CN108105777A - A kind of small continuous consumer waste incineration processing system - Google Patents

A kind of small continuous consumer waste incineration processing system Download PDF

Info

Publication number
CN108105777A
CN108105777A CN201810056142.8A CN201810056142A CN108105777A CN 108105777 A CN108105777 A CN 108105777A CN 201810056142 A CN201810056142 A CN 201810056142A CN 108105777 A CN108105777 A CN 108105777A
Authority
CN
China
Prior art keywords
outlet
gas
gas outlet
processing system
entrance
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
CN201810056142.8A
Other languages
Chinese (zh)
Other versions
CN108105777B (en
Inventor
耿长伟
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
BEIJING ZHONGLI XINDA ENVIRONMENTAL PROTECTION ENGINEERING Co.,Ltd.
Original Assignee
Guangzhou Li Shi Environmental Management Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Guangzhou Li Shi Environmental Management Co Ltd filed Critical Guangzhou Li Shi Environmental Management Co Ltd
Priority to CN201810056142.8A priority Critical patent/CN108105777B/en
Publication of CN108105777A publication Critical patent/CN108105777A/en
Application granted granted Critical
Publication of CN108105777B publication Critical patent/CN108105777B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • 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
    • F23G5/033—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment comminuting or crushing
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/02—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
    • F23G5/04—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment drying
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/08—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating
    • F23G5/14—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating including secondary combustion
    • F23G5/16—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating including secondary combustion in a separate combustion chamber
    • F23G5/165—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating including secondary combustion in a separate combustion chamber arranged at a different level
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/44—Details; Accessories
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/44—Details; Accessories
    • F23G5/442—Waste feed arrangements
    • F23G5/444—Waste feed arrangements for solid waste
    • 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
    • F23G5/46—Recuperation of heat
    • 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
    • F23J15/006—Layout of treatment plant
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J15/00—Arrangements of devices for treating smoke or fumes
    • F23J15/02—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material
    • F23J15/022—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material for removing solid particulate material from the gasflow
    • F23J15/025—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material for removing solid particulate material from the gasflow using filters
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J15/00—Arrangements of devices for treating smoke or fumes
    • F23J15/02—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material
    • F23J15/022—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material for removing solid particulate material from the gasflow
    • F23J15/027—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material for removing solid particulate material from the gasflow using cyclone separators
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J15/00—Arrangements of devices for treating smoke or fumes
    • F23J15/02—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material
    • F23J15/04—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material using washing fluids
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2201/00—Pretreatment
    • F23G2201/10—Drying by heat
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2201/00—Pretreatment
    • F23G2201/20—Dewatering by mechanical means
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2201/00—Pretreatment
    • F23G2201/80—Shredding
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2204/00—Supplementary heating arrangements
    • F23G2204/10—Supplementary heating arrangements using auxiliary fuel
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2205/00—Waste feed arrangements
    • F23G2205/12—Waste feed arrangements using conveyors
    • F23G2205/121—Screw conveyor
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2206/00—Waste heat recuperation
    • F23G2206/10—Waste heat recuperation reintroducing the heat in the same process, e.g. for predrying
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J2215/00—Preventing emissions
    • F23J2215/20—Sulfur; Compounds thereof
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J2217/00—Intercepting solids
    • F23J2217/10—Intercepting solids by filters
    • F23J2217/101—Baghouse type
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J2217/00—Intercepting solids
    • F23J2217/40—Intercepting solids by cyclones

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)

Abstract

The present invention relates to a kind of small continuous consumer waste incineration processing system, including burning preprocessing system, incineration system, air supply system, black smoke processing system and exhaust treatment system；Burning preprocessing system includes dustbin, rubbish Self-loading-unloading device, domestic garbage crusher, screw extruding feed device and drum-type garbage drying device；Incinerator includes feed system, incineration system, air supply system, black smoke processing system and exhaust treatment system；Black smoke processing system includes black smoke suction outlet and interlayer casing；Exhaust treatment system includes dry method device, half-dried subtraction unit and dust-extraction unit；The present invention has considered refuse breaking and the systematicness of dehydration, improve the air-tightness of incinerator, rubbish is promoted fully to burn, it more makes full use of except acid treatment, effectively remove the pollutants such as sour gas, organic pollution and particulate matter, it reduces secondary pollution to generate, achievees the purpose that drop low-cost high-efficiency environmental protection.

Description

A kind of small continuous consumer waste incineration processing system
Technical field
The present invention relates to technical field of domestic garbage treatment, are specially a kind of small continuous consumer waste incineration processing system System.
Background technology
In recent years, China's Small town economy rapidly develops, and is producing with generating substantial amounts of house refuse in process of consumption, raw If rubbish living is mishandling, certain soil can be not only occupied, wastes land resource, can also give out foul smell, grown each Kind bacterium；Samll cities and towns' Environmental Sanitation Infrastructures relatively lag behind, and house refuse is stacked everywhere, and dirty, unrest, poor problem are apparent, therefore small city It is imperative that town house refuse rationally handles disposal.
Have some small-sized consumer waste incineration pretreating devices currently on the market, but it is not a kind of be it is more common, all There are some defects or deficiency, such as：Crushing mechanism is too expensive, and flow is too long, and dehydration energy consumption is too big etc..
It is mechanical kiln grate furnace to be applied also more in small continuous domestic waste incineration process, however existing currently on the market Some mechanical kiln grate furnaces also have a little defects, first, feed system is not perfect, air-tightness device is not simple and effective enough；Second is that it burned The toxic gas generated in journey is too many, it should which optimization is internal as far as possible burns structure；Third, black smoke does not utilize, as pollutant Smoke processing system processing is sent into, resource had not only been wasted but also had added fume treatment expense；Fourth, landfill leachate is mostly using straight It connects to spray into incinerator and destroy, be affected to Refuse Incineration Process.
The content of the invention
It is an object of the invention in view of the above problems and deficiency, provide a kind of at low cost, efficient, environmentally friendly Small continuous consumer waste incineration processing system.
The technical proposal of the invention is realized in this way：A kind of small continuous consumer waste incineration processing system, including：
One burns preprocessing system, including dustbin, rubbish Self-loading-unloading device, domestic garbage crusher, screw extruding feeding dress It puts and drum-type garbage drying device；
Incineration system, air supply system, black smoke processing system and exhaust treatment system；
The incineration system includes incinerator body, and one be arranged in incinerator body fires room, fire grate, igniter, first row Grey mouth, dual firing chamber, the fixed link being fixedly mounted between a combustion room and dual firing chamber, the twin flue partition plate in fixed link, It stretches into and fires the indoor liquid unhurried current mechanism for being percolated input pipe, being arranged on twin flue partition plate upper surface, is arranged on dual firing chamber furnace wall On dual firing chamber's flue gas discharge opening, secondary combustion air inlets and second-time burning fuel jetting device；Described fixed link one end is with oozing Input pipe connection is filtered, the fixing pipe other end is connected by being percolated the percolate collection raw edge that fluid catheter and twin flue partition plate are equipped with, The liquid unhurried current mechanism is arranged below percolate collection raw edge, and liquid unhurried current mechanism includes being arranged on twin flue partition plate upper surface At least one convex stick or groove, convex stick or groove cause flow path of the percolate in twin flue partition plate upper surface to increase；
The air supply system includes gas gas-heat exchanger, and the gas gas-heat exchanger includes exchanger body, is arranged on friendship The intrinsic cold passage of parallel operation and the passage of heat, the passage of heat include the first air inlet and the 4th gas outlet；The cold passage bag The second air inlet, the first gas outlet, the second gas outlet and the 3rd gas outlet are included, the first gas outlet, the second gas outlet and the 3rd go out Gas port is connected with the second air inlet；And the 4th gas outlet, the first gas outlet, the second gas outlet and the 3rd gas outlet are pacified Equipped with air volume regulating valve door；First air inlet is connected with dual firing chamber flue gas discharge opening pipe, the 4th gas outlet and exhaust-gas treatment System entry connects；It is connected above second air inlet with extraneous fresh air, the oxygen-enriched combusting section of the first gas outlet and incinerator Connection, the second gas outlet are connected with the combustion with meagre oxygen section of incinerator, and the 3rd gas outlet is equipped with hot-wind inlet with drying garbage bucket Connection；
The black smoke processing system includes being arranged on the black smoke suction outlet on dual firing chamber top and interlayer casing, the interlayer casing bag Outer layer sleeve and the capillary being placed in outer layer sleeve are included, the outer layer sleeve includes straight connector, is arranged on straight connector one side Outer layer entrance and be arranged on straight connector end outer layer outlet, the capillary include capillary inlet and capillary outlet, Capillary outlet is parallel and is built in outer layer exit, capillary outlet and outer layer outlet composition nozzle, the outer layer entrance with Black smoke suction outlet connects, and capillary inlet and pressure-source communication, nozzle are connected with secondary combustion air inlets.
Further, the domestic garbage crusher include charging hopper, the screw extruding feed device include feed hopper, Extrusion spiral, helix tube, feeding discharge port and driving device；The dustbin is mounted on rubbish Self-loading-unloading device lower part, described The upper end of rubbish Self-loading-unloading device enters close to charging hopper entrance, the charging hopper outlet and the feed hopper of screw extruding feed device Mouth connection, the feeding discharge port are embedded in drum-type garbage drying device one end and are connected with rubbish feeding mouth before drying, institute Rubbish discharge port connects incinerator entrance after stating drying；Forward shovelling plate is installed in the drum-type garbage drying device, it is described Drying garbage cylinder is equipped with hot-wind inlet and foul smell floss hole, and the hot-wind inlet is connected with hot wind, foul smell floss hole and interlayer The entrance connection of the straight tube of casing is used as pressure source, and the 3rd wind turbine is equipped at the drying cylinder hot-wind inlet；The screw rod squeezes The helix tube lower end of pressing feeding device is equipped with aperture, and the helix tube lower end is equipped with aperture, is cased with arc groove outside the aperture, institute Arc groove lower end is stated equipped with rubbish extrusion dehydration leakage fluid dram.
Further, the liquid unhurried current mechanism is welded on twin flue partition plate upper surface by three convex sticks and forms head and the tail disconnection Oblique zigzag diversion trench.
Further, the burning processing system further includes afterheat utilizing system, and the afterheat utilizing system includes gas gas Heat exchanger and gas-liquid heat exchanger, the gas-liquid heat exchanger include the 3rd air inlet, the 4th air inlet, the 5th gas outlet and 6th gas outlet；4th gas outlet of the gas gas-heat exchanger is connected with the 3rd air inlet of gas-liquid heat exchanger, and described Four air inlets are connected with extraneous aquaporin, and the 5th gas outlet is water outlet, and the 5th external cooling tower in gas outlet, water is through supercooling After return the 4th air inlet, realize recycling for cooling water, the 6th gas outlet is connected with the first fans entrance.
Further, the exhaust treatment system includes dry method device and half-dried subtraction unit, pacifies on the left of the dry method device Equipped with the first wind turbine, the dry method device includes useless ashpit and screw rod into grey device, and the half-dried subtraction unit includes semidry method depickling Tower, first fan outlet are connected with semidry method extracting tower entrance, and the screw rod is mounted on the first wind turbine into the outlet of grey device It is connected on connecting pipe between semidry method extracting tower and with pipeline, the second ash discharge of connection is additionally provided between the pipeline Mouthful, the screw rod is sent by semidry method extracting tower into the ash that grey device drops out by the first wind turbine.
Further, exhaust treatment system further includes dust-extraction unit, and the dust-extraction unit includes cyclone dust collectors, pocket type removes Dirt device, the second wind turbine and chimney；The semidry method extracting tower outlet is connected with cyclone dust collectors entrance, and the cyclone dust collectors go out Mouth is connected with sack cleaner entrance, and the bag house outlet is connected with the second wind turbine air intake vent, and second wind turbine goes out Air port is connected with the entrance of chimney, and the outlet of the chimney is connected with outside air；The semidry method extracting tower, cyclone dust collectors And sack cleaner bottom is respectively provided with useless grey ash discharging hole, the ash discharging hole be designed with valve and ash discharging hole outlet all with useless ash Pond entrance connection, the second ash discharging hole outlet are in communication with the outside.
Further, two layers of elution layer is devised in the semidry method extracting tower, the first elution layer is equipped at least one Spray angle is 120 ° of nozzle, and the second elution layer is equipped with the nozzle that at least one spray angle is 90 °.
Further, the nozzle that the spray angle of the first elution layer installation is 120 ° is three, the second elution layer peace The spray angle of dress is that 90 ° of nozzle is one.
The present invention is of the invention with existing burning processing system for a kind of small continuous consumer waste incineration processing system It compares, has the following advantages：
1. existing equipment in the market has can be used in the formant equipment of the system, manufacture is at low cost, and installation operation is simple；
2. carrying out preliminary hydro-extraction by screw extruding feed device, reduce the load of drum-type garbage drying device, reduce Operation energy consumption；
3. carrying out processing landfill leachate using twin flue partition plate, not only handled percolate, and play protection partition plate and Adjust the effect for burning furnace temperature；
4. devising black smoke processing system and interlayer casing, additional power is not required, it is possible to black smoke be suctioned out, and be sent to two It disposes combustion room；
5. twin flue designs, the nitrogen oxides of generation can be allowed to cut down in the dual firing chamber of incinerator, reduce fume treatment cost；
6. useless ash is taken full advantage of, preliminary treatment has been carried out to flue gas, also improves calcium hydroxide medicine into ash system there is provided screw rod The service efficiency of agent reduces operating cost.
By optimizing waste incineration preprocessing system, incinerator internal structure and smoke processing system, rubbish has been considered Rubbish crushes the systematicness with dehydration, improves the air-tightness of incinerator, and rubbish is promoted fully to burn, and reduces secondary pollution and generates, Calcium hydroxide medicament is more made full use of, the pollutants such as sour gas, organic pollution and particulate matter is effectively removed, reaches rubbish It does not land, the purpose of foul smell indiffusion, the not outer row of waste liquid and waste heat do not waste.
The present invention will be further described below in conjunction with the accompanying drawings.
Description of the drawings
Fig. 1 is the structure diagram of the present invention；
Fig. 2 is the structure diagram of one embodiment of the invention；
Fig. 3 is the structure diagram of twin flue partition plate of the present invention；
Fig. 4 is the structure diagram of interlayer casing of the present invention.
Specific embodiment
Embodiment one：As shown in Figs 1-4, the present invention is a kind of small continuous consumer waste incineration processing system, including Burn preprocessing system, incineration system, air supply system, black smoke processing system and exhaust treatment system；The rubbish self-chambering Handler 2 hangs the automatic lifting feeding device of barrel type garbage truck using being similar to；Domestic garbage crusher 3 includes charging hopper 31, After drum-type garbage drying device 4 is including garbage inlet, foul smell floss hole 41, drying cylinder hot-wind inlet 42, drying before drying Rubbish discharge port 43 is equipped with forward shovelling plate in drum-type garbage drying device 4, material is made constantly to be copied in cylinder turning course It rises and spills down again, it is made fully to be contacted with thermal current, to improve drying efficiency and move forward material.Generally not directly using burning Flue gas after burning, because flue-gas temperature is excessively high to make some garbage decompositions, and flue gas does not pass through processing, containing toxic object Matter, hot wind source can be equipped with the 3rd by air with being generated after flue gas heat exchange after burning at drying cylinder hot-wind inlet 42 Wind turbine 421, the source of fresh air can be extracted by the 3rd wind turbine 421；The upper end of rubbish Self-loading-unloading device 2 and charging hopper 31 Closely, the outlet of charging hopper 31 connects entrance with 181 entrance of feed hopper of screw extruding feed device 18, feeding discharge port 182 are embedded in 4 one end of cartridge type drying garbage device and are connected with rubbish feeding mouth before drying, the spiral shell of screw extruding feed device 18 Coil lower end is equipped with aperture, and for removal waste fluid, shell is cased with outside the aperture, and for collecting waste liquid, the shell lower end is set There is rubbish extrusion dehydration leakage fluid dram 184.
Incinerator further includes hydraulic thrust door gear 17, hydraulic feed propulsion device 16, garbage feeding and stacks pond 15 and charging Closing door 24,24 upper end of charging closing door are equipped with sliding slot and sliding block, and hydraulic thrust door gear 17 and the contact point of sliding block are hinged on one It rises, hydraulic thrust door gear 17 is placed in 16 left side of hydraulic feed propulsion device, and hydraulic thrust door gear 17 includes the bar 25 that pushes, and push bar 25 perforation hydraulic feed propulsion devices 16 and garbage feeding stack pond 15, and the garbage feeding stacking use of pond 15 is corrosion resistant, there is one The material for determining intensity makes；Hydraulic feed propulsion device 16 be equipped with column type piston, hydraulic feed propulsion device 16 be placed in rubbish into Material stacks 15 left side of pond, and the entrance shape in garbage feeding stacking pond 15 is matched somebody with somebody with the discharge port 43 of rubbish preprocessing system merges company Logical, charging closing door 24 is made of high temperature resistant, corrosion resistant material, and charging closing door 24 leans to door for suspension type, and with burning The contact point for burning stove entrance is hingedly fixed in together, and garbage feeding stacks the outlet of pond 15 and connected with incinerator entrance and pass through charging Closing door 24 separates.Rubbish, into dumping pond 15, is then pushed into after pre-treatment by hydraulic feed propulsion device 16 Incinerator one fires the leading portion of room 51, in charging, by hydraulic thrust door gear 17 as hydraulic feed propulsion device 16 opens charging Closing door 24, because charging closing door 24 is heavier, if without hydraulic thrust door gear 17, rubbish can be pressed during charging Contracting, into after complete material, hydraulic thrust door gear 17 is shunk, and closes charging closing door 24, and then hydraulic feed propulsion device 16 is moved back again Original position is gone back to, so that incinerator keeps preferable sealing, garbage feeding stacks the entrance shape in pond 15 and rubbish preprocessing system Discharge port 43 with merge connect.Liquid unhurried current mechanism 21 is arranged on 20 lower section of percolate collection raw edge, and liquid unhurried current mechanism 21 is wrapped Include at least one convex stick or groove for being arranged on 23 upper surface of twin flue partition plate, convex stick or groove cause percolate twin flue every The flow path of 23 upper surface of plate increases, in favor of fully evaporating and destroying.Black smoke processing system include black smoke suction outlet 58 and Interlayer casing 59；Air supply system includes gas gas-heat exchanger 6 and associated conduit, and the gas gas-heat exchanger 6 includes first Air inlet 61, the second air inlet 62, the first gas outlet 63, the second gas outlet 64, the 3rd gas outlet 65 and the 4th gas outlet 66, institute The source of 62 fresh air of the second air inlet is stated to be extracted from the 3rd wind turbine 421.
Present invention additionally comprises afterheat utilizing system, including gas gas-heat exchanger 6 and gas-liquid heat exchanger 7；5th gas outlet 73 be water outlet, 73 external cooling tower of the 5th gas outlet, and water returns the 4th air inlet 72 after supercooling, realizes cooling water Recycle；Exhaust treatment system includes dry method device, half-dried subtraction unit and dust-extraction unit；The is equipped on the left of dry method device One wind turbine 13, dry method device include useless ashpit 14 and screw rod into grey device 141, and screw rod is interior equipped with dry lime powder into grey device 141, half-dried Subtraction unit includes semidry method extracting tower 8, and the of connection is additionally provided between the pipeline that the first wind turbine 13 is connected with semidry method extracting tower 8 Two ash discharging holes 26；The rotational speed regulation of screw rod can be utilized into the amount of ash, under normal circumstances, alkaline all also stronger, the hydrogen for the ash that gives up Calcium oxide has not been reacted with acidic materials completely, therefore can also be reused, extruding of the ash that gives up by screw rod into ash system After friction, the surface containing calcium hydroxide particle can be exposed, can be reacted with the sour gas in flue gas, in addition give up ash Surface area ratio is larger, has certain adsorption capacity, can adsorb and fall a certain amount of soot particulates, dioxins solid and heavy metal Deng.It with the useless ash of smoke mixture, can largely fall into the ash discharging hole of semidry method extracting tower air inlet front end, and then discharge cigarette Gas processing system, is transported away.Two layers of elution layer is devised in semidry method extracting tower 8, the first elution layer is equipped at least one Spray angle is 120 ° of nozzle 81, and the second elution layer is equipped with the nozzle 82 that at least one spray angle is 90 °；Dust-extraction unit Including cyclone dust collectors 9, sack cleaner 10, the second wind turbine 12 and chimney 11；Semidry method extracting tower 8 exports and cyclone dust collectors 9 entrances connect, and the outlet of cyclone dust collectors 9 is connected with 10 entrance of sack cleaner, the outlet of sack cleaner 10 and the second wind turbine 12 Air intake vent connects, and 12 air outlet of the second wind turbine is connected with the entrance of chimney 11, and the outlet of chimney 11 is connected with outside air；It is half-dried Method extracting tower 8, cyclone dust collectors 9 and 10 bottom of sack cleaner are respectively provided with useless grey ash discharging hole, and ash discharging hole is designed with valve and institute It states ash discharging hole outlet all to connect with useless 26 entrance of ashpit, the useless outlet of ashpit 26 is in communication with the outside；
As shown in Figs 1-4, including burning at preprocessing system, incineration system, air supply system, black smoke processing system and exhaust gas Reason system；The black smoke processing system includes being arranged on the black smoke suction outlet 58 on 52 top of dual firing chamber and interlayer casing 59, interlayer Casing 59 includes outer layer sleeve and the capillary being placed in outer layer sleeve, and the outer layer sleeve includes straight connector, is arranged on directly The outer layer entrance 591 of casing one side and the outer layer outlet for being arranged on straight connector end, capillary include capillary inlet 592 and hair Tubule exports, and capillary outlet is parallel and is built in outer layer exit, capillary outlet and outer layer outlet composition nozzle 593, outside Layer entrance 591 is connected with black smoke suction outlet 58, capillary inlet 592 and pressure-source communication, nozzle 593 and secondary combustion air inlets 56 connections.In order to handle a small amount of landfill leachate, leakage fluid dram 184 is connected with fixed link 19, and a pressure is equipped on connecting pipe Power water pump 27 conveys percolate using the fixed link of the inner hollow of twin flue partition plate, percolate is pumped into the upper surface of partition plate, By three, either four or five convex sticks are welded on 23 upper surface of twin flue partition plate and are formed from beginning to end for liquid unhurried current mechanism 21 The oblique zigzag diversion trench disconnected so that liquid flows from high to low, and moisture is then evaporated in incinerator, then is incinerated, Waste liquid is destroyed beneficial to fully quick.This design, can not only dispose landfill leachate, but also can make the temperature of partition plate will not be too Height in order to avoid partition plate is burnt and melted, and can control the temperature of incinerator.If the temperature of incinerator is excessively high, can be pumped into substantial amounts of Liquid is cooled down in time, in order to avoid burn out incinerator fire proofing tile；If temperature is too low, pumping liquid can be lacked or be not pumped into liquid Body allows incinerator to reduce the output of energy, fast lifting incineration temperature.
House refuse is fitted into after tentatively sorting in the dustbin 1, then lifts rubbish by rubbish Self-loading-unloading device 2 Rubbish bucket 1 simultaneously pour into the charging hopper 31 of refuse grinder 3 by discharging, is adjusted by adjusting 3 rotating speeds of the garbage crushing device The broken speed of rubbish, broken rubbish fall into feed hopper 181, and driving device 183 drives screw extruding feed device 18 right Rubbish carries out preliminary hydro-extraction, is then sent into drum-type garbage drying device 4 by feeding discharge port 182, dried rubbish from Discharge port 43 is discharged in incinerator body 5 and burns, and the amount of incinerator is entered by feed system control rubbish, and rubbish can be in a combustion Dryer section, incineration section and burning segment are passed sequentially through on the fire grate 511 of room, last lime-ash can be discharged from the first ash discharging hole 54, production Raw flue gas can pass through twin flue clamping plate 23 and enter dual firing chamber 52, carry out redox reaction, reduce the generation of pollutant, two combustions Room 52 ensure that flue gas keeps more than 2s under the conditions of 850 DEG C, a small amount of black smoke passes through interlayer by setting shortest device Casing 59 is sucked back into dual firing chamber 52 to burn again, and the flue gas of generation first passes through gas gas-heat exchanger 6, allows and feeds the new of incinerator Fresh air preheat, then again by gas-liquid heat exchanger 7, at this point, flue gas is made drastically to be cooled to the temperature of smoke processing system requirement Degree, makes full use of waste heat, subsequently into smoke processing system, contains a large amount of ashes, acid gas and other toxic gases Flue gas of refuse burning is pumped into semidry method extracting tower, 13 air outlet of the first wind turbine and semidry method depickling after cooling by the first wind turbine 13 The dry method device set between 8 air inlet of tower removes for semidry method extracting tower 8, cyclone dust collectors 9 and pocket type described in secondary use Dirt device 10 bottom discharge useless ash, and with the useless ash of smoke mixture, before largely falling into 8 air inlet of semidry method extracting tower In second ash discharging hole 26 at end, and then smoke processing system is discharged, be transported away, flue gas passes through contacts preliminary treatment with useless ash Afterwards, into semidry method extracting tower 8, flue gas is eluted by milk of lime, disposes sour gas, Bu Fen dioxin solids And cigarette ash, by treated the flue gas of semidry method extracting tower 8, the toxic gas of the overwhelming majority has been eliminated, it is only remaining More ash content, then passes sequentially through cyclone dust collectors 9 and sack cleaner 10, remove sour gas, organic pollution and Grain object, last flue gas is up to standard and passes through smoke stack emission.
Above-described embodiment is the preferable embodiment of the present invention, but embodiments of the present invention and from above-described embodiment Limitation, other any Spirit Essences without departing from the present invention with made under principle change, modification, replacement, combine, simplification, Equivalent substitute mode is should be, is included within protection scope of the present invention.

Claims (8)

1. a kind of small continuous consumer waste incineration processing system, it is characterised in that：Including
One burns preprocessing system, including dustbin（1）, rubbish Self-loading-unloading device（2）, domestic garbage crusher（3）, screw rod squeezes Pressing feeding device（18）And drum-type garbage drying device（4）；
Incineration system, air supply system, black smoke processing system and exhaust treatment system；
The incineration system includes incinerator body（5）, it is arranged on incinerator body（5）An interior combustion room（51）, fire grate （511）, igniter（53）, the first ash discharging hole（54）, dual firing chamber（52）, be fixedly mounted on a combustion room（51）And dual firing chamber（52）It Between fixed link（19）, mounted on fixed link（19）On twin flue partition plate（23）, stretch into combustion it is indoor diafiltration input pipe, set In twin flue partition plate（23）The liquid unhurried current mechanism of upper surface（21）, be arranged on dual firing chamber（52）Dual firing chamber flue gas row on furnace wall Outlet（55）, secondary combustion air inlets（56）With second-time burning fuel jetting device（57）；The fixed link（19）One end is with oozing Filter input pipe connection, fixing pipe（19）The other end is by being percolated fluid catheter（22）With twin flue partition plate（23）The percolate being equipped with Collect raw edge（20）Connection, the liquid unhurried current mechanism（21）It is arranged on percolate collection raw edge（20）Lower section, liquid unhurried current mechanism （21）Including being arranged on twin flue partition plate（23）At least one convex stick or groove of upper surface, convex stick or groove cause percolate to exist Twin flue partition plate（23）The flow path of upper surface increases；
The air supply system includes gas gas-heat exchanger（6）, the gas gas-heat exchanger（6）Including exchanger body, set It puts in the intrinsic cold passage of exchanger and the passage of heat, the passage of heat includes the first air inlet（61）And the 4th gas outlet （66）；The cold passage includes the second air inlet（62）, the first gas outlet（63）, the second gas outlet（64）And the 3rd gas outlet （65）, the first gas outlet（63）, the second gas outlet（64）And the 3rd gas outlet（65）With the second air inlet（62）Connection；And institute State the 4th gas outlet（66）, the first gas outlet（63）, the second gas outlet（64）And the 3rd gas outlet（65）It is mounted on tolerance tune Save valve；First air inlet（61）With dual firing chamber's flue gas discharge opening（55）Pipe connects, the 4th gas outlet（66）At exhaust gas Manage system entry connection；Second air inlet（62）Top is connected with extraneous fresh air, the first gas outlet（63）With incinerator Oxygen-enriched combusting section（512）Connection, the second gas outlet（64）With the combustion with meagre oxygen section of incinerator（513）Connection, the 3rd gas outlet （65）Hot-wind inlet is equipped with drying garbage bucket（42）Connection；
The black smoke processing system includes being arranged on dual firing chamber（52）The black smoke suction outlet on top（58）And interlayer casing（59）, institute State interlayer casing（59）Including outer layer sleeve and the capillary being placed in outer layer sleeve, the outer layer sleeve include straight connector, It is arranged on the outer layer entrance of straight connector one side（591）It is exported with the outer layer for being arranged on straight connector end, the capillary includes hair Tubule entrance（592）And capillary outlet, capillary outlet is parallel and is built in outer layer exit, and capillary outlet goes out with outer layer Mouth composition nozzle（593）, the outer layer entrance（591）With black smoke suction outlet（58）Connection, capillary inlet（592）With pressure source Connection, nozzle（593）With secondary combustion air inlets（56）Connection.
2. small continuous consumer waste incineration processing system according to claim 1, it is characterised in that：The life rubbish Rubbish crusher（3）Including charging hopper（31）, the screw extruding feed device（18）Including feed hopper（181）, extrusion spiral, spiral shell Coil, feeding discharge port（182）And driving device（183）；The dustbin（1）Mounted on rubbish Self-loading-unloading device（2）Under Portion, the rubbish Self-loading-unloading device（2）Upper end close to charging hopper（31）Entrance, the charging hopper（31）Outlet and screw extruding Feed device（18）Feed hopper（181）Entrance connects, the feeding discharge port（182）It is embedded in drum-type garbage drying device （4）One end simultaneously connects, rubbish discharge port after the drying with rubbish feeding mouth before drying（43）Connect incinerator entrance；The rolling Cartridge type drying garbage device（4）Forward shovelling plate is inside installed, the drying garbage cylinder is equipped with hot-wind inlet（42）It is arranged with foul smell Put mouth（41）, the hot-wind inlet（42）It is connected with hot wind, foul smell floss hole（41）With interlayer casing（59）Straight tube（591）'s Entrance connection is as pressure source, the drying cylinder hot-wind inlet（42）Place is equipped with the 3rd wind turbine（421）；The screw extruding is sent Expect device（18）Helix tube lower end be equipped with aperture, the helix tube lower end is equipped with aperture, is cased with arc groove outside the aperture （185）, the arc groove（185）Lower end is equipped with rubbish extrusion dehydration leakage fluid dram（184）.
3. small continuous consumer waste incineration processing system according to claim 1, it is characterised in that：The liquid delays Flow mechanism（21）Twin flue partition plate is welded on by three convex sticks（23）Upper surface forms the oblique zigzag diversion trench that head and the tail disconnect.
4. small continuous consumer waste incineration processing system according to claim 1, it is characterised in that：At the burning Reason system further includes afterheat utilizing system, and the afterheat utilizing system includes gas gas-heat exchanger（6）And gas-liquid heat exchanger （7）, the gas-liquid heat exchanger（7）Including the 3rd air inlet（71）, the 4th air inlet（72）, the 5th gas outlet（73）And the 6th Gas outlet（74）；The gas gas-heat exchanger（6）The 4th gas outlet（66）With gas-liquid heat exchanger（7）The 3rd air inlet （71）Connection, the 4th air inlet（72）It is connected with extraneous aquaporin and cooling tower passage, the 5th gas outlet（73）To go out The mouth of a river, the 5th gas outlet（73）External cooling tower, water return the 4th air inlet after supercooling（72）, realize cooling water It recycles, the 6th gas outlet（74）With the first wind turbine（13）Entrance connects.
5. small continuous consumer waste incineration processing system according to claim 1, it is characterised in that：At the exhaust gas Reason system includes dry method device and half-dried subtraction unit, and the first wind turbine is equipped on the left of the dry method device（13）, the dry method dress It puts including the ashpit that gives up（14）And screw rod is into grey device（141）, the half-dried subtraction unit include semidry method extracting tower（8）, described first Wind turbine（13）Air outlet and semidry method extracting tower（8）Entrance connects, and the screw rod is into grey device（141）Outlet is mounted on the first wind turbine （13）With semidry method extracting tower（8）Between connecting pipe on and connect with pipeline, the of connection is additionally provided between the pipeline Two ash discharging holes（26）, pass through the first wind turbine（13）By the screw rod into grey device（141）The ash dropped out is sent into semidry method extracting tower （8）.
6. small continuous consumer waste incineration processing system according to claim 1, it is characterised in that：Exhaust-gas treatment system System further includes dust-extraction unit, and the dust-extraction unit includes cyclone dust collectors（9）, sack cleaner（10）, the second wind turbine（12）With Chimney（11）；The semidry method extracting tower（8）Outlet and cyclone dust collectors（9）Entrance connects, the cyclone dust collectors（9）Outlet With sack cleaner（10）Entrance connects, the sack cleaner（10）Outlet and the second wind turbine（12）Air intake vent connects, described Second wind turbine（12）Air outlet and chimney（11）Entrance connection, the chimney（11）Outlet connected with outside air；It is described Semidry method extracting tower（8）, cyclone dust collectors（9）And sack cleaner（10）Bottom is respectively provided with useless grey ash discharging hole, the ash discharging hole Be designed with valve and the ash discharging hole outlet all with useless ashpit（14）Entrance connects, second ash discharging hole（26）Outlet and the external world Connection.
7. small continuous consumer waste incineration processing system according to claim 5 or 6, it is characterised in that：Described half Dry-process deacidification tower（8）Two layers of elution layer is inside devised, the first elution layer is equipped with the nozzle that at least one spray angle is 120 ° （81）, second, which elutes layer, is equipped with the nozzle that at least one spray angle is 90 °（82）.
8. small continuous consumer waste incineration processing system according to claim 7, it is characterised in that：First leaching The spray angle for washing layer installation is 120 ° of nozzle（81）For three, the nozzle that the spray angle that the second elution layer is installed is 90 ° （82）For one.
CN201810056142.8A 2018-01-20 2018-01-20 Small-size continuous type domestic waste incineration disposal system Active CN108105777B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201810056142.8A CN108105777B (en) 2018-01-20 2018-01-20 Small-size continuous type domestic waste incineration disposal system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201810056142.8A CN108105777B (en) 2018-01-20 2018-01-20 Small-size continuous type domestic waste incineration disposal system

Publications (2)

Publication Number Publication Date
CN108105777A true CN108105777A (en) 2018-06-01
CN108105777B CN108105777B (en) 2022-03-11

Family

ID=62220171

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201810056142.8A Active CN108105777B (en) 2018-01-20 2018-01-20 Small-size continuous type domestic waste incineration disposal system

Country Status (1)

Country Link
CN (1) CN108105777B (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110236440A (en) * 2019-07-08 2019-09-17 北京金茂绿建科技有限公司 Burning closestool
CN110715305A (en) * 2019-11-08 2020-01-21 义乌甘棠锅炉有限公司 Incinerator capable of achieving green emission and waste heat utilization
CN116498973A (en) * 2023-07-03 2023-07-28 浙江百能科技有限公司 PTA byproduct solid and liquid waste mixed incineration treatment system

Citations (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS52101873A (en) * 1976-06-16 1977-08-26 Mitsui Toatsu Chem Inc Apparatus for incinerating and treating cyanide-contained waste liquid
CN2711550Y (en) * 2004-06-14 2005-07-20 薛冰 Solid-liquid incineration furnace
CN1644986A (en) * 2005-01-13 2005-07-27 上海交通大学 Dehydrating combustion treating method for living refuse
CN201582825U (en) * 2009-09-25 2010-09-15 福建省丰泉环保控股有限公司 High-temperature flue gas afterheat utilization device
CN202283452U (en) * 2011-10-31 2012-06-27 江苏一同环保工程技术有限公司 Novel circulating fluid-bed semi-dry desulfurization device
CN105546547A (en) * 2016-01-27 2016-05-04 北京神雾环境能源科技集团股份有限公司 Twin-water-seal garbage pyrolysis circular furnace and method for treating percolate with same
CN105757673A (en) * 2016-03-30 2016-07-13 四川天壹环保科技有限公司 Small-scale efficient domestic garbage gasification incineration system and incineration method
KR101748390B1 (en) * 2017-04-26 2017-06-16 주식회사 그린이앤지 Incinerator for incinerating fishing net
JP3211196U (en) * 2012-04-18 2017-06-29 啓吾 清水 Sewage sludge and organic matter drying and incineration equipment
CN206846731U (en) * 2017-05-08 2018-01-05 广西华都环境投资有限公司 A kind of domestic waste incineration
CN208687734U (en) * 2018-01-20 2019-04-02 广州利世环境治理有限公司 A kind of small continuous consumer waste incineration processing system

Patent Citations (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS52101873A (en) * 1976-06-16 1977-08-26 Mitsui Toatsu Chem Inc Apparatus for incinerating and treating cyanide-contained waste liquid
CN2711550Y (en) * 2004-06-14 2005-07-20 薛冰 Solid-liquid incineration furnace
CN1644986A (en) * 2005-01-13 2005-07-27 上海交通大学 Dehydrating combustion treating method for living refuse
CN201582825U (en) * 2009-09-25 2010-09-15 福建省丰泉环保控股有限公司 High-temperature flue gas afterheat utilization device
CN202283452U (en) * 2011-10-31 2012-06-27 江苏一同环保工程技术有限公司 Novel circulating fluid-bed semi-dry desulfurization device
JP3211196U (en) * 2012-04-18 2017-06-29 啓吾 清水 Sewage sludge and organic matter drying and incineration equipment
CN105546547A (en) * 2016-01-27 2016-05-04 北京神雾环境能源科技集团股份有限公司 Twin-water-seal garbage pyrolysis circular furnace and method for treating percolate with same
CN105757673A (en) * 2016-03-30 2016-07-13 四川天壹环保科技有限公司 Small-scale efficient domestic garbage gasification incineration system and incineration method
KR101748390B1 (en) * 2017-04-26 2017-06-16 주식회사 그린이앤지 Incinerator for incinerating fishing net
CN206846731U (en) * 2017-05-08 2018-01-05 广西华都环境投资有限公司 A kind of domestic waste incineration
CN208687734U (en) * 2018-01-20 2019-04-02 广州利世环境治理有限公司 A kind of small continuous consumer waste incineration processing system

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110236440A (en) * 2019-07-08 2019-09-17 北京金茂绿建科技有限公司 Burning closestool
CN110236440B (en) * 2019-07-08 2021-10-08 北京金茂绿建科技有限公司 Incineration type closestool
CN110715305A (en) * 2019-11-08 2020-01-21 义乌甘棠锅炉有限公司 Incinerator capable of achieving green emission and waste heat utilization
CN116498973A (en) * 2023-07-03 2023-07-28 浙江百能科技有限公司 PTA byproduct solid and liquid waste mixed incineration treatment system
CN116498973B (en) * 2023-07-03 2023-09-22 浙江百能科技有限公司 PTA byproduct solid and liquid waste mixed incineration treatment system

Also Published As

Publication number Publication date
CN108105777B (en) 2022-03-11

Similar Documents

Publication Publication Date Title
CN101570388B (en) Harmless recycling treatment process for urban sludge
CN207081009U (en) A kind of residents in rural community pyrolysis gasification system
CN1850370A (en) Life-garbage comprehensive treatment technology
CN108240627A (en) A kind of chamber structure of solid waste incinerator
CN107525082A (en) A kind of garbage disposal combustion furnace and refuse disposal system
CN2809450Y (en) Continuous and controllable pyrogenation integrated refuse incinerator
CN108105777A (en) A kind of small continuous consumer waste incineration processing system
CN103695012A (en) Harmless pure gas extraction method and double-furnace folding garbage combustion furnace used in same
CN100432532C (en) Combined incineration treatment method for refuse and special vertical oxygen-enriched continuous incinerator
CN106224974A (en) Waste incineration processing system
CN208042154U (en) A kind of device of processing incineration flue gas of household garbage
CN207514917U (en) Waste incineration and generating electricity device
CN208687734U (en) A kind of small continuous consumer waste incineration processing system
CN208442834U (en) Reciprocating fire grate furnace for domestic garbage burning electricity generation
CN108613194B (en) A kind of device for villages and small towns consumer waste incineration
CN109357263A (en) A kind of refuse incinerator
CN208332274U (en) A kind of compact twin chamber twin flue waste incinerator
CN205383607U (en) Rubbish is ashless to burn burning furnace
CN208332269U (en) A kind of small continuous consumer waste incineration pretreating device
CN1460166A (en) Regenerative thermal waste incineration system
CN108006658A (en) A kind of compact twin chamber twin flue waste incinerator
CN203586223U (en) Double-furnace-stacked garbage combustion furnace for extracting pure coal gas harmlessly
CN101140069B (en) Environment protection garbage incineration device
CN208687737U (en) A kind of consumer waste incineration system of prevention and control flue gas pollutant
CN108036327A (en) A kind of efficient consumer waste incineration processing system of miniature energy-saving

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
TA01 Transfer of patent application right
TA01 Transfer of patent application right

Effective date of registration: 20210422

Address after: 100040 room 609, great wall building, block a, 22 Shijingshan Road, Shijingshan District, Beijing

Applicant after: BEIJING ZHONGLI XINDA ENVIRONMENTAL PROTECTION ENGINEERING Co.,Ltd.

Address before: 510032 A3146, west side of Zhong Cun New Town Road, 105 National Road, Zhong Cun street, Panyu District, Guangzhou, Guangdong.

Applicant before: GUANGZHOU BE WORLD ENVIRONMENTAL GOVERNANCE Co.,Ltd.

CB02 Change of applicant information
CB02 Change of applicant information

Address after: 100040 room 609, great wall building, block a, 22 Shijingshan Road, Shijingshan District, Beijing

Applicant after: Beijing zhonglixinda Environmental Technology Co.,Ltd.

Address before: 100040 room 609, great wall building, block a, 22 Shijingshan Road, Shijingshan District, Beijing

Applicant before: BEIJING ZHONGLI XINDA ENVIRONMENTAL PROTECTION ENGINEERING CO.,LTD.

GR01 Patent grant
GR01 Patent grant