CN106224969A - Stoker fired grate formula refuse gasification CIU and vortex burner - Google Patents
Stoker fired grate formula refuse gasification CIU and vortex burner Download PDFInfo
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- CN106224969A CN106224969A CN201610801164.3A CN201610801164A CN106224969A CN 106224969 A CN106224969 A CN 106224969A CN 201610801164 A CN201610801164 A CN 201610801164A CN 106224969 A CN106224969 A CN 106224969A
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- flue
- gasification furnace
- incinerator
- vortex burner
- flue gas
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/02—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
- F23G5/027—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage
- F23G5/0276—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage using direct heating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D45/00—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
- B01D45/02—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising gravity
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D45/00—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
- B01D45/12—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces
- B01D45/16—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces generated by the winding course of the gas stream, the centrifugal forces being generated solely or partly by mechanical means, e.g. fixed swirl vanes
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN A CARRIER GAS OR AIR
- F23C7/00—Combustion apparatus characterised by arrangements for air supply
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/02—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
- F23G5/04—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment drying
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/08—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating
- F23G5/14—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating including secondary combustion
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/44—Details; Accessories
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/44—Details; Accessories
- F23G5/46—Recuperation of heat
-
- 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
- F23G5/50—Control or safety arrangements
-
- 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
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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
- F23J3/00—Removing solid residues from passages or chambers beyond the fire, e.g. from flues by soot blowers
- F23J3/02—Cleaning furnace tubes; Cleaning flues or chimneys
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23L—SUPPLYING AIR OR NON-COMBUSTIBLE LIQUIDS OR GASES TO COMBUSTION APPARATUS IN GENERAL ; VALVES OR DAMPERS SPECIALLY ADAPTED FOR CONTROLLING AIR SUPPLY OR DRAUGHT IN COMBUSTION APPARATUS; INDUCING DRAUGHT IN COMBUSTION APPARATUS; TOPS FOR CHIMNEYS OR VENTILATING SHAFTS; TERMINALS FOR FLUES
- F23L9/00—Passages or apertures for delivering secondary air for completing combustion of fuel
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Incineration Of Waste (AREA)
Abstract
The invention discloses a kind of stoker fired grate formula refuse gasification CIU and vortex burner, the inner chamber of vortex burner includes the taper slag notch arranged from top to bottom, burning gallery, V cone passage and the ring smoke passage arranged from top to bottom around V cone passage, annular vent flue, the lower end edge tangentially-arranged vortex burner entrance of burning gallery sidewall, the breathing area of ring smoke passage tapers into from top to bottom, the upper end of ring smoke passage connects with the upper end of V cone passage, arrange tangential outlet flue on the sidewall of vortex burner to connect with annular vent flue, the lower end of annular vent flue sets annular cinder-discharging port.Use this vortex burner, there is higher efficiency of dust collection and efficiency of combustion, higher heat recovery efficiency, it is possible to realize controlled burning and controlled collection, reduce thermal losses, and pollutant emission can be efficiently reduced.
Description
Technical field
The invention belongs to solid waste incineration processing technology field, particularly relate to a kind of stoker fired grate formula refuse gasification and burn
Burning system and vortex burner.
Background technology
Existing technology of garbage disposal mainly has burning, sanitary landfills, compost, waste recovery etc..Conventional in garbage disposal
In technology, it is obvious that burning disposal has reduced training, innoxious thoroughly, occupation of land amount is little, and waste heat energy is obtained by, and secondary pollution is few
Etc. advantage, meet the strategic requirement of China's sustainable development.But along with both at home and abroad environmental requirement being improved constantly, how to strengthen
Control to secondary pollution is particularly important.Therefore, refuse pyrolysis gasification burning technology is gradually shifted onto the road of industrial applications
On, primarily now using all kinds of incineration technology especially for domestic rubbish, the industrialization widely of gasification burning technology will
The technological innovation bringing domestic garbage disposal industry is regenerated.
For many years, China's scientific research to the gasification burning technology such as biomass, rubbish, it is in progress a lot of, the base of laboratory
Plinth research is a lot, also has applied research, such as: rotary kiln type, the vertical and destructive gasifying of fluidized bed type or temperature gasification and high melt skill
Art etc..But Technique Popularizing application is upper or there is a definite limitation, raw material type, garbage treatment quantity, secondary pollution control and economical
Benefits etc. are principal elements.
In existing burning process and equipment, fire grate type incinerator is various informative, and its application accounts for whole world waste incineration
More than the 80% of the total market size, wherein has and uses mechanical type backstepping fire grate, forwards fire grate or combined fire grate in body of heater, also adopt
With the fire grate such as chain-plate type and drum-type.
In sum, typical incinerator, it is respectively arranged with himself advantage, but needs solution in the actual application of China
Problem and shortage:
1., for characteristics such as China's house refuse water content height, complicated components, the technology of moving hearth uses, to rubbish
Conveying capacity needs emphasis to consider.
2. being on the increase along with refuse production, sanitary fill such as mountain, garbage treatment quantity must be effectively improved,
Could meeting the market requirement.
3., in the face of strict pollutant emission requirement, secondary pollution controls the key problem being technically need to solve.
4., in order to effectively increase economic efficiency, in rubbish heat treatment process, the organic efficiency of heat needs to improve.Existing
Rubbish heat treatment technics generally use boiler to produce steam to shift steam turbine power generation onto, whole transition heat efficiency losses is relatively big, place
Manage identical quantity of refuse, relatively reduce thermal losses and raising heat exchanger effectiveness just can improve the thermal efficiency.
5. during conventional garbage burns mode and boiler applications, high-temperature dust removal is less or does not has, and some efficiency is the most not high enough, high
It is less that effect dedusting and burning are had both, and the easy dust stratification of boiler makes thermal conversion efficiency decline, thus lower power production, maintenance period is short
Deng.
Existing incinerator such as following two patent of invention: multiple row sectional drive combined type domestic garbage incinerator
(ZL200710092508.9) an open question and in two-stage garbage incinerator (ZL201010268376.2): at rubbish heat
Reason model comparision falls behind, and be simply dried-burns-burns, the process of solid combustion release heat；In stove, thermal chemical reaction is with oxidation
Reaction is main, and reduction reaction assists, and is easily generated secondary pollution；When rubbish burns in stove, cross oxygen quotient big, First air, two
Secondary wind infeed amount is big, and in flue gas, dust content is higher, affects heat reclaiming system and smoke processing system relatively big, easily amasss
Ash, exhaust gas volumn is relatively big, reduces thermal conversion efficiency；The gasification furnace not being separately provided and incinerator, can only process rubbish by several times,
Cannot realize large-scale rubbish continuous gasification burning disposal, garbage treatment quantity is less.
Summary of the invention
It is an object of the invention to overcome the deficiencies in the prior art, it is provided that a kind of stoker fired grate formula refuse gasification CIU
And vortex burner, vortex burner efficiency of dust collection, efficiency of combustion are higher, it is possible to reducing thermal losses, the organic efficiency of heat is relatively
Height, and pollutant emission can be efficiently reduced.
The object of the present invention is achieved like this:
A kind of vortex burner, the top board of described vortex burner arranges combustion chamber ignition combustion-supporting hole, and described whirlwind fires
Taper slag notch that the inner chamber of burner includes setting gradually from top to bottom, burning gallery, V cone passage and around V cone passage from
The ring smoke passage that top to bottm sets gradually, annular vent flue, described taper slag notch is up big and down small, described burning gallery
The lower end edge tangentially-arranged vortex burner entrance of sidewall, the sidewall of described burning gallery arranges some combustion airs and supplies air port,
Described each combustion air is respectively positioned on the top of vortex burner entrance, described ring smoke passage, annular vent flue and V for air port
Cone passage between by annular inducing QI pier separate, described V bore passage up big and down small, the breathing area of described ring smoke passage from
Top to bottm tapering into, the upper end of described ring smoke passage connects, under described ring smoke passage with the upper end of V cone passage
End connects with the upper end of annular vent flue, and the sidewall of described vortex burner arranges tangential outlet flue and annular vent flue
Connection, the lower end of described annular vent flue arranges annular cinder-discharging port.
Preferably, the bottom of described ring smoke passage is circumferentially arranged some point gas piers wide at the top and narrow at the bottom, adjacent on
Up-narrow and down-wide flue gas ring road is formed between point gas pier narrow under width.
Preferably, described vortex burner entrance is connected to feed the high-temperature flue of high-temperature flue gas, described high-temperature flue
On smoke movement parameter acquisition unit is set, described vortex burner entrance arranges variable synthesis gas approach, and described flue gas is transported
Dynamic parameter acquisition unit includes that sensing receives and signal processing unit, cooling unit, heat insulation pedestal and sensing element, described heat insulation
Pedestal is fixed on the tube wall of high-temperature flue, and described sensing element is fixed on heat insulation base along the direction being perpendicular to high-temperature flue axis
On seat, the measurement end of sensing element stretches in high-temperature flue, and described sensing receives and signal processing unit is fixed on sensing element
The one end being positioned at outside high-temperature flue, sensing receives and signal processing unit records the flue gas stream in high-temperature flue by sensing element
Amount, flow velocity, described cooling unit be enclosed in sensing element heat insulation pedestal, sensing receive and signal processing unit between one
Duan Shang, described variable synthesis gas approach includes actuator, fire-resistant bore adjustment seat, one end of described fire-resistant bore adjustment seat
Stretching in vortex burner entrance, the other end connects actuator, also includes the first flue gas composition detection device and control unit,
Described first flue gas composition detection device is arranged on high-temperature flue the flue gas composition in detecting high-temperature flue, described control
Unit electrically connects with the first flue gas composition detection device, sensing reception and signal processing unit, actuator respectively, control unit
Process smoke movement parameter, synthesis flue gas composition parameter, and stretching by actuating mechanism controls fire-resistant bore adjustment seat, and then
Control the pore size of variable synthesis gas approach.
Preferably, described variable synthesis gas approach also includes that fireproof flue, heat-insulating and sealing, compression thermal insulation layer, high temperature are close
Envelope, the cross section of described fireproof flue is U-shaped, and the opening of fireproof flue seals by compressing thermal insulation layer, and described fire-resistant bore is adjusted
Joint seat stretches in fireproof flue through compressing thermal insulation layer, and described fire-resistant bore conditioned seat width of one end in fireproof flue is big
In fire-resistant bore conditioned seat in the width of the outer one end of fireproof flue, arrange between fire-resistant bore adjustment seat and fireproof flue sidewall
Elevated-temperature seal, arranges heat-insulating and sealing between fire-resistant bore adjustment seat and compression thermal insulation layer.
A kind of stoker fired grate formula refuse gasification CIU, including incinerator, described incinerator includes grate,
And feed hopper, gasification furnace and the incinerator set gradually along feedstock direction on grate, the rear of gasification furnace is gasification furnace
Fall cinder notch, and incinerator is positioned at gasification furnace and falls the front lower place of cinder notch, and the rear of incinerator is the slag notch of incinerator, on described grate
Being provided with garbage pusher device, described garbage pusher device is positioned at the lower section of feed hopper, for the rubbish in feed hopper is pushed gasification furnace
In, being respectively arranged below with at least one and be independently arranged once of the lower section of gasification furnace moving hearth and incinerator moving hearth
Air compartment, is provided with windrow seal section between described feed hopper, gasification furnace, the grate part between described gasification furnace and incinerator is stayed
Having transition to fall slag section, the described transition slag section that falls is provided with residue pusher, for being pushed by the rubbish residue fallen in gasification furnace
In incinerator；
Described gasification furnace, incinerator include furnace shell, moving hearth respectively, and the forward and backward side of described gasification furnace passes through heap respectively
Material seal section, the transition slag section that falls seals, and described transition falls slag section isolation gasification furnace, incinerator, makes gasification furnace, incinerator the most only
Vertical；
Described gasification furnace, incinerator, respectively in the shape that arches upward, the face arch of described gasification furnace, rear arch are respectively provided with secondary air feed
Mouthful, the vault of described gasification furnace arranges the first exhanst gas outlet, and the vault of described incinerator arranges the second exhanst gas outlet, described gasification
Igniting combustion supporting hole it is respectively equipped with on stove, incinerator；
Also include vortex burner, described vortex burner entrance and the connection of the first exhanst gas outlet；
Also including circulating air feed system, described circulation air feed system includes dust arrester, the first blower fan, the second blower fan, institute
Stating the inlet end of dust arrester to be connected with the second exhanst gas outlet by pipeline, pipeline and the is passed through in the outlet side of described dust arrester
The inlet end of one blower fan connects, and the outlet side of described first blower fan connects the house steward of the first manifold, the arm of described first manifold
Connect for air port with the secondary on each air compartment of the lower section of gasification furnace moving hearth and gasification furnace face arch, rear arch respectively,
The first regulation valve it is respectively provided with on each arm of described first manifold, the air inlet of described second blower fan and atmosphere, described
The gas outlet of the second blower fan connects the house steward of the second manifold, the arm of described second manifold respectively with incinerator moving hearth below
Each air compartment and the inlet end of dust arrester, outlet side connection, each arm of described second manifold is respectively provided with the
Two regulation valves, also include that the 3rd manifold, the described house steward of the 3rd manifold connect with the gas outlet of the second blower fan, described 3rd manifold
Each arm connect for air port with each combustion air respectively, each arm of the 3rd manifold is respectively provided with the 3rd and regulates valve.
Preferably, described first manifold also has an arm being connected with vortex burner entrance, and this arm is provided with
Corresponding regulation valve, the remainder flue gas not utilized of the first blower fan extraction is injected into rotation by vortex burner entrance
Wind combustor, and by corresponding regulation valve regulation wind supply quantity.
Preferably, the arm that described first manifold is connected with vortex burner entrance be provided with flue gas amount detecting device,
Two flue gas composition detection devices, described flue gas amount detecting device, the second flue gas composition detection device and the 3rd regulation valve are respectively
Electrically connect with control unit, described control unit process second flue gas composition detection device gather synthesis flue gas composition parameter with
And the synthesis flue gas flow parameter that flue gas amount detecting device gathers, and by the 3rd governor valve control combustion air wind supply quantity.
High-temperature flue gas in order to effectively discharge incinerator carries out dedusting, it is preferable that described dust arrester is that whirlwind divides
From device or hot precipitator；Described first blower fan is high-temperature blower, is beneficial to work in high temperature environments, and described second blower fan is
Aerator.
In order to prevent altering wind between gasification furnace, incinerator, it is preferable that described transition fall be provided with in slag section to be opened/closed every
From door, described isolating door is for cutting off gasification furnace, incinerator.
In order to preferably adapt to the installing space in factory, it is preferable that the face arch of described gasification furnace is flat construction, or
Person, the face arch of gasification furnace is that rear end is inclined upwardly structure.
Owing to have employed technique scheme, there is advantages that
After described vortex burner synthesis flue gas tangentially enters, mix with the oxygen supply of combustion air and burn in the combustion channel,
Flue gas rotates and is advanced into V cone passage, and through annular inducing QI pier shunting, flying dust sedimentation falls into taper slag notch, and high-temperature flue gas is walked around
Annular inducing QI pier enters ring smoke passage, then enters the discharge of annular vent flue through flue gas ring road.Flue gas is up, and flying dust is conducted oneself with dignity
Sedimentation, and V cone passage under little upper greatly, volume increase, pressure reduce, flow velocity reduce, add cyclone centrifugal power effect, promote further
Enter flying dust sedimentation；Ring smoke passage flue gas size is gradually reduced, and detours, and velocity of flue gas reduces, and enters trapezoidal flue gas ring road,
Reducing the sucking-off of flying dust, dedusting is more favourable, and in annular vent flue, dust stratification is discharged by the cinder-discharging port that annular is uniform.Due to annular cigarette
The pyramidal structure of gas passage, the least the closer to discharge area, trapezoidal flue gas ring road makes high-temperature flue gas stream in ring smoke passage
Speed is uniformly.Vertically section cyclonic separation dedusting, V cone passage, ring smoke passage, ring road arranges combination and flying dust deadweight raising removes
Dirt efficiency, synthesizes flue gas and obtains being sufficiently mixed burning, improve efficiency of combustion during dedusting.
Control unit processes smoke movement parameter (speed, flow, fluid force etc.), synthesis flue gas composition and high-temperature blower and goes out
Mouth arrives flue gas composition and the flow of vortex burner, controls actuator regulation gas approach aperture, controls combustion air simultaneously
Amount, it is achieved the regulation that synthesis exhaust gas volumn that in waste component and heat treatment process, unstability is brought and component etc. fluctuate,
Thus control smoke inlet initial velocity and combustion-supporting oxygen-supplying amount well, to reach the purpose of high-effective dust-removing and burning.Control unit controls
Variable synthesis gas approach actuator: purely mechanic transmission, mechanical parameter enlarger, then drive actuator, execution efficiency
Higher.
Aerator blasts air and provides First air for incinerator and provide homoiothermic air feed for cyclone separator, high-temperature blower,
By the second regulation valve regulation wind supply quantity on corresponding pipeline, incinerator residue is made fully to burn；Then, high-temperature blower extraction combustion
The flue gas of cinder stove, after homoiothermic and cyclone collection flying dust, forms the flue gas supply gasification furnace of certain pressure once
Wind and secondary wind, by the first regulation valve regulation wind supply quantity on corresponding pipeline, in making gasification furnace, rubbish produces gasification, containing one
The quantitatively flue gas of synthesis gas, discharges from the first exhanst gas outlet, enters vortex burner processing links, and vortex burner provides high temperature
Flue gas.Present inventive concept is novel, and garbage treatment quantity is big, and the rubbish bed of material experiences dry, gasification and the combustion of residue on stoker fired grate
In the cinder stage, adapt to the characteristics such as China's house refuse water content height, complicated component, improve the energy in garbage processing procedure and convert
Pollutant discharge amount in efficiency and reduction flue gas, effectively prevents secondary pollution, and is capable of large-scale rubbish continuous gasification
Burning disposal, it is ensured that refuse gasification burns effect and lime-ash clinker ignition loss, relatively reduces thermal losses and improves heat exchanger effectiveness, carrying
The high thermal efficiency.
Gasification furnace, incinerator are provided separately, and the vault of gasification furnace arranges the first exhanst gas outlet, and the vault of incinerator arranges
Two exhanst gas outlets, are beneficial to process flue gas respectively according to the difference of flue gas quality, are conducive to flue gas ash removal, it is provided that more simultaneously
The flue gas of high-quality, the utilization rate making flue gas is higher, and the waste residue of discharge is less.
Accompanying drawing explanation
Fig. 1 is the structural representation of vortex burner；
Fig. 2 is the structural representation of smoke movement parameter acquisition unit；
Fig. 3 is the A-A cross-sectional schematic of Fig. 1；
Fig. 4 is the B-B cross-sectional schematic of Fig. 1；
Fig. 5 is the C-C cross-sectional schematic of Fig. 4；
Fig. 6 is the structural representation of stoker fired grate formula refuse gasification CIU.
Reference
1 is incinerator, and 101 is grate, and 102 is feed hopper, and 103 is gasification furnace, and 104 is incinerator, and 105 is stove
Bed, 106 is garbage pusher device, and 107 is an air compartment, and 108 is windrow seal section, and 109 fall slag section for transition, and 110 push away for residue
Glassware, 111 is isolating door, and 112 is the first exhanst gas outlet, and 113 is the second exhanst gas outlet, and 114 is igniting combustion supporting hole, and 115 is two
Secondary for air port, 116 is slag notch, and 117 is the cinder notch that falls；
2 is circulation air feed system, and 201 is dust arrester, and 202 is the first blower fan, and 203 is the second blower fan, and 204 is the first discrimination
Pipe, 205 is the second manifold, and 206 is the 3rd manifold, and 207 is the first regulation valve, and 208 is the second regulation valve, and 209 is the 3rd regulation
Valve；
3 is vortex burner, and 301 is combustion chamber ignition combustion-supporting hole, and 302 is taper slag notch, and 303 enter for vortex burner
Mouthful, 304 is tangential outlet flue, and 305 supply air port for combustion air, and 306 is burning gallery, and 307 is that V bores passage, and 308 is ring smoke
Passage, 309 is annular cinder-discharging port, and 310 is annular vent flue, and 311 is annular inducing QI pier, and 312 is a point gas pier, and 313 is flue gas
Ring road, 314 is high-temperature flue, and 315 receive and signal processing unit for sensing, and 316 is cooling unit, and 317 is heat insulation pedestal,
318 is sensing element, and 319 is actuator, and 320 is fire-resistant bore adjustment seat, and 321 is the first flue gas composition detection device, 322
For control unit, 323 is fireproof flue, and 324 is heat-insulating and sealing, and 325 for compressing thermal insulation layer, and 326 is elevated-temperature seal, and 327 is cigarette
Gas amount detecting device, 328 is the second flue gas composition detection device.
Detailed description of the invention
See Fig. 1 to Fig. 5, for a kind of preferred embodiment of vortex burner,
A kind of vortex burner, the top board of described vortex burner arranges combustion chamber ignition combustion-supporting hole 301, described whirlwind
The inner chamber of burner includes taper slag notch 302, burning gallery 306, V cone passage 307 and the ring set gradually from top to bottom
Ring smoke passage 308, the annular vent flue 310 that passage 307 sets gradually from top to bottom, described taper slag notch is bored around V
302 is up big and down small, the lower end edge tangentially-arranged taper slag notch 303 of described burning gallery 306 sidewall, described burning gallery 306
Sidewall on some combustion airs are set for air port 305, described each combustion air is respectively positioned on the upper of taper slag notch 303 for air port 305
Side, is separated by annular inducing QI pier 311 between described annular vent flue 310, ring smoke passage 308 and V cone passage 307,
Described V cone passage 307 is up big and down small, and the breathing area of described ring smoke passage 308 tapers into from top to bottom, described annular
The bottom of exhaust gases passes 308 is circumferentially arranged some point gas piers 312 wide at the top and narrow at the bottom, adjacent point gas pier 312 wide at the top and narrow at the bottom
Between form up-narrow and down-wide flue gas ring road 313.The breathing area of described ring smoke passage 308 tapers into from top to bottom,
The upper end of described ring smoke passage 310 connects with the upper end of V cone passage 307, the sidewall of described vortex burner is arranged and cuts
Connecting with annular vent flue 310 to outlet flue 304, the lower end of described annular vent flue arranges annular cinder-discharging port.
Described vortex burner entrance 303 is connected to feed the high-temperature flue 314 of high-temperature flue gas, described high-temperature flue
Arranging smoke movement parameter acquisition unit on 314, described vortex burner entrance 303 arranges variable synthesis gas approach, described
Smoke movement parameter acquisition unit includes that sensing receives and signal processing unit 315, cooling unit 316, heat insulation pedestal 317 and sense
Answering element 318, described heat insulation pedestal 317 to be fixed on the tube wall of high-temperature flue 314, described sensing element 318 is along being perpendicular to height
The direction of temperature flue 314 axis is fixed on heat insulation pedestal 317, and the measurement end of sensing element 318 stretches in high-temperature flue 314,
Described sensing receives and signal processing unit 315 is fixed on one end that sensing element 318 is positioned at outside high-temperature flue 314, and sensing connects
Receive and signal processing unit 315 records the flue gas flow in high-temperature flue 314, flow velocity, described cooling list by sensing element 318
Unit 316 be enclosed in sensing element 318 heat insulation pedestal 317, sensing receive and signal processing unit 315 between one section on,
Described heat insulation pedestal 317, cooling unit 316 prevent the heat conduction of high-temperature flue 314 from receiving and signal processing unit to sensing
315.Described variable synthesis gas approach includes actuator 319, fire-resistant bore adjustment seat 320, and described actuator 319 can be adopted
With cylinder, oil cylinder etc..One end of described fire-resistant bore adjustment seat 320 is stretched in vortex burner entrance 303, and the other end connects to be held
Row mechanism 319, also includes the first flue gas composition detection device 321 and control unit 322, described first flue gas composition detection device
321 are arranged on the flue gas composition on high-temperature flue 314 in detecting high-temperature flue 314, and described control unit 322 is respectively with
One flue gas composition detection device 321, sensing reception and signal processing unit 315, actuator 319 electrically connect, control unit 322
Process smoke movement parameter, synthesis flue gas composition parameter, and control stretching of fire-resistant bore adjustment seat 320 by actuator 319
Contracting, and then control the pore size of variable synthesis gas approach.
In the present embodiment, described variable synthesis gas approach also include fireproof flue 323, heat-insulating and sealing 324, compress heat insulation
Layer 325, elevated-temperature seal 326, described fireproof flue 323, elevated-temperature seal 326 can use conventional exotic material to make, described every
Heat seal 324, compression thermal insulation layer 325 can use conventional heat-barrier material to make.The cross section of described fireproof flue 323 is U-shaped, resistance to
The opening of fire flue 323 seals by compressing thermal insulation layer 325, and described fire-resistant bore adjustment seat 320 is stretched through compressing thermal insulation layer 325
Entering in fireproof flue 323, described fire-resistant bore adjustment seat 320 is positioned at the width of fireproof flue 323 one end more than fire-resistant bore
Adjustment seat 320 is positioned at the width of the outer one end of fireproof flue 323, sets between fire-resistant bore adjustment seat 320 and fireproof flue 323 sidewall
Put elevated-temperature seal 326, between fire-resistant bore adjustment seat 320 and compression thermal insulation layer 325, heat-insulating and sealing 324 is set.
See Fig. 6, for a kind of preferred embodiment of stoker fired grate formula refuse gasification CIU, including incinerator
1, described incinerator 1 includes grate 101, and set gradually along feedstock direction on grate 101 feed hopper 102, gas
Changing stove 103 and incinerator 104, the rear of incinerator 104 is the slag notch of incinerator 104, and gasification furnace 103 is mainly to rubbish
Carbon-containing part gasifies, and discharges flammable gasification flue gas and rubbish residue, and incinerator 104 is substantially carried out at the burning of carbon residue
Reason, and discharge innoxious lime-ash.The siege 105 of gasification furnace 103 and incinerator 104 all uses the mechanical kiln that segmentation independently drives
Row's formula moving hearth 105, the fire grate of stoker fired grate formula moving hearth 105 is by weight before and after moving grate plate and fixed grate plate
Folded, collect alternately and form, adjacent many groups moving grate plate is connected by pull bar, uses a set of driving means to drive.Machine
Tool grate-type moving hearth 105 is as the carrier of conveying garbage, and its embodiment can be all types of moving hearths 105, such as chain
Board-like, drum-type, multisection type fire grate system etc..
Described grate 101 is provided with garbage pusher device 106, and described garbage pusher device 106 is positioned at the lower section of feed hopper 102,
For the rubbish in feed hopper 102 is pushed in gasification furnace 103, the lower section of gasification furnace 103 moving hearth 105 and incinerator
104 moving hearths 105 be respectively arranged below with at least one air compartment 107 being independently arranged, in the present embodiment, with gasification furnace
The fire grate of air compartment 107 correspondence of 103 first halfs, driving means, as the dryer section of gasification furnace 103 siege 105, with gasification
The latter half of fire grate of air compartment 107 correspondence of stove 103, driving means are as the gasification section of gasification furnace 103 siege 105.Gasification
The dryer section of stove 103 siege 105, gasification section can be respectively adopted 1-2 independent air compartment 107 air feed, it is also possible to respectively
Use 3-4 independent air compartment 107 air feed.Certainly, fire grate, driving means and an air compartment 107 also can not be correspondingly arranged,
Preferably on regulation moving hearth 105, the bed of material moves and air distribution relation.Incinerator 104 can use 1-4 independent First air
Room 107 air feed, burns rear lime-ash and gets rid of from slag notch, enter next step treatment process.
Being provided with windrow seal section 108 between described feed hopper 102, gasification furnace 103, garbage pusher device 106 work enters at position
In windrow seal section 108, garbage raw material is put into from feed hopper 102 and is fallen, and garbage pusher device 106 retreats, then advances, the most
Secondary pusher forms windrow at windrow seal section 108, makes gasification furnace 103 entrance be in windrow sealing state, strengthens gasification furnace 103 close
Envelope effect, solves garbage pusher device 106 and the easy leakage problem of feed hopper 102.When needing complete prepurging to dispose all rubbish,
Garbage pusher device 106 forward impelling half stroke again, is pushed completely into rubbish in gasification furnace 103, makes gasification furnace 103 entrance lose
Windrow sealing effectiveness.Leave transition in grate 101 part between described gasification furnace 103 and incinerator 104 to fall slag section 109, institute
State the transition slag section 109 that falls and be provided with residue pusher 110, for the rubbish residue fallen in gasification furnace 103 is pushed incinerator
In 104, the transition slag section 109 that falls can be at windrow sealing state when piling up rubbish residue, strengthens gasification furnace 103 sealing effectiveness,
Solve to go here and there between gasification furnace 103, incinerator 104 problem of wind.In the present embodiment, described transition falls, and be provided with in slag section 109 can
The isolating door 111 of opening and closing, described isolating door 111 is for cutting off gasification furnace 103, incinerator 104.The furnace lifting initial stage or need control
When altering wind between gasification furnace 103 processed and incinerator, close isolating door 111, stack a certain amount of residue when the slag section that falls and form windrow
After sealing, isolating door 111 can be kept to open, the residue pusher 110 arranged with lower section is coordinated to use, continuous to realize rubbish
Gasification burning processes.
The upper end of described gasification furnace 103, incinerator 104 upper end respectively in the shape that arches upward, the face arch of described gasification furnace 103 is
Flat construction, or, the face arch of gasification furnace 103 is that rear end is inclined upwardly structure.The vault of described gasification furnace 103 arranges the first cigarette
Gas outlet 112, the vault of described incinerator 104 arranges the second exhanst gas outlet 113, the arching upward of described gasification furnace 103 upper end, burns
It is respectively equipped with igniting combustion supporting hole 114 on the arching upward of stove 104 upper end.Gasification flue gas is from first exhanst gas outlet the 112, second exhanst gas outlet
113 get rid of, and also include vortex burner 3, described vortex burner entrance and the connection of the first exhanst gas outlet.Gasification furnace 103 burner hearth
Space is compared with traditional incinerator, relatively reduced；Forward and backward arch position relative with moving hearth 105 diminishes, and decreases and burns
Burn the space that stove takies, be also easier to insulation, decrease the amount of leakage of heat, beneficially rubbish and fully gasify.Described gasification furnace
Secondary it is respectively provided with for air port 115 on the face arch of 103, rear arch.
Also including circulating air feed system 2, described circulation air feed system 2 includes dust arrester the 201, first blower fan 202, second
Blower fan 203, described dust arrester 201 is cyclone separator or hot precipitator, in the present embodiment, described dust arrester 201
For cyclone separator.Described first blower fan 202 is high-temperature blower, and described second blower fan 203 is aerator.Described dust arrester
The inlet end of 201 is connected by pipeline and the second exhanst gas outlet 113, and pipeline and the is passed through in the outlet side of described dust arrester 201
The inlet end of one blower fan 202 connects, and the outlet side of described first blower fan 202 connects the house steward of the first manifold 204, described first discrimination
The arm of pipe 204 respectively with each air compartment 107 of the lower section of gasification furnace 103 moving hearth 105 and gasification furnace 103 face arch,
Secondary on rear arch connects for air port 115, and each arm of described first manifold 204 is respectively provided with the first regulation valve 207, gasification
Stove 103 First air is that the flue gas generation certain pressure of high-temperature blower extraction incinerator 104 blasts the shifting of gasification furnace 103 stoker fired grate formula
In an air compartment 107 corresponding below dynamic siege 105, then by an air holes spray penetration rubbish on moving hearth 105, enter
Circulation of qi promoting, regulates wind supply quantity by the first regulation valve 207 on corresponding each arm.Gasification furnace 103 secondary wind is that high-temperature blower is taken out
Take incinerator 104 flue gas produce certain pressure blast gasification furnace 103 burner hearth, its spray-hole be arranged on gasification furnace 103 face arch and
On rear arch.Secondary it is provided with for air port 115, raising gasification efficiency, polymer substance decomposition in enhancing flue gas on forward and backward arch.After
Have igniting combustion supporting hole 114 on arch, furnace lifting, baker and in stablizing gasification furnace 103 temperature use, by the on corresponding each arm
One regulation valve 207 regulates wind supply quantity.The air inlet of described second blower fan 203 and atmosphere, the air that the second blower fan 203 blasts
Can be cold wind or the hot blast after heating.The gas outlet of described second blower fan 203 connects the house steward of the second manifold 205, institute
State the arm of the second manifold 205 respectively with incinerator 104 moving hearth 105 below each air compartment 107 and dust arrester
Inlet end, the outlet side of 201 connect, and each arm of described second manifold 205 is respectively provided with the second regulation valve 208.Incinerator
104 First air are that the air of certain pressure is blasted an air compartment corresponding below stoker fired grate formula moving hearth 105 by aerator
In 107, then by an air holes spray penetration residue on moving hearth 105, carry out residual burning, by corresponding each arm
First regulation valve 207 regulate wind supply quantity.The inlet end of dust arrester 201, the air intake of outlet side are homoiothermic air feed, homoiothermic air feed
It is that the air of certain pressure is blasted incinerator 104 and exports (i.e. cyclone inlet) and carry out homoiothermic, meanwhile, whirlwind by aerator
Separator outlet (i.e. high-temperature blower entrance) blasts further homoiothermic, is regulated by the first regulation valve 207 on corresponding each arm
Wind supply quantity.
Also including the 3rd manifold 206, the house steward of described 3rd manifold 206 connects with the gas outlet of the second blower fan 203, described
Each arm of the 3rd manifold 206 connects for air port 305 with each combustion air respectively, and each arm of the 3rd manifold 206 is respectively provided with
3rd regulation valve 209.Vortex burner entrance 303 and combustion-supporting confession air port are arranged in vortex burner 3 circumferential wall, permissible
Being that the flue gas in vortex burner 3 is longer with air mixture time, mixing is more uniformly distributed, and more fully burns.Cyclone firing
The combustion-supporting air feed of device 3 is that the air of certain pressure is blasted and combustion-supporting is injected into vortex burner 3, combustion-supporting air feed for air port by aerator
Approach axis can be radially or tangentially；Carry out syngas combustion.Meanwhile, the flue gas of high-temperature blower extraction incinerator 104 produces
Before certain pressure blasts an air compartment 107 corresponding below gasification furnace 103 stoker fired grate formula moving hearth 105 and gasification furnace 103,
Secondary air chamber on rear arch, described first manifold 204 also has an arm being connected with vortex burner smoke inlet, this
Pipe is provided with the regulation valve of correspondence.What high-temperature blower extracted has not utilized remainder flue gas, then by vortex burner 3 flue gas
Entrance is injected into vortex burner 3, carries out syngas combustion, and by corresponding regulation valve regulation wind supply quantity, this structure can
Reduce thermal losses and improve heat exchanger effectiveness, substantially increasing the organic efficiency of heat, and pollutant row can be efficiently reduced
High-volume.
Further, the arm that described first manifold is connected with vortex burner entrance is provided with flue gas amount detecting device
327, the second flue gas composition detection device 328, described flue gas amount detecting device, the second flue gas composition detection device and the 3rd are adjusted
Joint valve electrically connects with control unit respectively, and described control unit processes the synthesis flue gas group that the second flue gas composition detection device gathers
Divide the synthesis flue gas flow parameter that parameter and flue gas amount detecting device gather, and by the 3rd governor valve control combustion air air feed
Amount.
Described incinerator 104 is provided with cinder notch 117, and the slag notch 116 of described incinerator 104 is positioned at incinerator and falls cinder notch
The underface of 117, described in fall cinder notch 117 connected with the slag notch of dust arrester 201 by pipeline.This sealing structure is effective,
Can effectively hold minimizing pollutant discharge amount.
The waste disposal method of a kind of stoker fired grate formula refuse gasification CIU, the method sequentially includes the following steps:
Step A, closedown stoker fired grate formula refuse gasification incinerator 1 and the gate of atmospheric vent, start machinery grate-type rubbish
Rubbish incinerator 1, puts into feed hopper 102 by garbage raw material, and garbage pusher device 106 pusher back and forth will be from feed hopper 102
The garbage raw material fallen pushes the windrow seal section 108 between feed hopper 102, gasification furnace 103, makes windrow seal section 108 be formed
Windrow sealing state, unnecessary rubbish falls into the moving hearth 105 of gasification furnace 103, and the moving hearth 105 of gasification furnace 103 works,
Rubbish being conveyed into transition fall slag section 109, residue pusher 110 pusher back and forth, rubbish transition fallen in slag section 109 pushes away
Entering in incinerator 104, the moving hearth 105 of incinerator 104 works conveying garbage, until rubbish is at gasification furnace 103, incinerator
The moving hearth 105 of 104 is accumulated to required thickness: 0.6-0.8m, during baker, the rubbish piled up can protect mobile stove
Bed 105, prevents scaling loss siege 105.Stopping feeding intake to feed hopper 102, the moving hearth 105 of gasification furnace 103 and incinerator 104 stops
Only work, then, with start-up burner by the igniting combustion supporting hole 114 of gasification furnace 103 and incinerator 104 respectively with gasification furnace
103 and the burner hearth of incinerator 104 communicate, under the effect of start-up burner, gasification furnace 103 and incinerator 104 are carried out furnace lifting,
Baker, treats that this process stabilization completes, and makes gasification furnace 103 and incinerator 104 burner hearth reach predetermined temperature 600-700 DEG C；Baker
Purpose be the Natural Water in order to remove in lining and water of crystallization, in order to avoid rising too fast when going into operation due to furnace temperature, moisture content is a large amount of
Expansion causes body of heater spalling, bubbling or deforms even furnace wall and collapse, and affects intensity and the service life of heating furnace furnace wall.
Step B, startup regulation circulation air feed system 2, regulation gasification furnace 103, incinerator 104 and circulation air feed system 2
Technological parameter (pusher speed, fire grate speed, pathogenic wind-warm, blast and air quantity, secondary air temperature, blast and air quantity, furnace temperature,
Negative pressure, thickness of feed layer etc. in stove), feed intake to feed hopper 102, the moving hearth 105 of gasification furnace 103 works conveying garbage, rubbish
Proceeding by burning in the burner hearth of gasification furnace 103, rubbish residue is piled up formation windrow at transition falls slag section 109 and is sealed, and makes
The stove chamber inner combustion state temperature of gasification furnace 103 is stabilized to more than 850 DEG C, the moving hearth 105 work output combustion of incinerator 104
Rubbish residue after cinder.
Each technological parameter (pusher speed of step C, regulation gasification furnace 103, incinerator 104 and circulation air feed system 2
Negative pressure, thickness of feed layer in degree, fire grate speed, pathogenic wind-warm, blast and air quantity, secondary air temperature, blast and air quantity, furnace temperature, stove
Deng), rubbish is gradually gasified by gasification furnace 103, and gasification temperature is stable between 700-800 DEG C, makes the stable product of gasification furnace 103
The raw high-temperature flue gas containing 10%-20% synthesis gas, it is equal that gasification furnace 103 vaporized state stably carries out low temperature, middle temperature or high-temperature gasification
Can.Make incinerator 104 fired state temperature stabilization to more than 850 DEG C, it is achieved rubbish continuous gasification burning disposal；Need to regulate simultaneously
Each technological parameter of vortex burner 3, makes tangential outlet flue 304 temperature stabilization to more than 850 DEG C of vortex burner 3.
Step D, need to overhaul or during blowing out, stop feeding intake, regulation gasification furnace 103, incinerator 104 and circulation air feed system
The technological parameter of 2, makes gasification furnace 103 be gradually restored to fired state, after rubbish and rubbish residue burn, closes stoker fired grate
Formula refuse gasification incinerator 1 and circulation air feed system 2.Each technological parameter of vortex burner 3 need to be regulated simultaneously, make gasification furnace
103 are gradually restored to fired state.
Finally illustrate, preferred embodiment above only in order to technical scheme to be described and unrestricted, although logical
Cross above preferred embodiment the present invention to be described in detail, it is to be understood by those skilled in the art that can be
In form and it is made various change, without departing from claims of the present invention limited range in details.
Claims (10)
1. a vortex burner, it is characterised in that: combustion chamber ignition combustion-supporting hole, institute are set on the top board of described vortex burner
The inner chamber stating vortex burner includes that the taper slag notch set gradually from top to bottom, burning gallery, V bore passage and around V
Boring ring smoke passage, annular vent flue that passage sets gradually from top to bottom, described taper slag notch is up big and down small, described
The lower end edge tangentially-arranged vortex burner entrance of burning gallery sidewall, the sidewall of described burning gallery arranges some combustion airs
For air port, described each combustion air is respectively positioned on the top of vortex burner entrance, described ring smoke passage, annular vent for air port
Being separated by annular inducing QI pier between flue and V cone passage, described V cone passage is up big and down small, leading to of described ring smoke passage
Gas area tapers into from top to bottom, and the upper end of described ring smoke passage connects with the upper end of V cone passage, described ring smoke
The lower end of passage connects with the upper end of annular vent flue, and the sidewall of described vortex burner arranges tangential outlet flue and annular
Exhaust uptake connects, and the lower end of described annular vent flue arranges annular cinder-discharging port.
A kind of vortex burner the most according to claim 1, it is characterised in that: the bottom of described ring smoke passage is along week
To being provided with some point gas piers wide at the top and narrow at the bottom, between adjacent point gas pier wide at the top and narrow at the bottom, form up-narrow and down-wide flue gas ring road.
A kind of vortex burner the most according to claim 1, it is characterised in that: described vortex burner entrance is connected to
Feed the high-temperature flue of high-temperature flue gas, described high-temperature flue arranges smoke movement parameter acquisition unit, described vortex burner
Entrance arranges variable synthesis gas approach, described smoke movement parameter acquisition unit include sensing receive and signal processing unit,
Cooling unit, heat insulation pedestal and sensing element, described heat insulation pedestal is fixed on the tube wall of high-temperature flue, described sensing element edge
The direction being perpendicular to high-temperature flue axis is fixed on heat insulation pedestal, and the measurement end of sensing element stretches in high-temperature flue, described
Sensing receives and signal processing unit is fixed on one end that sensing element is positioned at outside high-temperature flue, and sensing receives and signal processing list
Unit records the flue gas flow in high-temperature flue, flow velocity by sensing element, described cooling unit be enclosed in sensing element be positioned at every
Hot radical seat, sensing receive and between signal processing unit one section, described variable synthesis gas approach includes actuator, resistance to
Burner footpath adjustment seat, one end of described fire-resistant bore adjustment seat is stretched in vortex burner entrance, and the other end connects actuator,
Also include that the first flue gas composition detection device and control unit, described first flue gas composition detection device are arranged on high-temperature flue
Flue gas composition in detecting high-temperature flue, described control unit receives with the first flue gas composition detection device, sensing respectively
And signal processing unit, actuator electrical connection, control unit processes smoke movement parameter, synthesis flue gas composition parameter, and leads to
Cross the flexible of actuating mechanism controls fire-resistant bore adjustment seat, and then control the pore size of variable synthesis gas approach.
A kind of vortex burner the most according to claim 3, it is characterised in that: described variable synthesis gas approach also includes
Fireproof flue, heat-insulating and sealing, compression thermal insulation layer, elevated-temperature seal, the cross section of described fireproof flue is U-shaped, opening of fireproof flue
Mouth seals by compressing thermal insulation layer, and described fire-resistant bore adjustment seat stretches in fireproof flue through compressing thermal insulation layer, described fire-resistant
Bore conditioned seat width of one end in fireproof flue is more than fire-resistant bore conditioned seat width of one end outside fireproof flue,
Elevated-temperature seal is set between fire-resistant bore adjustment seat and fireproof flue sidewall, sets between fire-resistant bore adjustment seat and compression thermal insulation layer
Put heat-insulating and sealing.
5. a stoker fired grate formula refuse gasification CIU, including incinerator, it is characterised in that: described incinerator
Including grate, and feed hopper, gasification furnace and the incinerator set gradually along feedstock direction on grate, the rear of gasification furnace is
The cinder notch that falls of gasification furnace, incinerator is positioned at gasification furnace and falls the front lower place of cinder notch, and the rear of incinerator is the slag notch of incinerator, institute
Stating grate and be provided with garbage pusher device, described garbage pusher device is positioned at the lower section of feed hopper, for being pushed away by the rubbish in feed hopper
Enter in gasification furnace, being respectively arranged below with at least one and independently set of the lower section of gasification furnace moving hearth and incinerator moving hearth
The air compartment put, is provided with windrow seal section, the grate between described gasification furnace and incinerator between described feed hopper, gasification furnace
Leaving transition in part to fall slag section, the described transition slag section that falls is provided with residue pusher, for the rubbish that will fall in gasification furnace
Residue pushes in incinerator；
Described gasification furnace, incinerator include furnace shell, moving hearth respectively, and the forward and backward side of described gasification furnace is close by windrow respectively
Envelope section, the transition slag section that falls seals, and described transition falls slag section isolation gasification furnace, incinerator, makes gasification furnace, incinerator separate；
Described gasification furnace, incinerator, respectively in the shape that arches upward, the face arch of described gasification furnace, rear arch are respectively provided with secondary and supply air port,
The vault of described gasification furnace arranges the first exhanst gas outlet, and the vault of described incinerator arranges the second exhanst gas outlet, described gasification furnace,
Igniting combustion supporting hole it is respectively equipped with on incinerator；
Also including the arbitrary described vortex burner of claim 1-4, described vortex burner entrance and the first exhanst gas outlet are even
Logical；
Also including circulating air feed system, described circulation air feed system includes dust arrester, the first blower fan, the second blower fan, described removes
The inlet end of dirt device is connected by pipeline and the second exhanst gas outlet, and pipeline and the first wind are passed through in the outlet side of described dust arrester
The inlet end of machine connects, and the outlet side of described first blower fan connects the house steward of the first manifold, and the arm of described first manifold is respectively
Connect for air port with the secondary on each air compartment of the lower section of gasification furnace moving hearth and gasification furnace face arch, rear arch, described
The first regulation valve it is respectively provided with on each arm of the first manifold, the air inlet of described second blower fan and atmosphere, described second
The gas outlet of blower fan connects the house steward of the second manifold, the arm of described second manifold respectively with incinerator moving hearth below each
Air compartment and the inlet end of dust arrester, outlet side connection, each arm of described second manifold is respectively provided with the second tune
Joint valve, also includes that the 3rd manifold, the described house steward of the 3rd manifold connect with the gas outlet of the second blower fan, described 3rd manifold each
Arm connects for air port with each combustion air respectively, and each arm of the 3rd manifold is respectively provided with the 3rd regulation valve.
A kind of stoker fired grate formula refuse gasification CIU the most according to claim 5, it is characterised in that: described first discrimination
Pipe also has an arm being connected with vortex burner entrance, and this arm is provided with the regulation valve of correspondence, the first blower fan extraction
The remainder flue gas not utilized be injected into vortex burner by vortex burner entrance, and by corresponding regulation
Valve regulation wind supply quantity.
A kind of stoker fired grate formula refuse gasification CIU the most according to claim 6, it is characterised in that: described first discrimination
The arm that pipe is connected with vortex burner entrance is provided with flue gas amount detecting device, the second flue gas composition detection device, described cigarette
Gas amount detecting device, the second flue gas composition detection device and the 3rd regulation valve electrically connect with control unit respectively, described control
What cell processing the second flue gas composition detection device gathered synthesizes flue gas composition parameter and the conjunction of flue gas amount detecting device collection
Become flue gas flow parameter, and by the 3rd governor valve control combustion air wind supply quantity.
A kind of stoker fired grate formula refuse gasification CIU the most according to claim 5, it is characterised in that: described dedusting fills
It is set to cyclone separator or hot precipitator；Described first blower fan is high-temperature blower, and described second blower fan is aerator.
A kind of stoker fired grate formula refuse gasification CIU the most according to claim 5, it is characterised in that: described transition falls
Being provided with isolating door to be opened/closed in slag section, described isolating door is for cutting off gasification furnace, incinerator.
A kind of stoker fired grate formula refuse gasification CIU the most according to claim 5, it is characterised in that: described gasification
The face arch of stove is flat construction, or, the face arch of gasification furnace is that rear end is inclined upwardly structure.
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| CN201610801164.3A CN106224969B (en) | 2016-09-05 | 2016-09-05 | Stoker fired grate formula refuse gasification incineration system and vortex burner |
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| CN201610801164.3A CN106224969B (en) | 2016-09-05 | 2016-09-05 | Stoker fired grate formula refuse gasification incineration system and vortex burner |
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| Publication number | Publication date |
|---|---|
| CN106224969B (en) | 2018-04-13 |
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Effective date of registration: 20230327 Address after: No. 3, Jianqiao Avenue, Jianqiao Industrial Park, Dadukou District, Chongqing 401325 Patentee after: Chongqing Sanfeng Environment Group Co.,Ltd. Patentee after: Chongqing University of Science & Technology Address before: No. 20, East Road, University City, Chongqing, Shapingba District, Chongqing Patentee before: Chongqing University of Science & Technology |