CN105927984A - Tar treatment chamber and smoke-free waste incineration system - Google Patents

Tar treatment chamber and smoke-free waste incineration system Download PDF

Info

Publication number
CN105927984A
CN105927984A CN201610522698.2A CN201610522698A CN105927984A CN 105927984 A CN105927984 A CN 105927984A CN 201610522698 A CN201610522698 A CN 201610522698A CN 105927984 A CN105927984 A CN 105927984A
Authority
CN
China
Prior art keywords
water
box
cooling
smoke
pipe
Prior art date
Application number
CN201610522698.2A
Other languages
Chinese (zh)
Other versions
CN105927984B (en
Inventor
陈仕敏
Original Assignee
陈仕敏
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 陈仕敏 filed Critical 陈仕敏
Priority to CN201610522698.2A priority Critical patent/CN105927984B/en
Publication of CN105927984A publication Critical patent/CN105927984A/en
Application granted granted Critical
Publication of CN105927984B publication Critical patent/CN105927984B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/44Details; Accessories
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D50/00Combinations of devices for separating particles from gases or vapours
    • B01D50/004Combinations of devices relating to groups B01D45/00 and B01D47/00
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/005Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by heat treatment
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/46Removing components of defined structure
    • B01D53/48Sulfur compounds
    • B01D53/485Sulfur compounds containing only one sulfur compound other than sulfur oxides or hydrogen sulfide
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/74General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/77Liquid phase processes
    • B01D53/78Liquid phase processes with gas-liquid contact
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2251/00Reactants
    • B01D2251/40Alkaline earth metal or magnesium compounds
    • B01D2251/404Alkaline earth metal or magnesium compounds of calcium
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2257/00Components to be removed
    • B01D2257/20Halogens or halogen compounds
    • B01D2257/206Organic halogen compounds
    • B01D2257/2064Chlorine
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2258/00Sources of waste gases
    • B01D2258/02Other waste gases
    • B01D2258/0283Flue gases
    • B01D2258/0291Flue gases from waste incineration plants
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2259/00Type of treatment
    • B01D2259/12Methods and means for introducing reactants
    • B01D2259/124Liquid reactants

Abstract

The invention provides a tar treatment chamber which comprises a treatment box body, a plurality of first water-cooling walls and a plurality of second water-cooling walls, wherein a partition plate is mounted in the treatment box body; the treatment box body comprises a top plate and a bottom plate which are opposite to each other; the treatment box body is divided into an upper box body and a lower box body by the partition plate; an exhaust structure is mounted on the treatment box body; a smoke outlet pipe of the exhaust structure penetrates through the upper box body and then extends into the lower box body; the upper box body communicates with the lower box body through a communicating pipe; the first water-cooling walls are mounted in the lower box body; gaps I are formed in the bottoms of the first water-cooling walls; first gas holes are formed above the gaps I; the tops of the first water-cooling walls incline to one side of the smoke outlet pipe respectively; the second water-cooling walls are mounted in the upper box body; gaps II are formed in the bottoms of the second water-cooling walls; second gas holes are formed above the gaps II; the exhaust structure is used for exhausting hot smoke into the lower box body; the hot smoke passes through the first water-cooling walls in sequence and then enters the upper box body through the communicating pipe; and the hot smoke passes through the second water-cooling walls in sequence and then is exhausted out of the treatment box body.

Description

A kind of tar processing room and non smoke refuse burning system
[technical field]
The present invention relates to a kind of refuse burning system, the tar processing room being specifically related in a kind of refuse burning system.
[background technology]
Along with growth in the living standard, the thing followed is then substantial amounts of house refuse, and at present, the mode of garbage disposal mainly has Sanitary landfill method, During High-Temperature Composting method and burning method.Sanitary landfill method garbage treatment quantity is big, simple to operate, but investment is big, rubbish The percolate intractability produced is big, and antiseepage film is damaged or percolate is bypassed the dam site, and easily makes a large amount of garbage leachate be penetrated into by earth's surface Surrounding enviroment and underground water source are caused severe contamination by underground.During High-Temperature Composting method make rubbish after compost treatment, house refuse Become humus health, tasteless.Both solve the outlet of rubbish, can reach again the purpose of resource, but house refuse heap Fertile amount is big, and nutrient content is low, and life-time service easily causes soil compaction and groundwater quality degenerates.Burning method is that rubbish is placed in high temperature In stove so that it is a kind of method that middle combustible component is fully oxidized, currently mainly there are again combustion-type, rotary furnace disc type, pyrolysis formula etc., Treatment effect is pretty good, but all there is the problems such as investment is big, incineration firing amount is little, incineration firing is insufficient, and dust treatment difficulty is up to standard.
[summary of the invention]
In view of the foregoing, it is necessary to a kind of tar processing room and non smoke refuse burning system, this tar processing cell structure are provided Simply, and can effectively remove the tar in smoke removing, reduce and pollute;It addition, this non smoke refuse burning system has process cigarette The filtration of heterogeneity in mist, has continuous high temperature resolving harmful gas simultaneously, reaches the purpose of zero smog emission.
For reaching above-mentioned purpose, the technical solution adopted in the present invention is: a kind of tar processing room, if including process casing Dry first water-cooling wall and some second water-cooling walls, be provided with dividing plate, and include relative top board and base plate in described treatment box body, Described process casing is divided into upper box and lower box by described dividing plate, and described process casing is provided with an exhaust structure, described in take out The pipe of wind structure can stretch into described lower box, described upper box and described lower box by connection after described upper box Pipe connects;Described some first water-cooling walls are separately mounted in described lower box, and top is connected with described dividing plate, bottom and institute Stating base plate to connect, the bottom of each first water-cooling wall offers breach, and has the first passage corresponding breach is opened above, The position of the first passage of adjacent first water-cooling wall is crisscross arranged, and the water level in described lower box is higher than described breach, less than institute State the first passage;The top of described some first water-cooling walls is respectively facing described pipe lopsidedness;Described some second water Cold wall is separately mounted in described upper box, and top is connected with described top board, and bottom is connected with described dividing plate, each second water The bottom of cold wall offers breach, and has the second passage corresponding breach is opened above, and the water level of described upper box is higher than Described breach, less than described second passage;The top of described some second water-cooling walls is respectively facing described connecting tube;Institute Stating some second water-cooling walls to be separately mounted in described upper box, and top is connected with described top board, bottom is connected with described dividing plate, The bottom of each second water-cooling wall offers breach, and has the second passage, described upper box corresponding breach is opened above Water level higher than described breach, less than described second passage;The top of described some second water-cooling walls is respectively facing described connection Pipe tilts.
A kind of non smoke refuse burning system, described non smoke refuse burning system includes incinerator, dust catching case, tar Process chamber, spun down tank, convection current dust arrester and column for smoke purification;Described incinerator connects with described dust catching case, institute State dust catching case to be connected with described tar processing room by an exhaust structure;Described tar processing room also includes some first water Cold wall and some second water-cooling walls, be provided with dividing plate, and include relative top board and base plate in described treatment box body, described every Described process casing is divided into upper box and lower box by plate, and described process casing is provided with an exhaust structure, described exhaust structure Pipe can be connected through stretch into described lower box, described upper box and described lower box after described upper box by communicating pipe; Described some first water-cooling walls are separately mounted in described lower box, and top is connected with described dividing plate, and bottom is with described base plate even Connecing, the bottom of each first water-cooling wall offers breach, and has the first passage corresponding breach is opened above, and adjacent first The position of the first passage of water-cooling wall is crisscross arranged, and the water level in described lower box is higher than described breach, logical less than described first Pore;The top of described some first water-cooling walls is respectively facing described pipe lopsidedness;Described some second water-cooling walls are respectively Being arranged in described upper box, and top is connected with described top board, bottom is connected with described dividing plate, the end of each second water-cooling wall Portion offers breach, and has the second passage corresponding breach is opened above, and the water level of described upper box is higher than described breach, Less than described second passage;The top of described some second water-cooling walls is respectively facing described connecting tube;Described exhaust structure In order to heat smoke to be evacuated to described lower box, heat smoke is entered on described by described communicating pipe after sequentially passing through some first water-cooling walls Casing, heat smoke discharges described process casing to described rotational flow settlement tank after sequentially passing through some second water-cooling walls;Described eddy flow sinks Fall tank connects described convection current dust arrester, and described convection current dust arrester connects described column for smoke purification, and described column for smoke purification passes through Another smoke exhaust pipe connects described incinerator.
The method have the advantages that
Heat smoke is evacuated to described lower box via described exhaust structure by the present invention, after heat smoke sequentially passes through some first water-cooling walls Being entered described upper box by described communicating pipe, heat smoke discharges described process casing after sequentially passing through some second water-cooling walls, because of water The effect of cold wall, flue gas fast cooling, decrease Hydrocarbon, carbon monoxide and nitrogen oxides particularly two English etc. harmful The regeneration of material, meanwhile, heat smoke meets cold formation tar fog, the impurity submerged in tar fog parcel flue gas, reduces harmful The discharge of material.
[accompanying drawing explanation]
Fig. 1 is a structural representation of non smoke refuse burning system the first embodiment of the present invention.
Fig. 2 is an enlarged drawing of II part in Fig. 1.
Fig. 3 is to dissipate chimney and a structural representation of bonnet in non smoke refuse burning system of the present invention.
Fig. 4 is a three-dimensional structure diagram of grate in non smoke refuse burning system of the present invention.
Fig. 5 is a structural representation of dust catching case in non smoke refuse burning system of the present invention.
Fig. 6 is a structural representation of the coal-tar middle oil process chamber of non smoke refuse burning system of the present invention.
Fig. 7 is a structural representation of rotational flow settlement tank in non smoke refuse burning system of the present invention.
Fig. 8 is a structural representation of convection current dust arrester in non smoke refuse burning system of the present invention.
Fig. 9 is a structural representation of column for smoke purification in non smoke refuse burning system of the present invention.
Figure 10 is a structural representation of the clean cigarette dish of column for smoke purification in Fig. 9.
Main element symbol description
Following detailed description of the invention will further illustrate the present invention in conjunction with above-mentioned accompanying drawing.
[detailed description of the invention]
Refer to Fig. 1, in one embodiment of the present invention, a non smoke refuse burning system 100 include an incinerator 10, One dust catching case 20, tar processing room 40, rotational flow settlement tank 50, convection current dust arrester 60 and a column for smoke purification 70.Described incinerator 10 connects described dust catching case 20, and described tar processing room 40 connects institute by an exhaust structure 80 Stating dust catching case 20, described rotational flow settlement tank 50 connects described convection current dust arrester 60, and described convection current dust arrester 60 connects Described column for smoke purification 70, described column for smoke purification 70 connects described incinerator 10 by a smoke exhaust pipe 90.Implement in the present invention In mode, described exhaust structure 80 is high pressure positive blower.
Please also refer to Fig. 2, described incinerator 10 includes that feed arrangement 11, drying chamber 12, body of heater 13, is slagged tap dress Put 14, one fume high-temperature process tank 15 and a chimney 16.Described drying chamber 12 is arranged on the side of described body of heater 13, and part Stretching in described body of heater 13, described feed arrangement 11 stretches into the inside of described drying chamber 12, and is driven by one first driving means 111 Dynamic, in order to rubbish to be delivered to described drying chamber 12, in the present embodiment, described feed arrangement 11 is conveyer belt, and described first drives Dynamic device 111 is motor, and this motor can manually or automatically control to be turned on and off.Described deslagging device 14 is positioned at described body of heater The lower section of 13, described fume high-temperature process tank 15 is arranged on described body of heater 13, and part exposes described body of heater 13.Described chimney 16 tops being arranged on described fume high-temperature process tank 15, and connect with described fume high-temperature process tank 15.
Described body of heater 13 includes inner furnace body 131 and an external furnace body 132, and described inner furnace body 131 and described external furnace body 132 weld On same pedestal 130, and there is identical central shaft;In at described fume high-temperature, tank 15 is partially installed on described inner furnace body 131 In, and surround a combustor 133 together with described inner furnace body 131, described pedestal 130, described inner furnace body 131 and described external furnace body Being formed with a flue gas recirculation room 134 between 132, the width of described flue gas recirculation room 134 is more than 40cm, embodiment party of the present invention In formula, described inner furnace body 131 and described external furnace body 132 are the cylindrical tube that steel plate is rolled into, described inner furnace body 131 interior Surface mount has the double-deck refractory brick of resistance to 1500 DEG C of high temperature, and it must be to carry out gear-like stickup along cylinder that refractory brick is pasted, gear Scattered flue (not shown) when recess position is incineration firing.
The sidewall of described inner furnace body 131 offers some through holes 135 of the described combustor of connection 133 and described flue gas recirculation room 134, Described some through holes 135 equidistantly distribute on the sidewall of described inner furnace body 131, and each through hole 135 ecto-entad is downward-sloping, And aperture is 15-25cm, it is preferable that aperture is 20cm;Described external furnace body 132 is provided with connection in the lower section of described drying chamber 12 Described dust catching case 20 and the smoke exhaust pipe 210 of described combustor 133.
It is provided with igniting chamber 137, grate 138, bonnet 139 and in described combustor 133 and dissipates chimney 140.Described scattered Chimney 140 top connects described fume high-temperature process tank 15, and bottom is provided with described bonnet 139, and described scattered chimney 140 is provided with Some smoke-dispelling holes 141 (see Fig. 3), it is preferable that described scattered chimney 140 is made up of thick steel pipe, and central shaft and described inner furnace body The central shaft of 131 overlaps.Please also refer to Fig. 3 and Fig. 4, described bonnet 139 is arranged on described pedestal 130, described pedestal 130 The tapered body of inwall, described fume high-temperature process tank 15 is arranged to arch near described combustor 33 side, and towards described combustion Burn side, room 133 protruding.Described igniting chamber 137 is arranged on the bottom of described bonnet 139, is fire-resistant by resistance to 1500 DEG C of high temperature The cylindrical tube of brick one-tenth is constituted.Described grate 138 is arranged in described igniting chamber 137, and include grate 1381 and Grate 1382 on one, described lower grate 1381 is crisscross arranged with described upper grate 1382.
Described drying chamber 12 includes feed bin 121, steam delivery pipe 122, grille door 123, push rod 124 and one second Driving means 125.Described feed arrangement 11 is connected with described feed bin 121, in order to rubbish to be delivered to described feed bin 121, described water Vapour delivery pipe 122 one end connects described feed bin 121, and the other end connects described dust catching case 20.Described feed bin 121 part stretches into Described inner furnace body 131, and bottom is provided with a stock guide 1211, and described stock guide 1211 tilts towards described body of heater 13, and And part stretches into described combustor 133, described grille door 123 is arranged on described feed bin 121 and is positioned at described inner furnace body 131, In order to be turned on and off described feed bin 121, specifically, described grille door 123 one end is rotatably connected with described feed bin 121, the other end Can against or depart from described stock guide 1211.Described push rod 124 one end connects described grille door 123, and the other end connects described second Driving means 125, described second driving means 125 is in order to push or pull on described push rod 124, and then is turned on and off described grid Door 123, in embodiments of the present invention, described second driving means 125 is motor.
Referring to Fig. 5, described dust catching case 20 includes interception casing 21, water intaking valve 22, drain valve 23, water Position monitoring valve 24 and some interception structures 25.Described interception casing 21 equipped with water, and include top board 211, base plate 212, Relative biside plate 213, back plate 214 and a header board 215;Described biside plate 213, described back plate 214 and described header board 215 Being respectively perpendicular connection described top board 211 and described base plate 212, described biside plate 213 is respectively perpendicular the described back plate 214 of connection and described Header board 215, it is preferable that described interception casing 21 is seal case, and is cuboid, it addition, described interception casing 21 is by thickness Steel plate is made.Described water intaking valve 22 is arranged on a water inlet pipe 221, and it is internal that described water inlet pipe 221 connects described interception casing 21, Described water intaking valve 22 is in order to control entering of water in described interception casing 21.Described drain valve 23 is arranged on an outlet pipe 231, It is internal that described outlet pipe 221 connects described interception casing 21, and described drain valve 23 is in order to control the row of water in described interception casing 21 Go out.Described monitoring water level valve 24 is in order to monitor whether the water level in described interception casing 21 exceeds predeterminated position, when described interception case When water level in body 21 is opened beyond predeterminated position and described monitoring water level valve 24, water will overflow, to inform staff, and institute State the water intercepted in casing 21 enough, described water intaking valve 22 can be closed.In the present embodiment, described water inlet pipe 221 and One end of described steam delivery pipe 122 is separately mounted on described top board 211, and connects in described interception casing 21;Described row One end of smoke pipe 210 and described outlet pipe 231 is respectively mounted wherein on side plate 213.The exhaust column 81 of described exhaust structure 80 (see Fig. 6) is positioned on another side plate 213.
Please continue to refer to Fig. 5, described some interception structures 25 are sequentially arranged in described interception casing 21 respectively, it is preferable that described Some interception structures 25 are on a same straight line being parallel to described interception casing 21 inner horizontal;Each group of interception structure 25 includes Having catching sheet 252 on catching sheet 251 and, the top of some described upper catching sheets 252 connects described top board 211, some under Conflict with the water intercepted in casing 21 in the bottom of catching sheet 251, it is preferable that be sequentially connected with some lower catching sheets 251 and some on block The line cutting plate 252 central point is a zigzag.Some described lower catching sheets 251 and some described upper catching sheets 252 are parallel to each other, The bottom of every once catching sheet 251 and each upper catching sheet 252 is all towards described smoke exhaust pipe 210 lopsidedness, and often once blocks Cutting the direction A that plate 251 and each upper catching sheet 252 and described smoke exhaust pipe 210 point to described exhaust structure 80 is 140-160 °; Distance between adjacent lower catching sheet 251 and upper catching sheet 252 is 20-80cm, and the top margin of lower catching sheet 251 and upper catching sheet The difference in height of the top margin of 252 is 30-50cm;Every top margin of catching sheet 251 once is 30-50cm with the difference in height of described top board 211, The base of each upper catching sheet 252 is 30-50cm with the difference in height of described interception casing 21 inner horizontal, in the present embodiment, It is 150 ° that every catching sheet 251 once and each upper catching sheet 252 and described smoke exhaust pipe 210 point to the direction A of described exhaust structure 80; Distance between adjacent lower catching sheet 251 and upper catching sheet 252 is 50cm, and the top margin of lower catching sheet 251 and upper catching sheet 252 The difference in height of top margin be 40cm;Every top margin of catching sheet 251 the most once is 40cm with the difference in height of described top board 211, each on block Cutting the base of plate 252 with the difference in height of described interception casing 21 inner horizontal is 40cm.So, during use, described combustor 133 In smog be extracted into interception casing 21 by described exhaust structure 80, smog sequentially passes through some described lower catching sheets 251 and some described After upper catching sheet 252, in smog, larger particles is blocked and fall in water, and in such smog, larger particles is at described dust catching It is evacuated to described tar processing room 40 by described exhaust structure 80 again after being removed in case 20.
Refer to Fig. 6, described tar processing room 40 include process casing 41, two water intaking valve 42,43, drain valve 44, Some first water-cooling walls 45, some second water-cooling wall 46 and two monitoring water level valves 47,48, in the present embodiment, described some The quantity of the first water-cooling wall 45 and some second water-cooling walls 46 all at least 6.Described process casing 41 include a top board 411, One base plate 412, biside plate 413, back plate 414 and a header board 415.Described biside plate 413, described back plate 414 and described before Plate 415 is respectively perpendicular the described top board 411 of connection and described base plate 412, and described biside plate 413 is respectively perpendicular the described back plate 414 of connection And described header board 415.In embodiments of the present invention, described process casing 41 is seal case, and is made up of steel plate, Preferably, described process casing 41 is cuboid.Being also equipped with a dividing plate 416 in described process casing 41, described dividing plate 416 will Described process casing 41 is divided into upper box 417 and a lower box 418, it is preferable that described upper box 417 volume and described nowel Body 418 volume is equal.The pipe 82 of described air draft mechanism 80 stretches into described lower box 418 after described upper box 417.Institute State upper box 417 and described lower box 418 is connected by a connecting pipe 419.
Water intaking valve 42,43 described in two is separately mounted on a water inlet pipe 421,431, and described water inlet pipe 421 connects described upper box 417, described water inlet pipe 431 connects described lower box 418, and described water intaking valve 42,43 is in order to control described upper box 417, described Entering of the cold water of lower box 418.Described drain valve 44 is arranged on an outlet pipe 441, and described outlet pipe 441 is respectively communicated with institute Stating upper box 417 and the inside of described lower box 418, described drain valve 44 is in order to control described upper box 417 and described lower box The discharge of 418 inner cold waters.Described two monitoring water level valves 47,48 are respectively in order to monitor described upper box 417 and described lower box 418 Water level whether beyond preset water level, when the water level of described upper box 417 and described lower box 418 is beyond preset water level and described water When position monitoring valve 47,48 is opened, water will overflow, to inform staff, and the water of upper box 417 and lower box 418 foot Enough, water intaking valve 42,43 can be closed.
Please continue to refer to Fig. 6, described some first water-cooling walls 45 are separately mounted in described lower box 418, and top with described every Plate 416 connects, and bottom is connected with described base plate 412, it is preferable that described some first water-cooling walls 45 are parallel to each other;Each first The bottom of water-cooling wall 45 offers a breach 451, and has one first passage 452 corresponding breach 451 is opened above, adjacent The position of the first passage 452 of the first water-cooling wall 45 is crisscross arranged, and the water level of described lower box 418 is higher than described breach 451, Less than described first passage 452;The top of described some first water-cooling walls 45 is respectively facing described pipe 82 lopsidedness, and And the angle of the central shaft of the outlet flue of each first water-cooling wall 45 and described pipe 82 is 25-35 °;Adjacent first water-cooling wall Distance between 45 is 50-80cm;Preferably, the central shaft of each first water-cooling wall 45 and the outlet flue of described pipe 82 Angle is 30 °.
Described some second water-cooling walls 46 are separately mounted in described upper box 417, and top is connected with described top board 411, bottom It is connected with described dividing plate 416, it is preferable that described some second water-cooling walls 46 are parallel to each other, the bottom of each second water-cooling wall 46 Offer a breach 461, and have one second passage 462 corresponding breach 461 is opened above, in embodiments of the present invention, It is sequentially connected with the second passage 462 on described some second water-cooling walls 46 on the straight line being parallel to described dividing plate 416;On described The water level of casing 417 is higher than described breach 461, less than described second passage 462;The top of described some second water-cooling walls 46 It is respectively facing and tilts described communicating pipe 419, and the angle between each second water-cooling wall 46 and the central shaft of described communicating pipe 419 For 25-35 °;Preferably, the angle between each second water-cooling wall 46 and the central shaft of described communicating pipe 419 is 30 °.Described Tar processing room 40 is also provided with a smoke exhaust pipe 49 at the side plate 413 away from described communicating pipe 419.When incineration firing, described convulsion Heat smoke is evacuated to described lower box 45 by structure 80, and heat smoke sequentially passed through after some first water-cooling walls 45 by described communicating pipe 419 Entering described upper box 417, heat smoke discharges described process casing 41, because of water-cooling wall after sequentially passing through some second water-cooling walls 46 Effect, flue gas fast cooling, decrease Hydrocarbon, carbon monoxide and nitrogen oxides particularly two the harmful substance such as English again Raw, meanwhile, heat smoke meets cold formation tar fog, and tar fog wraps up the impurity submerged in flue gas, then via described smoke exhaust pipe 49 Discharge described tar processing room 40 to described rotational flow settlement tank 50.
Referring to Fig. 7, described rotational flow settlement tank 50 includes lower tank 51, upper tank body 52, a connecting pipe 53, two water inlet Valve 54,55, two drain valve 56,57 and two monitoring water level valve 58,59.Described lower tank 51 is cylindrical seal tank body, described Described lower tank 51 is stretched in one end of smoke exhaust pipe 49, and the central shaft of exhaust opening is vertical with the sidewall of described lower tank 51.Described Upper tank body 52 is arranged on the top of described lower tank 51, and is connected with described lower tank 51 by described drain valve 56;Work as institute Stating drain valve 56 when opening, the water of described upper tank body 52 can enter described lower tank 51;Described communicating pipe 53 connects described lower tank Body 51 and upper tank body 52, and the one end of described communicating pipe 53 stretches into described upper tank body 52, and the central shaft of outlet flue and institute The sidewall stating upper tank body 52 is vertical.
Described two water intaking valves 54,55 are separately mounted to a water inlet pipe 541,551, and described water inlet pipe 541 connects described upper tank body 52, Described water inlet pipe 551 connects described lower tank 51.Described drain valve 57 is arranged on described lower tank 51, in order to by described lower tank Filthy water in body 51 is discharged.Described two monitoring water level valves 58,59 are separately mounted on an adjutage 581,591, described adjutage 581 connect described upper tank body 52, and the height of the central shaft of the end of the entry bottom of described adjutage 581 and described communicating pipe 53 Degree difference is ± 4cm, and the central shaft of the outlet flue of the most described communicating pipe 53 is ± 4cm with the height of water level difference of described upper tank body 52;Institute State adjutage 591 to connect in described lower tank 51, and the end of the entry bottom of described adjutage 591 and described smoke exhaust pipe 49 The difference in height of mandrel is ± 4cm, the height of water level difference of the central shaft of the exhaust opening of the most described smoke exhaust pipe 49 and described lower tank 51 is ± 4cm;Preferably, the entry bottom of described adjutage 581 is 0 with the difference in height of the central shaft of the end of described communicating pipe 53, described The entry bottom of adjutage 591 is 0 with the difference in height of the central shaft of the end of described smoke exhaust pipe 49;It addition, described upper tank body 52 and Adding CaO (calcium oxide) in the water of described lower tank 516, the top of described upper tank body 52 is also equipped with a smoke exhaust pipe 521, flue gas In SO2Settle with the liquid cyclone containing CaO (calcium oxide) in described rotational flow settlement tank 50, thus remove particulate contamination in flue gas And element sulphur, to described convection current dust arrester 60 after then discharging via described smoke exhaust pipe 521.
Referring to Fig. 8, described convection current dust arrester 60 includes some water tanks 61, and enters cigarette condensation tube 62, some intermediate condensation cylinders 63, smoke condensation tube 64, water intaking valve 65, some monitoring water level valves 66, some drain valves 67 and some communicating pipes 69, In present embodiment, the quantity of described some water tanks 61, described some monitoring water level valves 66 and the quantity of described some drain valves 67 Quite, and be 2;Each water tank 61 is welded by steel plate, and in cuboid.Described water intaking valve 65 is arranged on one On water inlet pipe 651, described water inlet pipe 651 is respectively communicated with described some water tanks 61, if described water intaking valve 65 is in order to control described solid carbon dioxide Entering of case 61 water;Described some drain valves 67 are separately mounted on some outlet pipes 671, and described some outlet pipes 671 are respectively Connecting described some water tanks 61, described some drain valves 67 are in order to control the discharge of water in described some water tanks 61;If described solid carbon dioxide Position monitoring valve 66 is separately mounted on described some water tanks 61, in order to monitor whether the water level in corresponding water tank 61 exceeds preset water level, When the water level in corresponding water tank 61 is opened beyond preset water level and corresponding monitoring water level valve 66, water will overflow, to inform work Personnel, can close water intaking valve 65.
Described enter the quantity such as cigarette condensation tube 62, described some intermediate condensation cylinders 63 and described smoke condensation tube 64 be separately mounted to described On some water tanks 61, and connect with corresponding water tank 61 respectively, described in enter cigarette condensation tube 62, described some intermediate condensation cylinders 63 And described smoke condensation tube 64 has identical structure, and by being sequentially communicated described some communicating pipes 69, described smoke exhaust pipe 521 End vertical insert described in enter cigarette condensation tube 62;Preferably, enter described in cigarette condensation tube 62, described some intermediate condensation cylinders 63 and Described smoke condensation tube 64 is cylindrical shape, and is made by steel plate.Adjacent enter cigarette condensation tube 62 and intermediate condensation cylinder 63 or One end of communicating pipe 69 between adjacent two intermediate condensation cylinders 63 or adjacent intermediate condensation cylinder 63 and smoke condensation tube 64 is connected into cigarette Condensation tube 62 or intermediate condensation cylinder 63, the other end is stretched in another intermediate condensation cylinder 63 or smoke condensation tube 64, further, Stretch into central shaft and the horizontal plane in corresponding water tank 61 of the end of the communicating pipe 69 of intermediate condensation cylinder 63 or smoke condensation tube 64. Described smoke condensation tube 64 connects a smoke exhaust pipe 641, and flue gas is entered convection current dust arrester 60 by described smoke exhaust pipe 521, and flue gas is by right Answer the obstruction of water tank 61 surrounding and enter cigarette condensation tube 62, intermediate condensation cylinder 63 or the smoke condensation tube 64 above water tank 61 recoils, The flue gas sprayed with described smoke exhaust pipe 521 or communicating pipe 69 again is at smoke condensation tube 62 or intermediate condensation cylinder 63 or smoke condensation tube 64 Fierce head-on collision, makes the oil reservoir being wrapped in dust surface be peeled off, so that dust is able to quick submerged, flue dust is through described Convection current dust arrester 60 process after through being delivered to described column for smoke purification 70 by described smoke exhaust pipe 641, it is preferable that described in enter cigarette condensation tube 62, each intermediate condensation cylinder 63, smoke condensation tube 64 central axis in the horizontal plane of corresponding water tank 61.
Refer to Fig. 9 and Figure 10, if described column for smoke purification 70 includes a purifying tube 71 clean cigarette dish 72, drain valve 73 And stair 74.Described purifying tube 71 is cylindrical tube, and is made up of steel plate.If described clean cigarette dish 72 is separately mounted to In described purifying tube 71, the corresponding each clean cigarette dish 72 of the inwall of described purifying tube 71 is convexly equipped with support (not shown meaning), described Frame in order to support the clean cigarette dish 72 of correspondence, such as, can be made up of some ribs.Each clean cigarette dish 72 is respectively by two halves disk 721 Composition, in the present embodiment, described two halves disk 721 is rotated by hinge 722 and is fixed together, a wherein semi-disc 721 Offering some exhaust smoke holes 7211, second half disk 721 is provided with scavenging material, described scavenging material in order to absorb in flue gas Grain, can be flannelette, activated carbon etc..If install described clean cigarette dish 72, in the direction of parallel described purifying tube 71 central shaft On, the semi-disc 721 in adjacent clean cigarette dish 72 with some exhaust smoke holes 7211 has the half of scavenging material on another clean cigarette dish 72 Disk 721 is crisscross arranged, it is preferable that if described clean cigarette dish 72 is arranged in parallel.Described clean cigarette dish 72 is installed for convenience, Being further opened with two windows 711 on the sidewall of described purifying tube 71, described stair 74 are arranged on the outer wall of described purifying tube 71, work Make personnel by described stair 74 of creeping, and to be installed to described purifying tube 71 through window 711 by clean cigarette dish 72.Described row Water valve 73 is arranged on described purifying tube 71, and near the bottom of described purifying tube 71;Preferably, if described clean cigarette dish 72 It is parallel to each other, if described clean cigarette dish 72 equidistantly distributes on described purifying tube 71.
One end of described smoke exhaust pipe 641 is arranged on described purifying tube 71, and near the bottom of described purifying tube 71, in order to by right The flue gas that stream dust arrester 60 processed drains into described column for smoke purification 70;The top of described purifying tube 71 is provided with described smoke exhaust pipe 90, the other end of described smoke exhaust pipe 90 stretches into described fume high-temperature process tank 15, in order to will process via described column for smoke purification 70 The flue dust crossed enters described fume high-temperature process tank 15.The flue gas that convection current dust arrester 60 processed is entered institute by described smoke exhaust pipe 641 State column for smoke purification 70, if after sequentially passing through described clean cigarette dish 72, the fine particle in flue gas is by the purification material on clean cigarette dish 72 Material absorption, drain into described fume high-temperature process tank 15 via described smoke exhaust pipe 90 the most again, described fume high-temperature process tank 15 in order to Pyrolytic toxic gas, such as two English etc..
The preferable working method of the one of non smoke refuse burning system 100 of the present invention is as follows: described feed bin delivered to by rubbish by feed arrangement 11 121, simultaneously close off described grille door 123, prevent the rubbish do not dried to be directly entered described combustor 133;Use non smoke rubbish During CIU 100, being lighted by the rubbish in combustor 133 by igniting chamber 137, the thermal current that incineration firing produces is at flue gas Spread rapidly under the effect of circular chamber 134 and scattered chimney 140, and the fresh air come in igniting chamber 137 be quickly sufficiently mixed, Guarantee that rubbish can fully burn, it is not necessary to add any oxidizer;It addition, the smog in combustor 133 is via described exhaust structure The effect of 80, is entered described dust catching case 20 by described smoke exhaust pipe 210, and meanwhile, the heat in described combustor 133 passes through institute State grille door 123 rubbish in described feed bin 121 is toasted so that the steam in rubbish passes through described steam delivery pipe 122 Enter after described dust catching case 20, steam and smog enter described dust catching case 20 and sequentially pass through some interception structures 25 Stop and will in smog larger particles dust intercept after fall in water, such larger particles dust be removed after flue gas stream by institute State exhaust structure 80 and be evacuated to described tar processing room 40.
Flue gas stream enters behind described tar processing room 40, sequentially passes through after some first water-cooling walls 45 of lower box 418 through top box Some second water-cooling walls 46 of body 417, heat smoke because of the effect of water-cooling wall, flue gas fast cooling, decrease Hydrocarbon, one Particularly two regeneration of the harmful substance such as English of carbonoxide and nitrogen oxides, meanwhile, heat smoke meets cold formation tar fog, tar fog bag Wrapping up in the impurity submerged in flue gas, the most treated flue gas drains in described rotational flow settlement tank 50.
Flue gas sequentially enters the lower tank 51 of rotational flow settlement tank 50, due to the central axial alignment sidewall of the exhaust opening of lower tank 51, and And the difference in height of the water level of lower tank 51 and central shaft is at ± 4cm, therefore flue gas drives water along sidewall when spraying described smoke exhaust pipe 49 Rotating, simultaneously containing under the effect of CaO in water, granule foreign and element sulphur in flue gas are removed, then through upper tank body 52 Again acting on, granule foreign and element sulphur in flue gas are efficiently removed, and the most processed flue gas drains into described convection current dedusting dress Put 60.
Flue gas vertically sprays in the water tank 61 in described convection current dust arrester 60 via smoke exhaust pipe 521, and flue gas is by water tank 61 surrounding Stop and condensation tube recoil above water tank 61, then with the flue gas sprayed smoke exhaust pipe 521 or communicating pipe 69 in condensation tube fierce Head-on collision, makes the oil reservoir being wrapped in dust surface be peeled off, the cigarette so that dust is able to quick submerged, after processing Gas is discharged in described column for smoke purification 70 again.
Flue gas enters after column for smoke purification 70, if after sequentially passing through described clean cigarette dish 72, and clean due on clean cigarette dish 72 Under the effect of formed material, after the flue dust in flue gas is blocked again, warp is drained into described fume high-temperature process tank by described smoke exhaust pipe 90 In 15, due to the effect of scattered chimney 140, the heat in combustor is led in described fume high-temperature process tank 15 so that cigarette Temperature in upward adverse flow of QI temperature process tank 15 is the highest, it is sufficient to by the toxic gas in flue gas, after two scruple solutions then concentration is low, Free of contamination air-flow is discharged via described chimney 16.
The present invention has following effective effect:
1. it is provided with stock guide and grille door bottom the drying chamber of incinerator, burning in percolate flowing in combustion chamber can be made, anti- Only poisonous and harmful liquid is the most excessive, pollutes;Grille door can also make the heat radiation of the rubbish burnt generation directly to not The rubbish of burning carries out high-temperature baking, removes moisture removal, garbage drying, gets ready for next round burning.
2. the igniting chamber in incinerator, flue gas recirculation room and scattered chimney are under the promotion of thermal current, form flue gas turbulent flow, make combustor Interior flue gas is quickly spread, it is ensured that rubbish can fully burn, and rubbish burns rubbish, it is not necessary to add any oxidizer, rubbish Processing cost reduces.
3. dust catching case, tar processing room, rotational flow settlement tank, convection current dust arrester, the employing of purifying column, effectively eliminate cigarette Various impurity in gas, make flue gas reach " zero smog " discharge.
4. fume high-temperature process tank is arranged on the top of combustor, and fume high-temperature process tank is directly toasted by the heat radiation of combustor, The temperature in fume high-temperature process tank tank is made to reach more than 1000 °, it is simple to two English produced when removing waste incineration.
Described above is the detailed description for the preferable possible embodiments of the present invention, but embodiment is not limited to the special of the present invention Profit application range, the equal change completed under the technical spirit suggested by all present invention or modification change, the present invention all should be belonged to Contained the scope of the claims.

Claims (10)

1. a tar processing room, includes process casing, it is characterised in that: described tar processing room also includes some first Water-cooling wall and some second water-cooling walls, be provided with dividing plate, and include relative top board and base plate in described treatment box body, described Described process casing is divided into upper box and lower box by dividing plate, and described process casing is provided with an exhaust structure, and described convulsion is tied The pipe of structure can stretch into described lower box, described upper box and described lower box by communicating pipe even after described upper box Logical;
Described some first water-cooling walls are separately mounted in described lower box, and top is connected with described dividing plate, bottom and the described end Plate connects, and the bottom of each first water-cooling wall offers breach, and has the first passage corresponding breach is opened above, adjacent The position of the first passage of the first water-cooling wall is crisscross arranged, and the water level in described lower box is higher than described breach, less than described the One passage;The top of described some first water-cooling walls is respectively facing described pipe lopsidedness;
Described some second water-cooling walls are separately mounted in described upper box, and top is connected with described top board, bottom with described every Plate connects, and the bottom of each second water-cooling wall offers breach, and has the second passage, institute corresponding breach is opened above The water level stating upper box is higher than described breach, less than described second passage;The top of described some second water-cooling walls is respectively facing Described connecting tube tilts;
Described exhaust structure in order to be evacuated to described lower box by heat smoke, and heat smoke sequentially passes through after some first water-cooling walls by described Communicating pipe enters described upper box, and heat smoke discharges described process casing after sequentially passing through some second water-cooling walls.
2. tar processing room as claimed in claim 1, it is characterised in that: each first water-cooling wall and the smoke of described pipe The angle of the central shaft of mouth is 25-35 °.
3. tar processing room as claimed in claim 2, it is characterised in that: each first water-cooling wall and the smoke of described pipe The angle of the central shaft of mouth is 30 °.
4. tar processing room as claimed in claim 2, it is characterised in that: each first water-cooling wall and the smoke of described pipe The angle of the central shaft of mouth is 50-80cm.
5. tar processing room as claimed in claim 2, it is characterised in that: the be sequentially connected with on described some second water-cooling walls Two passages are on the straight line being parallel to described dividing plate.
6. tar processing room as claimed in claim 5, it is characterised in that: each second water-cooling wall and the center of described communicating pipe Angle between axle is 25-35 °.
7. tar processing room as claimed in claim 6, it is characterised in that: each second water-cooling wall and the center of described communicating pipe Angle between axle is 30 °.
8. a non smoke refuse burning system, it is characterised in that: described non smoke refuse burning system includes incinerator, powder Dirt intercepts case, tar processing room, spun down tank, convection current dust arrester and column for smoke purification;Described incinerator and described dust Interception case connects, and described dust catching case is connected with described tar processing room by an exhaust structure;
Described tar processing room also includes some first water-cooling walls and some second water-cooling walls, be provided with in described treatment box body every Plate, and include relative top board and base plate, described process casing is divided into upper box and lower box, described process by described dividing plate Being provided with an exhaust structure on casing, the pipe of described exhaust structure can stretch into described lower box after described upper box, Described upper box and described lower box were connected by communicating pipe;
Described some first water-cooling walls are separately mounted in described lower box, and top is connected with described dividing plate, bottom and the described end Plate connects, and the bottom of each first water-cooling wall offers breach, and has the first passage corresponding breach is opened above, adjacent The position of the first passage of the first water-cooling wall is crisscross arranged, and the water level in described lower box is higher than described breach, less than described the One passage;The top of described some first water-cooling walls is respectively facing described pipe lopsidedness;
Described some second water-cooling walls are separately mounted in described upper box, and top is connected with described top board, bottom with described every Plate connects, and the bottom of each second water-cooling wall offers breach, and has the second passage, institute corresponding breach is opened above The water level stating upper box is higher than described breach, less than described second passage;The top of described some second water-cooling walls is respectively facing Described connecting tube tilts;
Described exhaust structure in order to be evacuated to described lower box by heat smoke, and heat smoke sequentially passes through after some first water-cooling walls by described Communicating pipe enters described upper box, and heat smoke is discharged described process casing and sunk to described eddy flow after sequentially passing through some second water-cooling walls Fall tank;
Described rotational flow settlement tank connects described convection current dust arrester, and described convection current dust arrester connects described column for smoke purification, described Column for smoke purification connects described incinerator by another smoke exhaust pipe.
9. non smoke refuse burning system as claimed in claim 8, it is characterised in that: each first water-cooling wall and described smoke The angle of the central shaft of the outlet flue of pipe is 25-35 °.
10. non smoke refuse burning system as claimed in claim 8, it is characterised in that: each second water-cooling wall is with described Angle between the central shaft of communicating pipe is 25-35 °.
CN201610522698.2A 2016-07-04 2016-07-04 A kind of tar processing room and non smoke refuse burning system Active CN105927984B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610522698.2A CN105927984B (en) 2016-07-04 2016-07-04 A kind of tar processing room and non smoke refuse burning system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610522698.2A CN105927984B (en) 2016-07-04 2016-07-04 A kind of tar processing room and non smoke refuse burning system

Publications (2)

Publication Number Publication Date
CN105927984A true CN105927984A (en) 2016-09-07
CN105927984B CN105927984B (en) 2018-07-20

Family

ID=56827084

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610522698.2A Active CN105927984B (en) 2016-07-04 2016-07-04 A kind of tar processing room and non smoke refuse burning system

Country Status (1)

Country Link
CN (1) CN105927984B (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108031219A (en) * 2017-11-17 2018-05-15 广西瑞航工程咨询有限公司 A kind of waste incinerator with filtration
CN108050524A (en) * 2017-11-17 2018-05-18 广西瑞航工程咨询有限公司 A kind of incinerator with sedimentation basin
CN108072037A (en) * 2017-11-29 2018-05-25 广西南宁市武鸣广喜环保设备有限公司 A kind of domestic garbage treating system
CN108072036A (en) * 2017-11-29 2018-05-25 广西南宁市武鸣广喜环保设备有限公司 A kind of incineration firing equipment
CN108087887A (en) * 2017-11-29 2018-05-29 广西南宁市武鸣广喜环保设备有限公司 A kind of refuse treatment plant with dryer
CN108087888A (en) * 2017-11-17 2018-05-29 广西瑞航工程咨询有限公司 A kind of incinerator with screen pipe
CN108105774A (en) * 2017-11-29 2018-06-01 广西南宁市武鸣广喜环保设备有限公司 A kind of refuse disposal system using deodorant

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003139320A (en) * 2001-10-31 2003-05-14 Masayoshi Nishio Dust removal device for incinerator
CN2566931Y (en) * 2002-08-09 2003-08-20 武绍之 Multifunction oil fume separating apparatus
CN204261547U (en) * 2014-11-14 2015-04-15 合肥环坤污泥干化设备有限公司 Incinerator smoke cleaning system
CN105344192A (en) * 2015-11-05 2016-02-24 无锡新人居科贸有限公司 Recyclable waste gas treatment device
CN205860034U (en) * 2016-07-04 2017-01-04 陈仕敏 A kind of tar processing room and non smoke refuse burning system

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003139320A (en) * 2001-10-31 2003-05-14 Masayoshi Nishio Dust removal device for incinerator
CN2566931Y (en) * 2002-08-09 2003-08-20 武绍之 Multifunction oil fume separating apparatus
CN204261547U (en) * 2014-11-14 2015-04-15 合肥环坤污泥干化设备有限公司 Incinerator smoke cleaning system
CN105344192A (en) * 2015-11-05 2016-02-24 无锡新人居科贸有限公司 Recyclable waste gas treatment device
CN205860034U (en) * 2016-07-04 2017-01-04 陈仕敏 A kind of tar processing room and non smoke refuse burning system

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108031219A (en) * 2017-11-17 2018-05-15 广西瑞航工程咨询有限公司 A kind of waste incinerator with filtration
CN108050524A (en) * 2017-11-17 2018-05-18 广西瑞航工程咨询有限公司 A kind of incinerator with sedimentation basin
CN108087888A (en) * 2017-11-17 2018-05-29 广西瑞航工程咨询有限公司 A kind of incinerator with screen pipe
CN108072037A (en) * 2017-11-29 2018-05-25 广西南宁市武鸣广喜环保设备有限公司 A kind of domestic garbage treating system
CN108072036A (en) * 2017-11-29 2018-05-25 广西南宁市武鸣广喜环保设备有限公司 A kind of incineration firing equipment
CN108087887A (en) * 2017-11-29 2018-05-29 广西南宁市武鸣广喜环保设备有限公司 A kind of refuse treatment plant with dryer
CN108105774A (en) * 2017-11-29 2018-06-01 广西南宁市武鸣广喜环保设备有限公司 A kind of refuse disposal system using deodorant

Also Published As

Publication number Publication date
CN105927984B (en) 2018-07-20

Similar Documents

Publication Publication Date Title
CN103363531B (en) A kind of dangerous waste incinerator complexes
CN105674284B (en) A kind of vertical pyrolysis gasification furnace
CN206222331U (en) A kind of domestic garbage disposer
CN104588402B (en) A kind of solid waste harmless treatment device and method
CN102703121B (en) Biomass gas generation system
US20080257236A1 (en) Smokeless furnace
CN202024338U (en) Garbage incinerator and flue-gas purification treatment device allowing zero dioxin discharge
CN100473902C (en) Incineration equipment system of rotary kiln for hazardous waste garbage
CN102889599B (en) Wet sewage sludge combustion furnace
CN205481003U (en) Processing system is discharged in industrial waste's environmental protection
CN204448794U (en) A kind of solid waste harmless treatment device
CN104891769B (en) Sludge drying and incineration system and method
CN105114955B (en) The preparation method of rotary kiln type continuous carbonization incinerator for thermal decomposition
CN200979174Y (en) Multiple combustion zero-discharge gas-firing fuel oil-firing device
CN102679364B (en) Household garbage treatment system
CN100565009C (en) Can realize the garbage burning processing method and the device of dioxin and dust zero discharge
CN207569881U (en) A kind of environment-friendly type burns purification furnace
CN106224974B (en) Waste incineration processing system
CN103256608B (en) sludge incineration method
CN105465790B (en) The environment protection emission processing system of trade waste
CN102042601A (en) Small efficient medicinal rubbish pyrolysis incinerator
CN207081009U (en) A kind of residents in rural community pyrolysis gasification system
CN105757673A (en) Small-scale efficient domestic garbage gasification incineration system and incineration method
CN205388313U (en) Processing system is discharged in industry solid waste's environmental protection
CN101368732B (en) Refuse incineration processing equipment and method

Legal Events

Date Code Title Description
PB01 Publication
C06 Publication
SE01 Entry into force of request for substantive examination
C10 Entry into substantive examination
GR01 Patent grant
GR01 Patent grant