CN1712777A - Refuse combustion and step-by-step combustion system of furnace vehicle - Google Patents
Refuse combustion and step-by-step combustion system of furnace vehicle Download PDFInfo
- Publication number
- CN1712777A CN1712777A CN 200410049958 CN200410049958A CN1712777A CN 1712777 A CN1712777 A CN 1712777A CN 200410049958 CN200410049958 CN 200410049958 CN 200410049958 A CN200410049958 A CN 200410049958A CN 1712777 A CN1712777 A CN 1712777A
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- Prior art keywords
- haydite
- track
- box
- car
- rubbish
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Links
- 238000002485 combustion reaction Methods 0.000 title description 7
- 239000010813 municipal solid waste Substances 0.000 claims abstract description 99
- 238000000034 method Methods 0.000 claims abstract description 26
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 16
- 238000007599 discharging Methods 0.000 claims abstract description 12
- 239000002893 slag Substances 0.000 claims description 67
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 23
- 239000000428 dust Substances 0.000 claims description 23
- 239000003546 flue gas Substances 0.000 claims description 23
- 238000012545 processing Methods 0.000 claims description 16
- 238000001179 sorption measurement Methods 0.000 claims description 15
- 238000012216 screening Methods 0.000 claims description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 13
- 239000000463 material Substances 0.000 claims description 12
- 239000010802 sludge Substances 0.000 claims description 12
- 239000002918 waste heat Substances 0.000 claims description 11
- 239000002994 raw material Substances 0.000 claims description 8
- 239000000779 smoke Substances 0.000 claims description 8
- 239000008187 granular material Substances 0.000 claims description 7
- 239000002245 particle Substances 0.000 claims description 7
- 239000010865 sewage Substances 0.000 claims description 6
- 238000004804 winding Methods 0.000 claims description 5
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 4
- 229910052799 carbon Inorganic materials 0.000 claims description 4
- 229910052760 oxygen Inorganic materials 0.000 claims description 4
- 239000001301 oxygen Substances 0.000 claims description 4
- 238000004056 waste incineration Methods 0.000 claims description 4
- 238000005056 compaction Methods 0.000 claims description 3
- 238000011144 upstream manufacturing Methods 0.000 claims description 3
- 239000004744 fabric Substances 0.000 claims description 2
- 229910052751 metal Inorganic materials 0.000 claims description 2
- 239000002184 metal Substances 0.000 claims description 2
- 238000007885 magnetic separation Methods 0.000 claims 2
- 238000001816 cooling Methods 0.000 claims 1
- 238000009826 distribution Methods 0.000 abstract description 3
- 239000003818 cinder Substances 0.000 abstract 1
- 239000003517 fume Substances 0.000 abstract 1
- 239000002956 ash Substances 0.000 description 39
- 239000011521 glass Substances 0.000 description 9
- 238000007789 sealing Methods 0.000 description 8
- 238000010586 diagram Methods 0.000 description 6
- 230000000694 effects Effects 0.000 description 5
- 239000000126 substance Substances 0.000 description 5
- 230000008901 benefit Effects 0.000 description 4
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical class C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 4
- 238000005245 sintering Methods 0.000 description 4
- HGUFODBRKLSHSI-UHFFFAOYSA-N 2,3,7,8-tetrachloro-dibenzo-p-dioxin Chemical compound O1C2=CC(Cl)=C(Cl)C=C2OC2=C1C=C(Cl)C(Cl)=C2 HGUFODBRKLSHSI-UHFFFAOYSA-N 0.000 description 3
- 229920000049 Carbon (fiber) Polymers 0.000 description 3
- 239000004917 carbon fiber Substances 0.000 description 3
- 238000009264 composting Methods 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000005453 pelletization Methods 0.000 description 3
- 238000002360 preparation method Methods 0.000 description 3
- 238000003825 pressing Methods 0.000 description 3
- 241000195493 Cryptophyta Species 0.000 description 2
- 239000006096 absorbing agent Substances 0.000 description 2
- 239000002817 coal dust Substances 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 230000008878 coupling Effects 0.000 description 2
- 238000010168 coupling process Methods 0.000 description 2
- 238000005859 coupling reaction Methods 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 229910001385 heavy metal Inorganic materials 0.000 description 2
- 239000006148 magnetic separator Substances 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 239000002689 soil Substances 0.000 description 2
- 235000002918 Fraxinus excelsior Nutrition 0.000 description 1
- 238000005266 casting Methods 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000008030 elimination Effects 0.000 description 1
- 238000003379 elimination reaction Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000035558 fertility Effects 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- -1 haydite Substances 0.000 description 1
- 239000011499 joint compound Substances 0.000 description 1
- 238000007500 overflow downdraw method Methods 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Images
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J1/00—Removing ash, clinker, or slag from combustion chambers
- F23J1/02—Apparatus for removing ash, clinker, or slag from ash-pits, e.g. by employing trucks or conveyors, by employing suction devices
-
- 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
- F23G5/006—General arrangement of incineration plant, e.g. flow sheets
-
- 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
- F23G5/40—Portable or mobile incinerators
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J15/00—Arrangements of devices for treating smoke or fumes
- F23J15/02—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material
- F23J15/022—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material for removing solid particulate material from the gasflow
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2205/00—Waste feed arrangements
- F23G2205/14—Waste feed arrangements using hopper or bin
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J2219/00—Treatment devices
- F23J2219/30—Sorption devices using carbon, e.g. coke
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J2900/00—Special arrangements for conducting or purifying combustion fumes; Treatment of fumes or ashes
- F23J2900/01005—Mixing water to ash
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Processing Of Solid Wastes (AREA)
- Gasification And Melting Of Waste (AREA)
Abstract
A garbage incinerating method and its step incinerator system are disclosed. Said system is composed of a step incinerator with a track, multiple cars on said track, the ferrying flat car and hydraulic propulsion at one end of said track, the cinder discharging car and collector at another end of said track, such units on the upper layer of supporting frame as haydite distributor, garbage distributor, preheater and ignitor, an underground garbage cabin linked with distribution station via garbage conveyer, an ash conveyer linked with ash discharging station for conveying the ash to sphericizing shop, a conveyer for conveying haydites from shop to distribution station, and a fume treating line consisting of afterheat boiler, duster, air heat exchanger, blower and activated carbon adsorber.
Description
Technical field
The present invention relates to a kind of garbage incineration method and reach walking-beam furnace car CIU, these method and system to refuse thermal value require lower (〉=200 kilocalories/kg), be specially adapted to composting, these method and system can be carried out harmless treatment to rubbish, treating capacity is big, can reach 1000-5000 ton/sky.
Background technology
Development and the increase of urban population and the raising of people's level of consumption along with modernization of industry production; treatment of urban garbage becomes the major subjects of urban construction and environmental protection; the rubbish of China 95% is the composting without letter sorting at present; traditional air storage rubbish, bury or on-site incineration rubbish can not satisfy at present to requirement on environmental protection; so both cause new refuse pollution easily, needed lot of manpower and material resources and high freight again.For this reason, people explore the various forms of garbage combustion devices of exploitation constantly.Chinese patent 02229115.6 discloses a kind of horizontal continuous disposal of refuse incinerator, comprises by body of heater, track, flat car, motor, material-conveying belt etc. and forming.Characteristics are that the body of heater end face has rubbish to throw in the hole, flat car and walking guide rail are arranged, the guide rail that the body of heater periphery has one-tenth " # " font of reciprocal walking to lay in the body of heater, garbage truck can go round and begin again to move and burn away the refuse, and a day disposal of refuse amount can reach 300 tons, and advantage is reasonable in design, simple in structure, easy to manufacture, easy to install, cost is low, the disposal of refuse amount is big, pollute and lack, be easy to apply, easy to operate.Be suitable for medium and the use of cities and towns, low middling city.But this patent volume is bigger, burns fully inadequately, and the thermal efficiency is lower, easily atmosphere is caused new pollution.Therefore, need to propose a kind of garbage incineration method and walking-beam furnace car refuse burning system.
Summary of the invention
The object of the present invention is to provide a kind of garbage incineration method and reach walking-beam furnace car CIU, these method and system to refuse thermal value require lower (〉=200 kilocalories/kg), be specially adapted to composting, these method and system can be carried out harmless treatment to rubbish, and treating capacity can reach 1000-5000 ton/sky.
The objective of the invention is to be realized by following technical proposals: a kind of garbage incineration method is characterized in that:
Use the step-by-step movement incinerator, this incinerator has a furnace body support, one bar oven Car Track is arranged on it, a plurality of box-type furnace cars are set on this track, the bottom half of this box-type furnace car is provided with fire grate, one end of described track is provided with ferry-boat flatcar and hydraulic feed device, and the other end of described track is provided with slag row and unloads and the slag collection device; Described furnace body support upper strata is equipped with haydite distributing device, rubbish distributing device, preheating device, igniter successively; The negative pressure header is equipped with in described furnace body support middle level, and this negative pressure header top is communicated with described box-type furnace car bottom, and this negative pressure header bottom is communicated with many negative pressure airduct tops that are set up in parallel, and described negative pressure airduct middle part is communicated with a thermal-arrest header;
When the box-type furnace car arrives the haydite distributing device, by the haydite distributing device haydite ball blank is laid in the box-type furnace car and forms initial bed, by the rubbish distributing device rubbish is laid on the described initial bed then;
When the box-type furnace car arrives the preheating device position, use preheating device the rubbish in the box-type furnace car to be carried out preheating, preheat temperature 200-300 ℃;
When the box-type furnace car arrives igniter, by igniter rubbish to be lighted, the incineration temperature of control rubbish reaches 1100～1200 ℃; And starting exhausting system in box-type furnace car bottom generation negative pressure, guiding rubbish burns to the bottom from the top, sinters haydite ball blank into haydite; In the waste incineration process, use heater that the rubbish in the box-type furnace car is heated oxygen supply.
When the box-type furnace car arrived slag row and unloads, the overturning discharging was discharged to the grog that burns and carries out break process in the disintegrating machine, and the particle diameter that makes slag granules is less than 30 millimeters;
Grog after break process is collected screening plant by conveying device and is sieved processing, and complete haydite is collected the haydite storehouse, and ash is collected ash bin, and the slag granules material is collected the slag storehouse;
By transmitting device ash is transported to a system ball workshop, generates haydite ball blank, it is standby to be transferred to the haydite distributing device then;
To burn the flue gas and the dust that produce by smoke discharging pipe and collect and send into the flue gas processing pipeline;
In the flue gas processing pipeline, carry out purified treatment by multi-tube dust cleaner, sack cleaner;
The ash of described deduster being collected by transmitting device is transported to a system ball workshop, generates haydite ball blank, and it is standby to be transferred to the haydite distributing device then.
A kind of walking-beam furnace car refuse burning system, it is characterized in that: a step-by-step movement incinerator is arranged in described system, this incinerator has a furnace body support, one bar oven Car Track is arranged on it, a plurality of box-type furnace cars are set on this track, the bottom half of this box-type furnace car is provided with fire grate, and an end of described track is provided with ferry-boat flatcar and hydraulic feed device, and the other end of described track is provided with slag row and unloads and the slag collection device; Described furnace body support upper strata is equipped with haydite distributing device, rubbish distributing device, preheating device, igniter successively; The negative pressure header is equipped with in described furnace body support middle level, and this negative pressure header top is communicated with described box-type furnace car bottom, and this negative pressure header bottom is communicated with many negative pressure airduct tops that are set up in parallel, and described negative pressure airduct middle part is communicated with a thermal-arrest header; Described slag collection device bottom is provided with breaker, two-stage screening plant, concentration equipment; A rubbish dicang is arranged, be connected with described rubbish distributing device, provide rubbish to incinerator continuously by the rubbish pipeline; There is an ash pipeline to be connected with described screening plant, ash is transported to a system ball workshop, in system ball workshop is that primary raw material is made haydite ball base with the ash, by a pipeline described haydite ball base is sent into described haydite distributing device again, is entered in the incinerator by the haydite distributing device; A flue gas processing pipeline is arranged, be provided with waste heat boiler, air heat exchanger, deduster, blower fan and activated carbon adsorption unit in this pipeline; Have an ash pipeline to be connected with deduster behind the described slag collection device, the ash that this deduster is collected is transported to system ball workshop.
Compared with the prior art the present invention has following advantage:,
1, the present invention is lower to the refuse thermal value requirement, and the rubbish of 〉=200 kilocalories/kg all can burn.
2, the present invention is simple in structure, small investment, and the burning condition is good, and treating capacity can reach 1000-5000 ton/sky, and operating cost is low.
3, but the present invention adopts two-stage igniter and drier energy savings, waste heat boiler is set waste heat recovery can be used for generating or central heating, has tangible smoke elimination to subtract the effect of dirt simultaneously, and its social benefit is huge.
4, the present invention adopts the activated carbon fiber adsorption box exhaust can be purified fully.
5, the present invention adopts haydite ball base to make bed material, need not add the sintering that fuel just can be finished haydite, because the haydite of sintering is the high-quality water-keeping material of soilless culture and arid area, market prospects are wide, therefore, can realize the commercialization of rubbish ashes.
6, the present invention can innoxious use municipal sludge and garbage leachate.
Description of drawings
The invention will be further described below in conjunction with drawings and Examples.
Fig. 1, the used incinerator structural representation of the present invention
Two schematic diagrames of the incinerator embodiment that Fig. 2, the present invention are used
Fig. 3, the used incinerator vertical view (vertical view of Fig. 1) of the present invention
Fig. 4, the used slag of the present invention are arranged the structure chart (the A portion enlarged drawing of Fig. 1) of unloading
Fig. 5, the used slag of the present invention are arranged the side view (left side view of Fig. 4) of unloading
Fig. 6, the used negative pressure header structure chart (the B-B cutaway view of Fig. 1) of the present invention
Fig. 7, used preheating device and the stove bassinet structure figure (the F portion enlarged drawing of Fig. 6) of the present invention
Fig. 8, the used distributing device structural representation (the C portion enlarged drawing of Fig. 2) of the present invention
Fig. 9, the used water seal conduit schematic diagram (H of Fig. 6 is to view) of the present invention
Figure 10, the used mud slide fastener schematic diagram (vertical view of Fig. 9) of the present invention
Figure 11, the used traction track schematic diagram (the D-D cutaway view of Fig. 3) of the present invention
Figure 12, the used adsorption box structural representation of the present invention
Figure 13, the used adsorption box filter core distribution schematic diagram (cutaway view of Figure 12 G-G) of the present invention
Figure 14, the used filter cartridge construction schematic diagram (Figure 12 partial enlarged drawing) of the present invention
Figure 15, refuse burning system figure of the present invention
The specific embodiment
Embodiment one:
At first the employed step-by-step movement incinerator of present embodiment being done one describes in detail, this incinerator has a furnace body support 15, this support is a metal framework, its length is 50 meters-200 meters, one bar oven Car Track 6 is housed on this furnace body support, a plurality of box-type furnace cars 7 are set on this track, and the bottom half of this box-type furnace car is provided with fire grate, and the casing both sides are provided with wheel; One end of described furnace body support is provided with ferry-boat flatcar 16 and hydraulic feed device 17, and the other end of described track is provided with slag row and unloads 5 and slag collection device 4.Described slag collection device top is provided with the tail dust excluding hood, and the middle part is provided with the slag collection bucket, and the bottom is provided with breaker.Described furnace body support upper strata is equipped with rubbish distributing device 13, preheating device 11, igniter 10 successively.Be provided with an igniter in this igniter, this igniter is arranged on described box-type furnace car top, and this igniter is conventional gas igniter.Igniter is provided with principal point firearm and auxiliary igniter.Negative pressure header 8 is equipped with in described furnace body support middle level, this negative pressure header top is communicated with described box-type furnace car bottom, this negative pressure header bottom is communicated with many negative pressure airduct 81 tops that are set up in parallel, this negative pressure BOD is communicated with the water seal conduit 20 that is positioned at described furnace body support one side, and described negative pressure airduct middle part is communicated with a thermal-arrest header 21; Described ferry-boat flatcar be arranged on one with the vertically disposed up ferry-boat track 603 of stove Car Track on, described slag row unload be arranged on one with the vertically disposed descending ferry-boat track 601 of stove Car Track on, between described up ferry-boat track and the descending ferry-boat track traction track parallel with the stove Car Track 602 is set, is provided with a tractor 61 below this traction track.
Referring to Fig. 1, Fig. 7, in the present embodiment, described box-type furnace car has the casting car body 701 of a grooved, and the car body bottom is provided with fire grate 702, and wheel 703 is equipped with in the car body both sides.This car body rear and front end is Qian shape port, when end to end the connecting together of a plurality of stove cars, can form an elongated conduit.In order to realize the slipper seal of bottom of furnace body and negative pressure header, keep the negative pressure state in the negative pressure header, described stove car bottom is provided with sliding sealing device, and described negative pressure header top combines with this sliding sealing device sealing.This sliding sealing device is made of with the quiet plate 705 of sealing that is installed in negative pressure header top the moving plate 704 of the sealing of stove car bottom.Sealing is moved plate and is sealed the less dynamic seal (packing) gap of maintenance between the quiet plate.
Referring to Fig. 3, Fig. 4, Fig. 5, Figure 11, in the present embodiment, a plurality of box-type furnace cars are end to end on stove Car Track 6, advance the mode of the stepper drive of front truck to move by the back car.In order to drive box-type furnace car step run, the right-hand member of described stove Car Track is provided with a hydraulic feed device 17, and this hydraulic feed device is made of Hydraulic Station 171, propelling oil cylinder 172, propelling coaster 173.This propelling coaster is a weight vehicle, can advance coaster can absorb consequent axial impact in each startup of box-type furnace car and dwelling period in the shock-free box-type furnace car that passes to of the thrust of hydraulic jack.Unload slag in order to drive box-type furnace car row, the left end of described stove Car Track is provided with a slag row and unloads 5, this slag row unloads and is provided with a winch support 511, a winding plant 53, a pair of quiet pulley 52, hinge is adorned a rotary parking platform 54 on the described winch support, this parking platform is provided with the parking orbital segment 55 that can dock with described stove Car Track level, and this rotary parking platform one end is by hinge 56 and winch support hinge dress, and the other end is connected with the carrying cable 58 of winding plant.Winch bracket is installed on the ride 51, and ride has and drives wheel 57.Drive motors 512 is housed on the ride, and this motor is connected with driving wheel power.When the box-type furnace car enters on the rotary parking platform, winding plant starts, and carrying cable traction rotary parking platform is that the center of circle rotates counterclockwise with the hinge, makes the box-type furnace car realize 40 °-60 ° inclination, relies on the gravity effect to finish slag row and unloads.The rotary parking platform resets to level then.Drive motors starts, and drives slag row and unloads and move along descending ferry-boat track 601, arrives traction track 602 positions and stops, and the tractor 61 below this traction track enters box-type furnace car lower position.Described tractor can move on the bottom track 614 of oneself, and this bottom track is parallel with described traction track, and described bottom track can be two rail, also can be to mix the earth road surface.The tractor front portion is provided with traction hook 611 (this hook is provided with conventional automatic coupling and uncoupling rigging), the rear portion is provided with and advances hook 612 (this hook is provided with conventional automatic coupling and uncoupling rigging), the bottom is provided with wheel 613, this tractor drives by a wirerope draw-gear 605, and this wirerope opposite is provided with fixedly transfer roller 606.When wirerope draw-gear forward rotation, tractor travels left, after the traction hook of tractor front portion and the hook groove on the box-type furnace car articulate, wirerope draw-gear backward rotation, traction box-type furnace car disengaging slag row unloads and enters on the traction track, and along this track to right travel, when near up ferry-boat track 603 positions, stop, wirerope draw-gear forward rotation, the traction hook breaks off relations with the box-type furnace car, the propelling hook and the box-type furnace car at tractor rear portion articulate, and the wirerope draw-gear is backward rotation once more, the box-type furnace car are shifted onto on the parking orbital segment of ferry-boat flatcar.This ferry-boat flatcar is made of wheel 161, car body platform 162, parking orbital segment 163, drive unit 164.The ferry-boat flatcar starts, and this stove car is transported to the right-hand member original position of described stove Car Track along up ferry-boat track.
Referring to Fig. 2 and Fig. 8 (this figure shows the distributing device broken section), in the present embodiment, be provided with a haydite distributing device 14 before the described rubbish distributing device, be provided with a bitubular eccentric swage 12 between described rubbish distributing device and the preheating device.The haydite distributing device adopts conventional structure, is made of hopper 143, material roller 141, bottom scraper plate 142, and the structure of rubbish distributing device and haydite distributing device are basic identical.Haydite distributing device and rubbish distributing device are set in sequence in box-type furnace garage and walk the track top, be fixed on the furnace body support, it highly can be adjusted, when the box-type furnace car enters into its lower position, earlier in the stove car, lay haydite ball base by the haydite distributing device, it is laid on the fire grate as initial bed 140, and then on initial bed, covers waste layer 130 by the rubbish distributing device.Described haydite ball base is that raw material is made by the ash and the glass dust of the output of burning away the refuse, with rubbish is that fuel sinters it into haydite, harmful substances such as the dioxin in the garbage ash and city, heavy metal will combine under molten condition with glass dust and become the glass ore deposit mutually, and this haydite is to be difficult for degraded and undissolved material.Thus, improved the degree of purification of rubbish.
Bitubular eccentric swage is provided with front and back stages, each level is respectively established a pressing roller holder 121, this pressing roller holder is provided with 1-3 material pressing drum 122, this eccentric swage is arranged on described box-type furnace car top, be fixed on the furnace body support, it highly can be adjusted, and when the box-type furnace car that has rubbish entered into this eccentric swage position, this eccentric swage was with garbage truck.The compaction rate of rubbish can improve efficiency of combustion and temperature after improving, and promotes rubbish completing combustion.
Referring to Fig. 7 (in order to save view, the cross section of preheating device is presented on Fig. 7), in order to improve ignition temperature and efficiency of combustion, present embodiment was provided with a preheating device 11 before igniter, this preheating device cover is contained on the described box-type furnace car, be fixed on the furnace body support, this preheating device is provided with a preheating cover body 111, this preheating cover body is arranged on box-type furnace garage and walks the track top, shunting grid 112 is housed in the cover body, the cover body top is provided with hot air inlet 113, and cover body length is 10 meters-20 meters, and the hot-air that garbage pre-heating is used is provided by the air heat exchanger that is installed on the smoke discharging pipe.When the box-type furnace car that has rubbish entered into its lower position, the hot-air of shunting grid ejection improved its temperature and aridity, for burning is prepared to its preheating.
Referring to Fig. 2, in order to improve ignition temperature and efficiency of combustion, in the present embodiment, described igniter back is provided with a heater 9, this heater cover is contained on the described box-type furnace car, is fixed on the furnace body support, and its concrete structure and preheating device are identical, be not described in detail at this, heater length is 30 meters-100 meters.When the box-type furnace car that has rubbish entered into its lower position, the hot-air of shunting grid ejection heated it, improves ignition temperature and aftercombustion oxygen.
Referring to Fig. 1, Fig. 3, Fig. 6, in the present embodiment, in order to improve the clean-up effect of waste incineration effect and flue gas, negative pressure header 8 is equipped with in described furnace body support middle level, this negative pressure header top and stove car bottom is communicated with, produces negative pressure in box-type furnace car bottom, guide rubbish from the top to base burning.This header is long vacuum cavity, and its length is 80 meters-150 meters.This negative pressure header bottom is set up in parallel with many and is negative pressure airduct 81 tops that tilt to install and is communicated with, and the negative pressure airduct is provided with valve 82, can close this valve at any time, to a negative pressure airduct maintenance.The negative pressure BOD is communicated with the water seal conduit 20 that is positioned at described furnace body support one side.The negative pressure airduct tilts to install, and the particle that carries in the flue gas of refuse burning can be separated from flue gas, and be fallen in the water seal conduit at inertia force and gravity effect.Described negative pressure airduct middle part is communicated with a thermal-arrest header 21, at connecting portion dedusting grid 212 can be set, and this dedusting grid further separates the particle in the incineration flue gas, and isolated particle can drop in the water seal conduit along the negative pressure airduct.The length of thermal-arrest header is suitable with the negative pressure header, in the thermal-arrest header waste heat boiler 83 is set, and the heat energy that this waste heat boiler is collected can be used for cogeneration (afterheat generating system comprises drum 84, Turbo-generator Set 18, water pump 19).The thermal-arrest header is provided with a smoke discharging pipe 211, is respectively equipped with air heat exchanger 22, heat exchanger air blast 23, multi-tube dust cleaner 29, sack cleaner 28, air-introduced machine 27, active carbon adsorption case 26 and chimney 25 in this smoke discharging pipe.The hot-air of air heat exchanger output offers preheating device and heater by pipeline.
Referring to Fig. 6, Fig. 9, Figure 10, in the present embodiment, water seal conduit 20 bottoms are provided with sealing water, are provided with mud slide fastener 191 in the water seal conduit, and this slide fastener is installed on the roller rack 193, and roller rack is provided with a plurality of carrying rollers 194.This slide fastener is made of chain 192, scraper plate 195, great wheel 196, tail wheel 197, drive motors 199, can clear up the mud in the water seal conduit continuously, and mud is entered a sludge bin 198.
Referring to Fig. 1, in the present embodiment, the left end of described track is provided with slag row and unloads and slag collection device 4.Described slag collection device top is provided with tail dust excluding hood 41, the middle part is provided with the slag collection bucket, the bottom is provided with breaker, the slag that stove car row unloads is handled the back earlier through a refractory vibrating screen 24 through disintegrating machine, send into screening plant then, slag is separated into slag, haydite, ash by screening plant.The dust that the slag that the tail dust excluding hood unloads stove car row produces collects, by ducted deduster 3, blower fan 2, chimney 1 udst separation.
Referring to Figure 12, Figure 13, Figure 14, in the present embodiment, be provided with active carbon adsorption case 26 in the described smoke discharging pipe.This adsorption box can adsorb the harmful substances such as dioxin of carrying in the flue gas and change into innocuous substance.This adsorption box has a rectangular box 261, its top is adsorption chamber 262, its underpart is a collection chamber 263, the bottom is provided with air inlet 264, and the top is provided with exhaust outlet 265, and a plurality of tubular absorbers 266 are housed in the adsorption chamber, this absorber is made of inner frame 267, outer skeleton 268, active carbon fiber felt 269, described inside and outside skeleton is tubular, uniform a plurality of pores 260 on it, and active carbon fiber felt is installed between two skeletons.In the present embodiment, in order to reduce manufacturing cost, the sorbing material in the adsorption box can be an active carbon fiber felt, also can adopt active carbon particle.
The present invention uses above-mentioned step-by-step movement incinerator to carry out garbage disposal:
When the box-type furnace car arrives the haydite distributing device, by the haydite distributing device haydite ball blank is laid in the box-type furnace car and forms initial bed, by the rubbish distributing device rubbish is laid on the described initial bed then;
When the box-type furnace car arrives the preheating device position, use preheating device the rubbish in the box-type furnace car to be carried out preheating, preheat temperature 200-300 ℃;
When the box-type furnace car arrives igniter, by igniter rubbish to be lighted, the incineration temperature of control rubbish reaches 1100～1200 ℃; And starting exhausting system in box-type furnace car bottom generation negative pressure, guiding rubbish burns to the bottom from the top, sinters haydite ball blank into haydite; In the waste incineration process, use heater that the rubbish in the box-type furnace car is heated oxygen supply.
When the box-type furnace car arrived slag row and unloads, the overturning discharging was discharged to the grog that burns and carries out break process in the disintegrating machine, and the particle diameter that makes slag granules is less than 30 millimeters;
Grog after break process is collected screening plant by conveying device and is sieved processing, and complete haydite is collected the haydite storehouse, and ash is collected ash bin, and the slag granules material is collected the slag storehouse;
By transmitting device ash is transported to a system ball workshop, generates haydite ball blank, it is standby to be transferred to the haydite distributing device then;
To burn the flue gas and the dust that produce by smoke discharging pipe and collect and send into the flue gas processing pipeline;
In the flue gas processing pipeline, carry out purified treatment by multi-tube dust cleaner, sack cleaner;
The ash of described deduster being collected by transmitting device is transported to a system ball workshop, generates haydite ball blank, and it is standby to be transferred to the haydite distributing device then.
The described system ball of present embodiment workshop comprises haydite base batching dicang, batch mixer, disc-type pelletizing machine, and this batch mixer is conventional cylindrical mixer.
Embodiment two:
In order to improve the reliability of burning, and improve the heat energy utilization rate, increase following technical measures on the basis of embodiment one, the use system for compacting carries out compaction treatment to described rubbish when described cloth is finished after; When the section between box-type furnace car arrival distributing device and the igniter, use preheating device that the rubbish in the box-type furnace car is carried out preheating; After the grog screening of described burning is handled, the haydite of selecting is cooled off earlier, collect the haydite storehouse then; In the flue gas processing pipeline,, carry out purified treatment by activated carbon adsorption unit to burning flue gas and the dust that produces; By a waste heat boiler collection of energy in the described flue gas is got up, be used for cogeneration, perhaps be used for central heating.
Embodiment three:
Referring to Figure 15, a kind of walking-beam furnace car refuse burning system uses embodiment one described incinerator, and a rubbish dicang 38 is arranged, and is connected with described rubbish distributing device 13 by the rubbish pipeline, provides rubbish to incinerator continuously; There is an ash pipeline to be connected with refractory vibrating screen 24, ash is transported to a system ball workshop, in system ball workshop is that primary raw material is made haydite ball base with the ash, by a pipeline described haydite ball base is sent into described haydite distributing device 14 again, enter in the incinerator by the haydite distributing device; A flue gas processing pipeline is arranged, be provided with waste heat boiler 83, air heat exchanger 22, multi-tube dust cleaner 28, sack cleaner 29, blower fan 27 and activated carbon adsorption unit 26 in this pipeline; There is an ash pipeline to be connected, the isolated ash of this deduster is transported to the haydite base batching dicang 33 in system ball workshop with deduster 3 behind the described slag collection device.The described system ball of present embodiment workshop comprises haydite base batching dicang 33, cylindrical mixer 34, disc-type pelletizing machine 35, haydite base dryer 36, and this batch mixer is conventional cylindrical mixer; System ball workshop is that primary raw material is made haydite ball base by batch mixer, disc-type pelletizing machine with the ash, dry through haydite base dryer, by a pipeline described haydite ball base is sent into haydite base storehouse 37, described haydite distributing device is sent described haydite ball base into by a pipeline in haydite base storehouse.
The slag that stove car row unloads is handled the back through disintegrating machine and is isolated ash through a refractory vibrating screen 24 earlier, remaining slag is through a ring type cooler 30, a magnetic separator 31, send into screening plant 32 at last, by screening plant slag is separated into slag, haydite, sends into slag storehouse 44, haydite storehouse 45 respectively.
Stove car row unloads the dust that slag produces, collect by the tail dust excluding hood 41 that is installed in furnace body support, purify by ducted deduster 3, blower fan 2, chimney 10 dirt, the isolated ash of this deduster is transported to the ash of collecting by a pipeline haydite base batching dicang in system ball workshop.
In the present embodiment, the hot-air of air heat exchanger output offers preheating device 11 and heater 9 by pipeline.The steam of waste heat boiler 83 outputs offers Turbo-generator Set by pipeline.This unit comprises steamdrum 84, Turbo-generator Set 18, water pump 19.
Embodiment four:
Referring to Figure 15, use system of the present invention not only can burn away the refuse, can also handle municipal sludge and garbage leachate, on embodiment three bases, described rubbish dicang upstream is provided with place where the garage is piled up, also be provided with a sewage transport pipeline and a sludge carrier pipe line in this place where the garage is piled up, this sewage transport pipeline is connected with described system ball workshop respectively with the sludge carrier pipe line, and garbage leachate and municipal sludge are transported to the raw material of system ball workshop as haydite ball base.
In the present embodiment, rubbish dicang upstream is provided with place where the garage is piled up 42, rubbish magnetic separator 40, refuse grinder 39.Also be provided with a sewage transport pipeline and a sludge carrier pipe line in the described place where the garage is piled up, this sewage transport pipeline is connected with described system ball workshop respectively with the sludge carrier pipe line, have a municipal sludge storehouse 43 to be connected with described system ball workshop, the mud that garbage leachate, mud and municipal treatment plant are produced is transported to the raw material of system ball workshop as haydite ball base.
The first method of described haydite ball blank preparation is that its weight ratio is glass dust 1-10, rubbish ash or slag ash 90-99 with glass dust and rubbish ash or the mixed ball of slag ash.
The second method of described haydite ball blank preparation is that its weight ratio is glass dust 1-10 with glass dust, mud and rubbish ash or the mixed ball of slag ash, mud 10-30, rubbish ash or slag ash 60-80.
The third method of described haydite ball blank preparation is with algae soil, coal dust and rubbish ash or the mixed ball of slag ash, and its weight ratio is algae soil 1-5, coal dust 1-5, rubbish ash or slag ash 80-90.
Mode with the incineration treatment of garbage haydite can be called sintering process or fusion method, it is stable that haydite ball base forms physico-chemical property through 600-1000 degree high temperature sintering, the great material of hardness, harmful substances such as the dioxin in the garbage ash and city, heavy metal will combine under molten condition with glass dust and become the glass ore deposit mutually, this haydite has advantages of higher stability, be the material that is difficult for degraded and is not dissolved in water, but can preserve moisture and fertility.
Claims (10)
1, a kind of garbage incineration method is characterized in that:
Use the step-by-step movement incinerator, this incinerator has a furnace body support, one bar oven Car Track is arranged on it, a plurality of box-type furnace cars are set on this track, the bottom half of this box-type furnace car is provided with fire grate, one end of described track is provided with ferry-boat flatcar and hydraulic feed device, and the other end of described track is provided with slag row and unloads and the slag collection device; Described furnace body support upper strata is equipped with haydite distributing device, rubbish distributing device, preheating device, igniter successively; The negative pressure header is equipped with in described furnace body support middle level, and this negative pressure header top is communicated with described box-type furnace car bottom, and this negative pressure header bottom is communicated with many negative pressure airduct tops that are set up in parallel, and described negative pressure airduct middle part is communicated with a thermal-arrest header;
When the box-type furnace car arrives the haydite distributing device, by the haydite distributing device haydite ball blank is laid in the box-type furnace car and forms initial bed, by the rubbish distributing device rubbish is laid on the described initial bed then;
When the box-type furnace car arrives the preheating device position, use preheating device the rubbish in the box-type furnace car to be carried out preheating, preheat temperature 200-300 ℃;
When the box-type furnace car arrives igniter, by igniter rubbish to be lighted, the incineration temperature of control rubbish reaches 1100～1200 ℃; And starting exhausting system in box-type furnace car bottom generation negative pressure, guiding rubbish burns to the bottom from the top, sinters haydite ball blank into haydite; In the waste incineration process, use heater that the rubbish in the box-type furnace car is heated oxygen supply.
When the box-type furnace car arrived slag row and unloads, the overturning discharging was discharged to the grog that burns and carries out break process in the disintegrating machine, and the particle diameter that makes slag granules is less than 30 millimeters;
Grog after break process is collected screening plant by conveying device and is sieved processing, and complete haydite is collected the haydite storehouse, and ash is collected ash bin, and the slag granules material is collected the slag storehouse;
By transmitting device ash is transported to a system ball workshop, generates haydite ball blank, it is standby to be transferred to the haydite distributing device then;
To burn the flue gas and the dust that produce by smoke discharging pipe and collect and send into the flue gas processing pipeline;
In the flue gas processing pipeline, carry out purified treatment by multi-tube dust cleaner, sack cleaner;
The ash of described deduster being collected by transmitting device is transported to a system ball workshop, generates haydite ball blank, and it is standby to be transferred to the haydite distributing device then.
2, garbage incineration method according to claim 1 is characterized in that: use system for compacting that described rubbish is carried out compaction treatment after described cloth is finished; Grog after break process carries out hot screening to be handled, the slag that sieves out is carried out cooling processing, then cooled slag being carried out magnetic separation handles, isolate the carbon element metal object, slag after the magnetic separation processing is carried out regrading to be handled, the haydite of selecting is collected the haydite storehouse, and the slag granules of selecting is collected the slag storehouse, and the ash that sifts out is collected ash bin; In the flue gas processing pipeline,, carry out purified treatment by activated carbon adsorption unit to burning flue gas and the dust that produces; By a waste heat boiler collection of energy in the described flue gas is got up.
3, a kind of walking-beam furnace car refuse burning system, it is characterized in that: a step-by-step movement incinerator is arranged in described system, this incinerator has a furnace body support, one bar oven Car Track is arranged on it, a plurality of box-type furnace cars are set on this track, the bottom half of this box-type furnace car is provided with fire grate, and an end of described track is provided with ferry-boat flatcar and hydraulic feed device, and the other end of described track is provided with slag row and unloads and the slag collection device; Described furnace body support upper strata is equipped with haydite distributing device, rubbish distributing device, preheating device, igniter successively; The negative pressure header is equipped with in described furnace body support middle level, and this negative pressure header top is communicated with described box-type furnace car bottom, and this negative pressure header bottom is communicated with many negative pressure airduct tops that are set up in parallel, and described negative pressure airduct middle part is communicated with a thermal-arrest header; Described slag collection device bottom is provided with breaker, two-stage screening plant, concentration equipment; A rubbish dicang is arranged, be connected with described rubbish distributing device, provide rubbish to incinerator continuously by the rubbish pipeline; There is an ash pipeline to be connected with described screening plant, ash is transported to a system ball workshop, in system ball workshop is that primary raw material is made haydite ball base with the ash, by a pipeline described haydite ball base is sent into described haydite distributing device again, is entered in the incinerator by the haydite distributing device; A flue gas processing pipeline is arranged, be provided with waste heat boiler, air heat exchanger, deduster, blower fan and activated carbon adsorption unit in this pipeline; Have an ash pipeline to be connected with deduster behind the described slag collection device, the ash that this deduster is collected is transported to system ball workshop.
4, walking-beam furnace car refuse burning system according to claim 3, it is characterized in that: described rubbish dicang upstream is provided with place where the garage is piled up, also be provided with a sewage transport pipeline and a sludge carrier pipe line in this place where the garage is piled up, this sewage transport pipeline is connected with described system ball workshop respectively with the sludge carrier pipe line, and garbage leachate and municipal sludge are transported to the raw material of system ball workshop as haydite ball base.
5, walking-beam furnace car refuse burning system according to claim 4, it is characterized in that: described step-by-step movement incinerator, a furnace body support is arranged, one bar oven Car Track is housed on the described furnace body support, a plurality of box-type furnace cars are set on this track, the bottom half of this box-type furnace car is provided with fire grate, and the casing both sides are provided with wheel; One end of described furnace body support is provided with ferry-boat flatcar and hydraulic feed device, and the other end of described track is provided with slag row and unloads and the slag collection device; Described furnace body support upper strata is equipped with rubbish distributing device, preheating device, igniter successively; The negative pressure header is equipped with in described furnace body support middle level, this negative pressure header top is communicated with described box-type furnace car bottom, this negative pressure header bottom is communicated with many negative pressure airduct tops that are set up in parallel, this negative pressure BOD is communicated with the water seal conduit that is positioned at described furnace body support one side, and described negative pressure airduct middle part is communicated with a thermal-arrest header; Described ferry-boat flatcar be arranged on one with the vertically disposed up ferry-boat track of stove Car Track on, described slag row unload be arranged on one with the vertically disposed descending ferry-boat track of stove Car Track on, between described up ferry-boat track and the descending ferry-boat track traction track parallel with the stove Car Track is set, is provided with a tractor below this traction track.
6, continous way box incinerator according to claim 5, it is characterized in that: described igniter is provided with principal point firearm and auxiliary igniter.
7, continous way box incinerator according to claim 5 is characterized in that: be provided with bitubular eccentric swage between described rubbish distributing device and the preheating device.
8, continous way box incinerator according to claim 5, it is characterized in that: described thermal-arrest header is provided with flue, in this pipeline air heat exchanger is housed.
9, continous way box incinerator according to claim 5, it is characterized in that: described slag row unloads and is provided with a winch support, a winding plant, hinge is adorned a rotary parking platform on the described winch support, this parking platform is provided with the parking orbital segment that can dock with described stove Car Track level, this parking platform one end is by hinge and winch support hinge dress, and the other end is connected with the carrying cable of winding plant.
10, continous way box incinerator according to claim 5 is characterized in that: in the described thermal-arrest header waste heat boiler is set.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2004100499586A CN100445640C (en) | 2004-06-22 | 2004-06-22 | Refuse combustion and step-by-step combustion system of furnace vehicle |
| PCT/CN2004/000814 WO2005124234A1 (en) | 2004-06-22 | 2004-07-15 | A method and a step incinerator vehicle system for incinerating waste |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2004100499586A CN100445640C (en) | 2004-06-22 | 2004-06-22 | Refuse combustion and step-by-step combustion system of furnace vehicle |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1712777A true CN1712777A (en) | 2005-12-28 |
| CN100445640C CN100445640C (en) | 2008-12-24 |
Family
ID=35509775
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2004100499586A Expired - Fee Related CN100445640C (en) | 2004-06-22 | 2004-06-22 | Refuse combustion and step-by-step combustion system of furnace vehicle |
Country Status (2)
| Country | Link |
|---|---|
| CN (1) | CN100445640C (en) |
| WO (1) | WO2005124234A1 (en) |
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100491826C (en) * | 2007-08-01 | 2009-05-27 | 重庆科技学院 | Multiple row sectional drive combined type domestic garbage incinerator |
| CN100507363C (en) * | 2007-07-18 | 2009-07-01 | 重庆科技学院 | Built-in refuse incineration feed device |
| CN100510529C (en) * | 2007-07-18 | 2009-07-08 | 重庆科技学院 | Step drying type garbage pusher |
| CN103423732A (en) * | 2013-09-03 | 2013-12-04 | 孝感市保东新型节能燃料有限公司 | Modified boiler with crop straw replacing fire coal |
| CN103438460A (en) * | 2013-09-24 | 2013-12-11 | 李先强 | Garbage disposal system |
| CN103968369A (en) * | 2014-05-22 | 2014-08-06 | 上海捷世欧国际贸易有限公司 | Secondary carbon combustion system for waste wet ash in coal gasification |
| CN104896481A (en) * | 2015-06-11 | 2015-09-09 | 凯天环保科技股份有限公司 | Garbage incinerator and smoke gas purification plant for its application |
| CN105258135A (en) * | 2015-11-18 | 2016-01-20 | 宝鸡市晋旺达机械设备有限公司 | Box type harmless treatment drying-combusting furnace |
| CN106040697A (en) * | 2016-04-29 | 2016-10-26 | 田原宇 | Household garbage slag cleaning and sorting process |
| CN106552816A (en) * | 2016-11-29 | 2017-04-05 | 湖南省环境保护科学研究院 | The refuse disposal for being sorted after a kind of high-temperature heat treatment again and application process |
| CN106734093A (en) * | 2016-12-23 | 2017-05-31 | 北京首钢国际工程技术有限公司 | A kind of house refuse flying dust removes the device and its application method of removing heavy metals |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| JPS5547133A (en) * | 1978-09-28 | 1980-04-03 | Tsubakimoto Chain Co | Feeder |
| US4944236A (en) * | 1989-08-24 | 1990-07-31 | Sheen Chao Chin | Tunnel type garbage incinerator |
| US4986196A (en) * | 1990-08-13 | 1991-01-22 | Butch Adam F | Solid waste incinerator system |
| JPH0650517A (en) * | 1992-07-31 | 1994-02-22 | Kubota Corp | Incinerator |
| CN1106120A (en) * | 1994-01-27 | 1995-08-02 | 颜金清 | Incinerating assembly for refuse |
| CN2535672Y (en) * | 2002-04-16 | 2003-02-12 | 陈凤仪 | Horizontal continuously garbage-treatment incinerator |
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2004
- 2004-06-22 CN CNB2004100499586A patent/CN100445640C/en not_active Expired - Fee Related
- 2004-07-15 WO PCT/CN2004/000814 patent/WO2005124234A1/en active Application Filing
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100507363C (en) * | 2007-07-18 | 2009-07-01 | 重庆科技学院 | Built-in refuse incineration feed device |
| CN100510529C (en) * | 2007-07-18 | 2009-07-08 | 重庆科技学院 | Step drying type garbage pusher |
| CN100491826C (en) * | 2007-08-01 | 2009-05-27 | 重庆科技学院 | Multiple row sectional drive combined type domestic garbage incinerator |
| CN103423732B (en) * | 2013-09-03 | 2015-05-20 | 孝感市保东新型节能燃料有限公司 | Modified boiler with crop straw replacing fire coal |
| CN103423732A (en) * | 2013-09-03 | 2013-12-04 | 孝感市保东新型节能燃料有限公司 | Modified boiler with crop straw replacing fire coal |
| CN103438460A (en) * | 2013-09-24 | 2013-12-11 | 李先强 | Garbage disposal system |
| CN103968369A (en) * | 2014-05-22 | 2014-08-06 | 上海捷世欧国际贸易有限公司 | Secondary carbon combustion system for waste wet ash in coal gasification |
| CN104896481A (en) * | 2015-06-11 | 2015-09-09 | 凯天环保科技股份有限公司 | Garbage incinerator and smoke gas purification plant for its application |
| CN104896481B (en) * | 2015-06-11 | 2017-06-27 | 凯天环保科技股份有限公司 | A kind of incinerator and its smoke eliminator of application |
| CN105258135A (en) * | 2015-11-18 | 2016-01-20 | 宝鸡市晋旺达机械设备有限公司 | Box type harmless treatment drying-combusting furnace |
| CN106040697A (en) * | 2016-04-29 | 2016-10-26 | 田原宇 | Household garbage slag cleaning and sorting process |
| CN106552816A (en) * | 2016-11-29 | 2017-04-05 | 湖南省环境保护科学研究院 | The refuse disposal for being sorted after a kind of high-temperature heat treatment again and application process |
| CN106734093A (en) * | 2016-12-23 | 2017-05-31 | 北京首钢国际工程技术有限公司 | A kind of house refuse flying dust removes the device and its application method of removing heavy metals |
Also Published As
| Publication number | Publication date |
|---|---|
| CN100445640C (en) | 2008-12-24 |
| WO2005124234A1 (en) | 2005-12-29 |
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