-drip opening are arranged on the bottom of the second combustion chamber.
The utility model is further set to: the sidewall of described body of heater upside is provided with upper observation hole, the inner chamber upside of described body of heater is provided with two-fluid pipe, two-fluid pipe is connected with cesspool by external water pumper, and the two-fluid pipe that is positioned at body of heater inner chamber is provided with atomizer.
The utility model is further set to: in described the first combustion chamber and the second combustion chamber, be equipped with temperature sensor, on the first combustion chamber and the second combustion chamber, be respectively equipped with blowdown pipe, controller is compared with setting signal according to the temperature signal of described temperature sensor transmission, control with this air capacity that blowdown pipe is blown into the first combustion chamber and the second combustion chamber, and then control and be blown into the indoor amount of oxygen of secondary firing to control the ignition temperature in the first combustion chamber and the second combustion chamber.
The utility model is further set to: described driving gearshaft offers air inducing hole one time along its axis, and one time air inducing hole communicates with body of heater inner chamber.
The utility model is further set to: described fire grate is provided with three, and three fire grates are triangular shape or in-line laterally interts in body of heater inside, and the longitudinal cross-section shape of fire grate is hexagon, and the outer surface of every fire grate is equipped with several burrs.
The utility model is further set to: as a kind of rubbish processing to be harmless technique of burning cracking type rubbish processing to be harmless device described in above-mentioned, realized by following steps:
(1) rubbish is inserted in garbage pool, rubbish in garbage pool is sent into one-level cracking incinerator by manipulator and feed pipe and carry out primary combustion cracking, in the process of burning cracking, on described rubbish or to one-level cracking incinerator inner chamber, continue from top to bottom to spray the sewage from extracting in cesspool by two-fluid pipe and water pumper, the rubbish ash that burning produces is discharged from the scum pipe of one-level cracking incinerator, sewage is sprayed to and on rubbish, burns or sewage is sprayed in one-level cracking incinerator inner chamber and is burnt, there is redox reaction, H2O+C at high temperature forms water-gas, partial combustion deposits yields sulfide, nitride is Ji bioxin,
(2) gas one-level cracking incinerator burning or cracking rubbish and sewage being produced sends into that secondary firing is indoor carries out second-time burning, in the process of second-time burning, be blown into the indoor amount of fresh air of secondary firing by control and control the indoor ignition temperature of secondary firing at 800 DEG C-1200 DEG C, at least 2 seconds time of staying of burning, the flying dust that second-time burning the produces part that sinks is discharged from the ash discharging hole of secondary combustion chamber, and the material of second-time burning is mainly that the water-gas that produces of primary combustion, sulfide, nitride are Ji bioxin.
The utility model is further set to: described sewage is that the sewage that goes out from the rubbish filtering in garbage pool is or/and the sewage producing from other channel.
The utility model is further set to: described rubbish is industrial refuse, and industrial refuse contains poisonous and harmful substance, and poisonous and harmful substance comprises heavy metal, cement, brick and tile, fiber, cast stone.
The utility model is further set to: the indoor ignition temperature of described secondary firing is 1100 DEG C.
By adopting technique scheme, the technique effect that the utility model reaches is:
1, occasionally disposal of refuse timely, there will not be rubbish bulk deposition to produce stench and some other to health and the influential gas of environment, and efficiency is higher, in the process of whole work, when adding rubbish and the stove after burning being mixed to eliminating, whole equipment is without quitting work, and equipment can reach the function of sustainable work;
2, in the process of burning, be all that the gas that utilizes incineration firing to produce carries out second-time burning, the energy of second-time burning can further be changed into electric energy or other purposes all can, in whole process, can not produce waste gas and waste water etc. and environmental protection be had to the object of impact, not only energy-conservation but also environmental protection, can accomplish refuse reclamation to rubbish, in the situation that environmental protection being accomplished to certain contribution, also ensure that the rubbish producing in life and industry has obtained dealing carefully with;
3, various rubbish all can be accomplished to focus on, without classification, so just accomplish the pooling of resources of garbage disposal, and in whole work, although can mix by generating portion stove, but with respect to traditional technology, the assorted minimizing much of stove of product, ashes amount after burning is greatly reduced, and be almost not have ashes in secondary combustion chamber, after burning by one-level cracking funace to secondary combustion chamber, most poisonous and hazardous material is by cracking in high temperature, only need in follow-up smokejack, add basic some except nitre denitrogenate and the device of dedusting can make to be discharged to atmosphere in gas nontoxic, to having of environmental resource very large guarantee,
4, be the sewage producing in rubbish to the sewage spraying in one-level cracking funace, effectively accomplish the cyclic utilization of waste, effectively saved the waste of the water resource of depending on for existence.
Brief description of the drawings
Below in conjunction with accompanying drawing, the utility model is described in further detail.
Fig. 1 is structural principle schematic diagram of the present utility model.
Fig. 2 is the ignition temperature diagram of each layer in one-level cracking funace of the present utility model.
Wherein, 10 is gear chamber, and 11 is body of heater, and 12 is feed pipe, 13 is feed ram, and 14 is piston motor, and 15 is mixed flue gas efferent duct, and 16 is scum pipe, 17 is that gear motor, 18 is travelling gear, and 19 is driving gearshaft, and 20 is residue fire grate, and 21 is fire grate, 22 is fire hole, and 23 is thermometer hole, and 24 is peep hole, and 25 is an air inducing hole, 26 is two-fluid pipe, and 27 is the first combustion chamber, and 28 is the second combustion chamber, and 29 is ash discharging hole, 30 is exhaust outlet, and 31 is air exhauster, and 32 is upper observation hole.
Detailed description of the invention
As shown in Figure 1, for the disclosed a kind of cracking type rubbish processing to be harmless device that burns of the utility model, comprise one-level cracking funace, one-level cracking funace comprises gear chamber 10, be located at body of heater 11 and the feed pipe 12 on gear chamber 10 tops, the mixed flue gas efferent duct 15 that the scum pipe 16 of body of heater 11 downsides and body of heater 11 tops are communicated with body of heater 11 inner chambers, gear motor 17 in gear chamber 10 drives driving gearshaft 19 to rotate by travelling gear 18, described body of heater 11 is inner near bottom-up residue fire grate 20 and the fire grate 21 of being respectively equipped with in furnace bottom position, described residue fire grate 20 is connected with the driving gearshaft 19 stretching in body of heater 11 from the axis hole at gear chamber 10 tops, on the sidewall of described body of heater 11 bottoms, be respectively equipped with fire hole 22, thermometer hole 23, peep hole 24, described feed pipe 12 is located on the lateral wall on body of heater 11 tops and is communicated with body of heater 11 inner chambers, in feed pipe 12, be provided with to be driven to move back and forth by piston motor 14 material is pushed to the feed ram 13 in body of heater 11, the outlet of described mixed flue gas efferent duct 15 and the intracavity inter-connection of secondary combustion chamber, on the sidewall of secondary combustion chamber, be provided with to secondary combustion chamber's inner chamber and be blown into the gas blow pipe of fresh air and be arranged on the air blast 31 on gas blow pipe, the bottom of secondary combustion chamber is provided with exhaust outlet 30 and ash discharging hole 29.
In above-mentioned, described secondary combustion chamber comprises the first combustion chamber 27 of horizontally set and the second combustion chamber 28 vertically arranging, the first combustion chamber 27 is communicated with the body of heater 11 inner chamber tops of one-level cracking funace by tube connector, the other end of the first combustion chamber 27 is communicated with by transition conduit with the top of the second combustion chamber 28, in transition conduit, be connected with the air blast 31 that the gas of body of heater 11 interior generations is extracted into the first combustion chamber 27 and is delivered to the second combustion chamber 28, described exhaust outlet 30 and ash discharging hole 29 are arranged on the bottom of the second combustion chamber 28.Certainly secondary combustion chamber can be the independent combustion chamber of horizontally set or the combustion chamber of vertical setting, or also can in the combustion chamber in horizontal or vertical direction with certain inclination.
In above-mentioned, the sidewall of described body of heater 11 upsides is provided with upper observation hole 32, the inner chamber upside of described body of heater 11 is provided with two-fluid pipe 26, and two-fluid pipe 26 is connected by external water pumper and cesspool, and the two-fluid pipe that is positioned at body of heater 11 inner chambers is provided with atomizer.Described peep hole divides two-layer up and down, be mainly watch rubbish high-temperature cracking and cracking whether abundant, make its cracking technology process more intuitively transparent.On one-level cracking funace, be also provided with all kinds of instrument, mainly play monitoring and protection stove, make its performance optimum state.Peep hole can be understood cracking situation in stove timely and effectively, guarantees stove stable operation.
In above-mentioned, in described the first combustion chamber 27 and the second combustion chamber 28, be equipped with temperature sensor, on the first combustion chamber 27 and the second combustion chamber 28, be respectively equipped with blowdown pipe, controller is compared with setting signal according to the temperature signal of described temperature sensor transmission, control with this air capacity that blowdown pipe is blown into the first combustion chamber 27 and the second combustion chamber 28, and then control the amount of oxygen being blown in secondary combustion chamber 28 to control the ignition temperature in the first combustion chamber 27 and the second combustion chamber 28.
In above-mentioned, described driving gearshaft 19 offers air inducing hole 25,25, one times, an air inducing hole along its axis and communicates with body of heater 11 inner chambers.
In the present embodiment, in solid waste enters stove, as shown in Figure 2, in stove, be divided into dead level, drying layer, cleaving layer, Pintsch process layer, burning zone, after-flame layer and residual layer from top to bottom.Fire grate is between burning zone or burning zone and Pintsch process layer.Described dead level be mainly after the antipyretic gasification of solid waste can burning fume, temperature is 300 DEG C～450 DEG C or 300 DEG C～600 DEG C; Described drying layer is exactly solid waste stacking place, plays drying functions, and temperature is 200 DEG C～500 DEG C; Described cleaving layer is that part solid waste starts gasification reaction, and temperature is 550 DEG C～800 DEG C; Described Pintsch process layer is exactly that the cracking under high temperature anaerobic condition of most of solid waste becomes fuel gas, and temperature is 600 DEG C～1000 DEG C; Described burning zone be exactly solid waste just at high-temp combustion, for cracking above provides enough temperature, temperature is 500 DEG C～1000 DEG C; Described after-flame layer is exactly the product after burning, and temperature is 300 DEG C～450 DEG C or 300 DEG C～800 DEG C; Described residual layer is exactly the slag that can not burn again, and temperature is 150 DEG C～400 DEG C or 300 DEG C～400 DEG C;---drying layer---cleaving layer---Pintsch process layer---cracking under the condition of anoxic after burning zone that rubbish in stove is through dead level, carbide after Pintsch process is constantly displaced downwardly to burning zone, and the Pintsch process burning away is so-called smouldering, in stove, produce a large amount of flammable mixed flue gas, under suction function, in a large number can burning fume enter the overall process of dual firing chamber and the abundant mixed combustion of excess air.
In above-mentioned, the required bed of material is stacked and highly also had certain requirement, because need enough bed depths in cracking reaction process, make it reach best cracking requirement, the general bed of material is stacked and is highly 4～5 meters.
In above-mentioned, described fire grate 21 is provided with three, article three, to be triangular shape or in-line built on stilts for fire grate 21, built on stilts setting is mainly to increase combustion space, for Pintsch process gasification provides condition for validity, and laterally intert in body of heater 11 inside, the longitudinal cross-section shape of fire grate 21 is hexagon, the appearance of every fire grate 21 is all provided with burr equably, with increasing friction force; Described three fire grates 21 and burr all adopt wear-resisting and high temperature resistant synthetic steel.
As a kind of rubbish processing to be harmless technique of burning cracking type rubbish processing to be harmless device described in above-mentioned, realized by following steps:
(1) rubbish is inserted in garbage pool, rubbish in garbage pool is sent into one-level cracking incinerator by manipulator and feed pipe and carry out primary combustion cracking, in the process of burning cracking, on described rubbish or to one-level cracking incinerator inner chamber, continue from top to bottom to spray the sewage from extracting in cesspool by two-fluid pipe and water pumper, the rubbish ash that burning produces is discharged from the scum pipe of one-level cracking incinerator, sewage is sprayed on rubbish to burning or sewage is sprayed to while burning in one-level cracking incinerator inner chamber, there is redox reaction, H
2o+C at high temperature forms water-gas, and partial combustion deposits yields sulfide, nitride are Ji bioxin;
(2) gas one-level cracking incinerator burning or cracking rubbish and sewage being produced sends into that secondary firing is indoor carries out second-time burning, in the process of second-time burning, be blown into the indoor amount of fresh air of secondary firing by control and control the indoor ignition temperature of secondary firing at 800 DEG C-1200 DEG C, at least 2 seconds time of staying of burning, the flying dust that second-time burning the produces part that sinks is discharged from the ash discharging hole of secondary combustion chamber, and the material of second-time burning is mainly that the water-gas that produces of primary combustion, sulfide, nitride are Ji bioxin.
Mixed flue gas enters dual firing chamber burning, and ignition temperature is at least greater than more than 850 DEG C, and the burning time of staying must have and is greater than more than 2 seconds.
Pyrolysis gasification incinerator in above-mentioned has complete pyrolysis gasification and burning to solid waste incineration, heat, after cracking fuel gas out to have good stability, sealing, gasification result good etc.It is unstable that this technique has overcome supplied materials, and refuse thermal value inequality and strong adaptability comprise the burning that can process various solid waste things, as house refuse, general industry rubbish, industrial solid castoff, biomass fuel and mud etc.
Described sewage returns pressure spray process and mainly utilizes garbage, waste-water as heat, pyrolysis gasification and Pintsch process carbon-coating generation reduction reaction, produces more fuel gas.Owing to adding a small amount of free state waste water, be conducive to adjustments of gas structural constituent, improve fuel gas quality, at high temperature form the fuel gas such as flammable water-gas simultaneously.Remove the tar that produces and the thorough decomposition of harmful substance in Pintsch process, reduced the intensity of exhaust gas purification system below, reduced a whole set of process costs, and greatly solved a social difficult problem for dispose of sewage difficulty, high in cost of production destructor plant.Be conducive to the development of environmental protection cause, really reach without waste water, the discharge such as pollution-free.
In above-mentioned, described sewage is that the sewage that goes out from the rubbish filtering in garbage pool is or/and the sewage producing from other channel.Described rubbish is industrial refuse, and industrial refuse contains poisonous and harmful substance, and poisonous and harmful substance comprises heavy metal, cement, brick and tile, fiber, cast stone.The indoor ignition temperature of described secondary firing is 1100 DEG C.
In above-mentioned, described waste water returns spray technique and is effectively blocked in the flying dust producing in pyrolysis gasification burning process, complete equipment is played better protection and is increased the service life simultaneously.Described stove negative pressure, is that solid waste thing need to make it the reduction reaction that gasifies in heat, cracking under anoxia condition, also ensures that stench phenomenon does not occur rubbish in burning process simultaneously.Described solid waste treatment processes, without adding any combustible, realizes thoroughly and burning, thereby reaches the requirement of saving the energy.
Above-described embodiment is only preferred embodiment of the present utility model, not limits according to this protection domain of the present utility model, therefore: all equivalences of doing according to structure of the present utility model, shape, principle change, within all should being covered by protection domain of the present utility model.
Claims (6)
1. one kind is burned cracking type rubbish processing to be harmless device, comprise one-level cracking funace, one-level cracking funace comprises gear chamber, be located at body of heater and the feed pipe on gear chamber top, the mixed flue gas efferent duct that the scum pipe of body of heater downside and body of heater top are communicated with body of heater inner chamber, gear motor in gear chamber drives driving gearshaft to rotate by travelling gear, bottom-up residue fire grate and the fire grate of being respectively equipped with in close furnace bottom position in described body of heater, described residue fire grate is connected with the driving gearshaft stretching in body of heater from the axis hole at gear chamber top, on the sidewall of described lower portion of furnace body, be respectively equipped with fire hole, thermometer hole, peep hole, described feed pipe is located on the lateral wall of upper of furnace body and is communicated with body of heater inner chamber, in feed pipe, be provided with to be driven to move back and forth by piston motor material is pushed to the feed ram in body of heater, it is characterized in that: the outlet of described mixed flue gas efferent duct is communicated with the inner chamber of secondary combustion chamber, on the sidewall of secondary combustion chamber, be provided with to secondary combustion chamber's inner chamber and be blown into the gas blow pipe of fresh air and be arranged on the hair-dryer on gas blow pipe, the bottom of secondary combustion chamber is provided with exhaust outlet and slag-drip opening.
2. a kind of cracking type rubbish processing to be harmless device that burns according to claim 1, it is characterized in that: described secondary combustion chamber comprises the first combustion chamber of horizontally set and the second combustion chamber vertically arranging, one end of the first combustion chamber is communicated with the body of heater inner chamber top of one-level cracking funace by tube connector, the other end of the first combustion chamber is communicated with by transition conduit with the top of the second combustion chamber, in transition conduit, be connected with the air exhauster that the gas producing in body of heater is extracted into the first combustion chamber and is delivered to the second combustion chamber, described exhaust outlet and slag-drip opening are arranged on the bottom of the second combustion chamber.
3. a kind of cracking type rubbish processing to be harmless device that burns according to claim 2, it is characterized in that: in described the first combustion chamber and the second combustion chamber, be equipped with temperature sensor, on the first combustion chamber and the second combustion chamber, be respectively equipped with blowdown pipe, controller is compared with setting signal according to the temperature signal of described temperature sensor transmission, control with this air capacity that blowdown pipe is blown into the first combustion chamber and the second combustion chamber, and then control and be blown into the indoor amount of oxygen of secondary firing to control the ignition temperature in the first combustion chamber and the second combustion chamber.
4. a kind of cracking type rubbish processing to be harmless device that burns according to claim 1, it is characterized in that: the sidewall of described body of heater upside is provided with upper observation hole, the inner chamber upside of described body of heater is provided with two-fluid pipe, two-fluid pipe is connected with cesspool by external water pumper, and the two-fluid pipe that is positioned at body of heater inner chamber is provided with atomizer.
5. a kind of cracking type rubbish processing to be harmless device that burns according to claim 1, is characterized in that: described driving gearshaft offers air inducing hole one time along its axis, and one time air inducing hole communicates with body of heater inner chamber.
6. a kind of cracking type rubbish processing to be harmless device that burns according to claim 5, it is characterized in that: described fire grate is provided with three, three fire grates are triangular shape or in-line laterally interts in body of heater inside, the longitudinal cross-section shape of fire grate is hexagon, and the outer surface of every fire grate is equipped with several burrs.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420261627.8U CN203893189U (en) | 2014-05-19 | 2014-05-19 | Incineration cracking type garbage harmless treatment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420261627.8U CN203893189U (en) | 2014-05-19 | 2014-05-19 | Incineration cracking type garbage harmless treatment device |
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| CN203893189U true CN203893189U (en) | 2014-10-22 |
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| CN201420261627.8U Expired - Lifetime CN203893189U (en) | 2014-05-19 | 2014-05-19 | Incineration cracking type garbage harmless treatment device |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103953931A (en) * | 2014-05-19 | 2014-07-30 | 张文国 | Incineration cracking type innocent garbage treatment device and process |
| CN105485691A (en) * | 2016-01-07 | 2016-04-13 | 厦门青山绿水再生资源有限公司 | Suspension type combustion, carbonization and splitting integrated equipment |
| CN105605583A (en) * | 2016-03-15 | 2016-05-25 | 台州汇一贵金属贸易有限公司 | Rubbish cracking still |
| CN106482127A (en) * | 2016-11-19 | 2017-03-08 | 无锡市智锋金属科技有限公司 | With the furnace chamber that may move fire grate |
| CN107388267A (en) * | 2017-09-01 | 2017-11-24 | 嵊州市科灵机械有限公司 | A kind of gasification furnace |
| CN113983475A (en) * | 2021-11-01 | 2022-01-28 | 贵州智杰生态环保科技有限公司 | Incinerator |
-
2014
- 2014-05-19 CN CN201420261627.8U patent/CN203893189U/en not_active Expired - Lifetime
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103953931A (en) * | 2014-05-19 | 2014-07-30 | 张文国 | Incineration cracking type innocent garbage treatment device and process |
| CN105485691A (en) * | 2016-01-07 | 2016-04-13 | 厦门青山绿水再生资源有限公司 | Suspension type combustion, carbonization and splitting integrated equipment |
| CN105605583A (en) * | 2016-03-15 | 2016-05-25 | 台州汇一贵金属贸易有限公司 | Rubbish cracking still |
| CN106482127A (en) * | 2016-11-19 | 2017-03-08 | 无锡市智锋金属科技有限公司 | With the furnace chamber that may move fire grate |
| CN107388267A (en) * | 2017-09-01 | 2017-11-24 | 嵊州市科灵机械有限公司 | A kind of gasification furnace |
| CN107388267B (en) * | 2017-09-01 | 2023-07-18 | 嵊州市科灵机械有限公司 | Gasification furnace |
| CN113983475A (en) * | 2021-11-01 | 2022-01-28 | 贵州智杰生态环保科技有限公司 | Incinerator |
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