CN106224970B - Cavity combustion chamber in stoker fired grate formula refuse gasification CIU and inverted cone-shaped - Google Patents
Cavity combustion chamber in stoker fired grate formula refuse gasification CIU and inverted cone-shaped Download PDFInfo
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- CN106224970B CN106224970B CN201610801181.7A CN201610801181A CN106224970B CN 106224970 B CN106224970 B CN 106224970B CN 201610801181 A CN201610801181 A CN 201610801181A CN 106224970 B CN106224970 B CN 106224970B
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- flue
- inverted cone
- combustion chamber
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- gasification furnace
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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
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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
- F23G5/08—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating
- F23G5/14—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating including secondary combustion
- F23G5/16—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating including secondary combustion in a separate combustion chamber
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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
- F23G5/44—Details; Accessories
- F23G5/442—Waste feed arrangements
- F23G5/444—Waste feed arrangements for solid waste
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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
- F23G5/50—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
- F23J15/02—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material
- F23J15/022—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material for removing solid particulate material from the gasflow
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J15/00—Arrangements of devices for treating smoke or fumes
- F23J15/02—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material
- F23J15/022—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material for removing solid particulate material from the gasflow
- F23J15/027—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material for removing solid particulate material from the gasflow using cyclone separators
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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
- F23L5/00—Blast-producing apparatus before the fire
- F23L5/02—Arrangements of fans or blowers
-
- 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
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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
- F23J2217/00—Intercepting solids
- F23J2217/40—Intercepting solids by cyclones
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J2217/00—Intercepting solids
- F23J2217/60—Intercepting solids using settling/precipitation chambers
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Environmental & Geological Engineering (AREA)
- Incineration Of Waste (AREA)
Abstract
The invention discloses cavity combustion chamber in a kind of stoker fired grate formula refuse gasification CIU and inverted cone-shaped, the inner chamber of cavity combustion chamber includes the burning gallery set gradually from top to bottom in inverted cone-shaped, conial channel, flying dust expansion chamber, taper slag notch and the ring smoke passage set around conial channel, annular vent flue, conial channel is up-small and down-big, the diameter of flying dust expansion chamber is more than the diameter of conial channel lower end, ring smoke passage is in up-small and down-big taper, the lower end of ring smoke passage connects with flying dust expansion chamber, the lower end of annular vent flue connects with the upper end of ring smoke passage, taper slag notch is up big and down small.Using cavity combustion chamber in this inverted cone-shaped, there is higher efficiency of dust collection and efficiency of combustion, higher heat recovery efficiency, controlled burning and controllable collection can be realized, reduce thermal losses, and pollutant emission can be efficiently reduced.
Description
Technical field
The invention belongs to solid waste incineration processing technology field, more particularly to a kind of stoker fired grate formula refuse gasification to burn
Cavity combustion chamber in burning system and inverted cone-shaped.
Background technology
Existing technology of garbage disposal mainly has burning, sanitary landfills, compost, waste recovery etc..It is conventional in garbage disposal
In technology, burning disposal has that reduced training is obvious, it is innoxious thoroughly, occupation of land amount is small, and waste heat energy is utilized, and secondary pollution is few
The advantages that, meet the strategic requirement of China's sustainable development.But with the continuous improvement to environmental requirement both at home and abroad, 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, especially for domestic rubbish primarily now using all kinds of incineration technologies, gasification burning technology widely industrialize by
The technological innovation of domestic garbage disposal industry is brought to regenerate.
For many years, scientific research of the China to the gasification burning technology such as biomass, rubbish, be in progress a lot of, the base in laboratory
Plinth research is a lot, also has application study, such as：Rotary kiln type, vertical and fluidized bed type destructive gasifying or temperature gasification and high melting skill
Art etc..But Technique Popularizing is applied upper or a definite limitation be present, raw material type, garbage treatment quantity, secondary pollution control and economy
Benefit etc. is principal element.
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, mechanical backstepping fire grate, forwards fire grate or combined fire grate are used in body of heater wherein having, is also adopted
With fire grates such as chain-plate type and drum-types.
In summary, typical incinerator, respectively there is its own advantage, but need what is solved in China's practical application
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. with being on the increase for refuse production, sanitary fill such as mountain, garbage treatment quantity must be effectively improved,
It can just meet the market requirement.
3. in face of strict pollutant emission requirement, secondary pollution control is the key problem for technically needing to solve.
4. in order to effectively increase economic efficiency, in rubbish heat treatment process, the organic efficiency of heat needs to improve.It is existing
Rubbish heat treatment technics generally use boiler produce steam shift steam turbine power generation onto, whole transition heat efficiency losses are larger, place
Identical quantity of refuse is managed, relative thermal losses and the raising heat exchanger effectiveness can of reducing improves the thermal efficiency.
5. conventional garbage is burned in mode and boiler applications, high-temperature dust removal is less or does not have, and some efficiency is also not high enough, high
Effect dedusting and burning are had both less, the easy dust stratification of boiler, decline thermal conversion efficiency, so as to which lower power production, maintenance period are short
Deng.
For example following two patents of invention of existing incinerator：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
Manage model comparision to fall behind, simply dry-burn-burn, solid combustion discharges the process of heat；Thermal chemical reaction is to aoxidize in stove
Based on reaction, reduction reaction auxiliary, secondary pollution is also easy to produce；When rubbish burns in stove, oxygen quotient excessively is big, First air, two
Secondary wind infeed amount is big, and dust content is higher in flue gas, and heat reclaiming system and smoke processing system are had a great influence, easily product
Ash, exhaust gas volumn is larger, reduces thermal conversion efficiency；The gasification furnace and incinerator not being separately provided, can only handle rubbish by several times,
Large-scale rubbish continuous gasification burning disposal can not be realized, garbage treatment quantity is smaller.
The content of the invention
It is an object of the invention to overcome the deficiencies of the prior art and provide a kind of stoker fired grate formula refuse gasification CIU
With cavity combustion chamber in inverted cone-shaped, cavity combustion chamber has higher efficiency of dust collection and efficiency of combustion in inverted cone-shaped, can realize controllable
Burning and controllable dedusting, can reduce thermal losses, the organic efficiency of heat is higher, and can efficiently reduce pollutant emission.
The object of the present invention is achieved like this：
Cavity combustion chamber in a kind of inverted cone-shaped, set combustion chamber ignition combustion-supporting on the top plate of cavity combustion chamber in the inverted cone-shaped
Hole, the tangentially-arranged inverted cone-shaped inner chamber entry of combustion chamber of upper end edge of inverted cone-shaped inner chamber sidewall of combustion chamber, in the inverted cone-shaped
The inner chamber of cavity combustion chamber include set gradually from top to bottom burning gallery, conial channel, flying dust expansion chamber, taper slag notch with
And around conial channel set ring smoke passage, annular vent flue, the ring smoke passage, annular vent flue with
Separated between conial channel by annular air guide pier, some combustion air air feed mouths are set in the side wall of the burning gallery, it is described
Each combustion air air feed mouth is respectively positioned on the lower section of inverted cone-shaped inner chamber entry of combustion chamber, and the conial channel is up-small and down-big, the flying dust
The diameter of expansion chamber is more than the diameter of conial channel lower end, and the ring smoke passage is in up-small and down-big taper, ring smoke
The lower end of passage connects with flying dust expansion chamber, and the lower end of the annular vent flue connects with the upper end of ring smoke passage, falls
Tangential outlet flue is set to be connected with annular vent flue in the side wall of tapered interior cavity combustion chamber, under big on the taper slag notch
It is small.
Preferably, the top of the ring smoke passage it is circumferentially arranged have it is some it is up-narrow and down-wide divide gas pier, adjacent point
Narrow wide flue gas ring road under being formed between gas pier.
Preferably, inverted cone-shaped inner chamber entry of combustion chamber is connected to feed the high-temperature flue of high-temperature flue gas, the height
Smoke movement parameter acquisition unit is set on warm flue, and inverted cone-shaped inner chamber entry of combustion chamber sets variable synthesis flue gas to enter
Mouthful, the smoke movement parameter acquisition unit includes sensing reception and signal processing unit, cooling unit, heat-insulated pedestal and sensing
Element, the heat-insulated pedestal are fixed on the tube wall of high-temperature flue, and the sensing element is along perpendicular to the side of high-temperature flue axis
To being fixed on heat-insulated pedestal, the measurement end of sensing element is stretched into high-temperature flue, and the sensing receives and signal processing unit
One end that sensing element is located at outside high-temperature flue is fixed on, sensing receives and signal processing unit measures high temperature by sensing element
Flue gas flow, flow velocity in flue, the cooling unit are enclosed in sensing element and are located at heat-insulated pedestal, sensing reception and signal
Manage on one section between unit, the variable synthesis gas approach includes executing agency, fire resisting bore adjustment seat, the resistance to burner
One end of footpath adjustment seat is stretched into the entry of combustion chamber of inverted cone-shaped inner chamber, other end connection executing agency, in addition to the first flue gas group
Divide detection means and control unit, the first flue gas composition detection means, which is arranged on high-temperature flue, to be used to detect high-temperature flue
Interior flue gas composition, described control unit are received and signal processing unit, held with the first flue gas composition detection means, sensing respectively
Row mechanism electrically connects, control unit processing smoke movement parameter, synthesis flue gas composition parameter, and passes through actuating mechanism controls fire resisting
Bore adjustment seat is stretched, and then controls the pore size of variable synthesis gas approach.
Preferably, it is close also to include fireproof flue, heat-insulating and sealing, compression thermal insulation layer, high temperature for the variable synthesis gas approach
Envelope, the cross section of the fireproof flue is U-shaped, and the opening of fireproof flue is sealed by compressing thermal insulation layer, and the fire resisting bore is adjusted
Section seat is stretched into fireproof flue through thermal insulation layer is compressed, and the width that the fire resisting bore adjustment seat is located at one end in fireproof flue is big
It is located at the width of one end outside fireproof flue in fire resisting bore adjustment seat, is set between fire resisting bore adjustment seat and fireproof flue side wall
Elevated-temperature seal, heat-insulating and sealing is set between fire resisting bore adjustment seat and compression thermal insulation layer.
A kind of stoker fired grate formula refuse gasification CIU, including incinerator, the incinerator include grate,
And feed hopper, gasification furnace and the incinerator set gradually on grate along feedstock direction, the rear of gasification furnace is gasification furnace
Slag mouth, incinerator are located at the front lower place of gasification furnace slag mouth, and the rear of incinerator is the slag notch of incinerator, on the grate
Provided with garbage pusher device, the garbage pusher device is located at the lower section of feed hopper, for the rubbish in feed hopper to be pushed into gasification furnace
Interior, the lower section of gasification furnace moving hearth and incinerator moving hearth are respectively arranged below with least one be independently arranged once
Air compartment, windrow seal section is provided between the feed hopper, gasification furnace, is stayed on the grate part between the gasification furnace and incinerator
There is transition slag section, the transition slag section is provided with residue pusher, for the rubbish residue push-in that will be fallen in gasification furnace
In incinerator；
The gasification furnace, incinerator include furnace shell, moving hearth respectively, and the forward and backward side of the gasification furnace passes through heap respectively
Expect seal section, the sealing of transition slag section, the transition slag section isolation gasification furnace, incinerator, make gasification furnace, incinerator mutually only
It is vertical；
The gasification furnace, incinerator set secondary air feed respectively respectively in arching upward shape on the face arch of the gasification furnace, rear arch
Mouthful, the vault of the gasification furnace sets the first exhanst gas outlet, and the vault of the incinerator sets the second exhanst gas outlet, the gasification
Igniting combustion supporting hole is respectively equipped with stove, incinerator；
Also include cavity combustion chamber in inverted cone-shaped, inverted cone-shaped inner chamber entry of combustion chamber connects with the first exhanst gas outlet；
Also include circulation air feed system, the circulation air feed system includes dust arrester, the first blower fan, the second blower fan, institute
The inlet end for stating dust arrester is connected by pipeline with the second exhanst gas outlet, and the outlet side of the dust arrester passes through pipeline and
The inlet end connection of one blower fan, the outlet side of first blower fan connect the house steward of the first manifold, the branch pipe of first manifold
Connected respectively with the secondary air feed mouth on each air compartment and gasification trimmer arch, rear arch of the lower section of gasification furnace moving hearth,
First regulating valve is set respectively on each branch pipe of first manifold, and the air inlet and atmosphere of second blower fan are described
The gas outlet of second blower fan connects the house steward of the second manifold, the branch pipe of second manifold respectively with below incinerator moving hearth
The inlet end of each an air compartment and dust arrester, outlet side connection, the is set on each branch pipe of second manifold respectively
Two regulating valves, in addition to the 3rd manifold, the house steward of the 3rd manifold connect with the gas outlet of the second blower fan, the 3rd manifold
Each branch pipe connected respectively with each combustion air air feed mouth, the 3rd regulating valve is set respectively on each branch pipe of the 3rd manifold.
Preferably, first manifold also has a branch pipe being connected with inverted cone-shaped inner chamber entry of combustion chamber, the branch pipe
Corresponding regulating valve is provided with, the remainder flue gas not utilized that the first blower fan extracts is entered by cavity combustion chamber in inverted cone-shaped
Mouth is injected into cavity combustion chamber in inverted cone-shaped, and passes through corresponding regulation valve regulation wind supply quantity.
Preferably, the branch pipe that first manifold is connected with inverted cone-shaped inner chamber entry of combustion chamber is provided with flue gas amount detection device
Put, the second flue gas composition detection means, the flue gas amount detecting device, the second flue gas composition detection means and the 3rd regulating valve
Electrically connected respectively with control unit, described control unit handles the synthesis flue gas composition ginseng of the second flue gas composition detection means collection
Number and the synthesis flue gas flow parameter of flue gas amount detecting device collection, and pass through the 3rd governor valve control combustion air wind supply quantity.
In order to effectively carry out dedusting to the high-temperature flue gas of incinerator discharge, it is preferable that the dust arrester is whirlwind point
From device or hot precipitator；First blower fan is high-temperature blower, and beneficial to working in high temperature environments, second blower fan is
Air blower.
In order to prevent that wind is altered between gasification furnace, incinerator, it is preferable that be provided with the transition slag section it is to be opened/closed every
From door, the isolating door is used to separate gasification furnace, incinerator.
In order to preferably adapt to the installing space in factory, it is preferable that the face arch of the gasification furnace is flat construction, or
Person, the face arch of gasification furnace are inclined upwardly structure for rear end.
By adopting the above-described technical solution, the present invention has the advantages that：
Flying dust expansion chamber external drum, back taper passage is up-small and down-big, volume increase, pressure reduce, flow velocity reduce, plus whirlwind from
Mental power function, further promote flying dust sedimentation；Flying dust sedimentation building volume further increases, and dust removing effects are further；Annular cigarette
Gas passage flue gas size is gradually reduced, and flue gas is up, and flying dust, into trapezoidal flue gas ring road, reduces the suction of flying dust from resedimentation
Go out, dedusting is more favourable；Flue gas smaller closer to discharge area due to the pyramidal structure of ring smoke passage, wide at the top and narrow at the bottom
Ring road makes ring smoke passage high temperature flue gas flow rate uniform.The dedusting of burning gallery section cyclonic separation, back taper passage, flying dust sedimentation
Room, ring smoke passage, ring road set combination to improve efficiency of dust collection, and flue gas is synthesized during dedusting and obtains being sufficiently mixed combustion
Burn, improve efficiency of combustion.
Control unit processing smoke movement parameter (speed, flow, fluid force etc.), synthesis flue gas composition and high-temperature blower go out
Mouth is to the flue gas composition and flow of cavity combustion chamber in inverted cone-shaped, control executing agency regulation gas approach aperture, while control helps
Air capacity is fired, realizes the fluctuations such as unstability is brought in waste component and heat treatment process synthesis exhaust gas volumn and component
Regulation, so as to control smoke inlet initial velocity and combustion-supporting oxygen-supplying amount, to reach the purpose of high-effective dust-removing and burning.Control unit
Control variable synthesis gas approach executing agency：Purely mechanic transmission, mechanical parameter enlarger, then executing agency is driven, perform
It is more efficient.
Air blower blasts air and provides First air for incinerator and provide temperature adjustment air feed for cyclone separator, high-temperature blower,
By the second regulation valve regulation wind supply quantity on corresponding pipeline, incinerator residue is set fully to burn；Then, high-temperature blower extracts combustion
The flue gas of cinder stove, after temperature adjustment and cyclone collection flying dust, form the flue gas supply gasification furnace of certain pressure once
Wind and Secondary Air, by the first regulation valve regulation wind supply quantity on corresponding pipeline, rubbish in gasification furnace is produced gasification, contain one
The flue gas of quantitative synthesis gas, discharged from the first exhanst gas outlet, into inverted cone-shaped in cavity combustion chamber processing links, the combustion of inverted cone-shaped inner chamber
Burn room and high-temperature flue gas is provided.Present inventive concept is novel, and garbage treatment quantity is big, and the rubbish bed of material undergoes dry, gas on stoker fired grate
Change the stage that burns with residue, adapt to the characteristics such as China's house refuse water content height, complicated component, improve garbage processing procedure
In energy conversion efficiency and reduce pollutant discharge amount in flue gas, effectively prevent secondary pollution, and can realize large-scale
Rubbish continuous gasification burning disposal, ensure that refuse gasification burns effect and lime-ash clinker ignition loss, it is relative to reduce thermal losses and raising
Heat exchanger effectiveness, improve the thermal efficiency.
Gasification furnace, incinerator are provided separately, and the vault of gasification furnace sets the first exhanst gas outlet, and the vault of incinerator sets the
Two exhanst gas outlets, flue gas is handled respectively beneficial to the difference according to flue gas quality, while be advantageous to flue gas ash removal, can provide more
The flue gas of high-quality, make the utilization rate of flue gas higher, the waste residue of discharge is less.
Brief description of the drawings
Fig. 1 is the structural representation of cavity combustion chamber in inverted cone-shaped；
Fig. 2 is the structural representation of smoke movement parameter acquisition unit；
Fig. 3 is Fig. 1 A-A schematic cross-sectional views；
Fig. 4 is Fig. 1 B-B schematic cross-sectional views；
Fig. 5 is Fig. 4 C-C schematic cross-sectional views；
Fig. 6 is the structural representation of stoker fired grate formula refuse gasification CIU.
Reference
1 is incinerator, and 101 be grate, and 102 be feed hopper, and 103 be gasification furnace, and 104 be incinerator, and 105 be stove
Bed, 106 be garbage pusher device, and 107 be an air compartment, and 108 be windrow seal section, and 109 be transition slag section, and 110 push away for residue
Glassware, 111 be isolating door, and 112 be the first exhanst gas outlet, and 113 be the second exhanst gas outlet, and 114 be igniting combustion supporting hole, and 115 be two
Secondary air feed mouth, 116 be slag notch, and 117 be slag mouth；
2 be circulation air feed system, and 201 be dust arrester, and 202 be the first blower fan, and 203 be the second blower fan, and 204 be the first discrimination
Pipe, 205 be the second manifold, and 206 be the 3rd manifold, and 207 be the first regulating valve, and 208 be the second regulating valve, and 209 be the 3rd regulation
Valve；
3 be cavity combustion chamber in inverted cone-shaped, and 301 be combustion chamber ignition combustion-supporting hole, and 302 be taper slag notch, and 303 be inverted cone-shaped
Inner chamber entry of combustion chamber, 304 be tangential outlet flue, and 305 be combustion air air feed mouth, and 306 be burning gallery, and 307 be conial channel,
308 be flying dust expansion chamber, and 309 be ring smoke passage, and 310 be annular vent flue, and 311 be annular air guide pier, and 312 be to divide gas
Pier, 313 be flue gas ring road, and 314 be high-temperature flue, and 315 receive and signal processing unit for sensing, and 316 be cooling unit, 317
It is sensing element for heat-insulated pedestal, 318,319 be executing agency, and 320 be fire resisting bore adjustment seat, and 321 be the first flue gas composition
Detection means, 322 be control unit, and 323 be fireproof flue, and 324 be heat-insulating and sealing, and 325 is compress thermal insulation layer, and 326 be high temperature
Sealing, 327 be flue gas amount detecting device, and 328 be the second flue gas composition detection means.
Embodiment
Referring to Fig. 1 to Fig. 5, for a kind of preferred embodiment of cavity combustion chamber in inverted cone-shaped, the inverted cone-shaped inner chamber burning
Combustion chamber ignition combustion-supporting hole 301 is set on the top plate of room 3, and the upper end edge of the side wall of cavity combustion chamber 3 is tangentially-arranged in the inverted cone-shaped
Inverted cone-shaped inner chamber entry of combustion chamber 303, the inner chamber of cavity combustion chamber 3 includes the burning set gradually from top to bottom in the inverted cone-shaped
Passage 306, conial channel 307, flying dust expansion chamber 308, taper slag notch 302 and the annular set around conial channel 307
Exhaust gases passes 309, annular vent flue 310, the ring smoke passage 309, annular vent flue 310 and conial channel 307
Between separated by annular air guide pier 311, some combustion air air feed mouths 305 are set in the side wall of the burning gallery 306, it is described
Each combustion air air feed mouth 305 is respectively positioned on the lower section of inverted cone-shaped inner chamber entry of combustion chamber 303, and the conial channel 307 is up-small and down-big,
The diameter of the flying dust expansion chamber 308 be more than the lower end of conial channel 307 diameter, the ring smoke passage 309 present it is small under
Big taper, the lower end of ring smoke passage 309 connect with flying dust expansion chamber 308, the lower end of the annular vent flue 310 with
The upper end connection of ring smoke passage 309, the top of the ring smoke passage 309 is circumferentially arranged have it is some up-narrow and down-wide
Divide gas pier 312, narrow wide flue gas ring road 313 under being formed between adjacent point of gas pier 312.The side wall of cavity combustion chamber 3 in inverted cone-shaped
Upper to set tangential outlet flue 304 to be connected with annular vent flue 310, the taper slag notch 302 is up big and down small.
Inverted cone-shaped inner chamber entry of combustion chamber 303 is connected to feed the high-temperature flue 314 of high-temperature flue gas, the high temperature
Smoke movement parameter acquisition unit is set on flue 314, and inverted cone-shaped inner chamber entry of combustion chamber 303 sets variable synthesis flue gas
Import, the smoke movement parameter acquisition unit include sensing reception and signal processing unit 315, cooling unit 316, heat-insulated base
Seat 317 and sensing element 318, the heat-insulated pedestal 317 are fixed on the tube wall of high-temperature flue 314, the edge of sensing element 318
It is fixed on perpendicular to the direction of the axis of high-temperature flue 314 on heat-insulated pedestal 317, the measurement end of sensing element 318 stretches into high temperature cigarette
In road 314, the sensing receives and signal processing unit 315 is fixed on sensing element 318 is located at outside high-temperature flue 314 one
End, sensing reception and signal processing unit 315 measure flue gas flow, flow velocity in high-temperature flue 314 by sensing element 318,
The cooling unit 316 is enclosed in sensing element 318 and is located between heat-insulated pedestal 317, sensing reception and signal processing unit 315
One section on, the heat-insulated pedestal 317, cooling unit 316 prevent the heat of high-temperature flue 314 conduct to sensing receive and signal
Processing unit 315.The variable synthesis gas approach includes executing agency 319, fire resisting bore adjustment seat 320, the execution machine
Structure 319 can use cylinder, oil cylinder etc..Inverted cone-shaped inner chamber entry of combustion chamber 303 is stretched into one end of the fire resisting bore adjustment seat 320
It is interior, other end connection executing agency 319, in addition to the first flue gas composition detection means 321 and control unit 322, described first
Flue gas composition detection means 321, which is arranged on high-temperature flue 314, to be used to detect the flue gas composition in high-temperature flue 314, the control
Unit 322 processed respectively with the first flue gas composition detection means 321, sensing receive and signal processing unit 315, executing agency 319
Electrical connection, control unit 322 handles smoke movement parameter, synthesis flue gas composition parameter, and controls fire resisting by executing agency 319
Bore adjustment seat 320 is stretched, and then controls the pore size of variable synthesis gas approach.
In the present embodiment, it is heat-insulated that the variable synthesis gas approach also includes fireproof flue 323, heat-insulating and sealing 324, compression
Layer 325, elevated-temperature seal 326, the fireproof flue 323, elevated-temperature seal 326 can use conventional exotic material to make, it is described every
Heat seal 324, compression thermal insulation layer 325 can use conventional heat-barrier material to make.The cross section of the fireproof flue 323 is U-shaped, resistance to
The opening of fiery flue 323 is sealed by compressing thermal insulation layer 325, and the fire resisting bore adjustment seat 320 is stretched through thermal insulation layer 325 is compressed
Enter in fireproof flue 323, the width that the fire resisting bore adjustment seat 320 is located at one end in fireproof flue 323 is more than fire resisting bore
Adjustment seat 320 is located at the width of 323 outer one end of fireproof flue, is set between fire resisting bore adjustment seat 320 and the side wall of fireproof flue 323
Elevated-temperature seal 326 is put, heat-insulating and sealing 324 is set between fire resisting bore adjustment seat 320 and compression thermal insulation layer 325.
Referring to Fig. 6, for a kind of preferred embodiment of stoker fired grate formula refuse gasification CIU, including incinerator
1, the incinerator 1 includes grate 101, and feed hopper 102, the gas set gradually on grate 101 along feedstock direction
Change 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 is gasified, 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 mechanical kiln that the siege 105 of gasification furnace 103 and incinerator 104 is independently driven using segmentation
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
It is folded, it is spaced collect form, adjacent multigroup moving grate plate is connected by pull bar, is driven using a set of drive device.Machine
Tool grate-type 105 carrier as conveying garbage of moving hearth, embodiments thereof can be all types of moving hearths 105, such as chain
Board-like, drum-type, multisection type fire grate system etc..
The grate 101 is provided with garbage pusher device 106, and the garbage pusher device 106 is located at the lower section of feed hopper 102,
For the rubbish in feed hopper 102 to be pushed into gasification furnace 103, the lower section of the moving hearth 105 of gasification furnace 103 and incinerator
104 moving hearths 105 are respectively arranged below with an at least one air compartment 107 being independently arranged, in the present embodiment, with gasification furnace
Fire grate, drive device corresponding to air compartment 107 of 103 first halfs, as the dryer section of the siege 105 of gasification furnace 103, with gasification
The gasification section of fire grate, drive device as the siege 105 of gasification furnace 103 corresponding to a latter half of air compartment 107 of stove 103.Gasification
The 1-2 independent air feeds of air compartment 107 can be respectively adopted in dryer section, the gasification section of the siege 105 of stove 103, can also distinguish
Using the 3-4 independent air feeds of air compartment 107.Certainly, fire grate, drive device and an air compartment 107 can not be also correspondingly arranged,
Preferably bed of material movement and air distribution relation on regulation moving hearth 105.Incinerator 104 can use 1-4 independent First airs
The air feed of room 107, burn rear lime-ash and excluded from slag notch, into next step treatment process.
Windrow seal section 108 is provided between the feed hopper 102, gasification furnace 103, the work of garbage pusher device 106 is entered to be located in place
In in windrow seal section 108, garbage raw material is put into from feed hopper 102 and fallen, and garbage pusher device 106 retreats, then promotes, reciprocal more
Secondary pusher forms windrow in windrow seal section 108, the entrance of gasification furnace 103 is in windrow sealing state, and enhancing gasification furnace 103 is close
Effect is sealed, solves garbage pusher device 106 and 102 easy leakage problem of feed hopper.When needing the complete prepurging to dispose all rubbish,
The forward impelling half stroke again of garbage pusher device 106, rubbish is pushed completely into gasification furnace 103, loses the entrance of gasification furnace 103
Windrow sealing effectiveness.Transition slag section 109, institute are left on the part of grate 101 between the gasification furnace 103 and incinerator 104
State transition slag section 109 and be provided with residue pusher 110, the rubbish residue for will be fallen in gasification furnace 103 is pushed into incinerator
In 104, transition slag section 109 can be at windrow sealing state when accumulating rubbish residue, strengthen the sealing effectiveness of gasification furnace 103,
Solves the problems, such as string wind between gasification furnace 103, incinerator 104.In the present embodiment, being provided with the transition slag section 109 can
The isolating door 111 of opening and closing, the isolating door 111 are used to separate gasification furnace 103, incinerator 104.At furnace lifting initial stage or need to control
When altering wind between gasification furnace 103 and incinerator processed, isolating door 111 is closed, stacking a certain amount of residue when slag section forms windrow
After sealing, isolating door 111 can be kept to open, coordinate to use with the residue pusher 110 that lower section is set, to realize that rubbish is continuous
Gasification burning processing.
The upper end of the gasification furnace 103, the upper end of incinerator 104 are respectively in the shape that arches upward, the face arch of the gasification furnace 103
Flat construction, or, the face arch of gasification furnace 103 is inclined upwardly structure for rear end.The vault of the gasification furnace 103 sets the first cigarette
Gas outlet 112, the vault of the incinerator 104 set the second exhanst gas outlet 113, and the upper end of gasification furnace 103 is arched upward, burnt
Igniting combustion supporting hole 114 is respectively equipped with the arching upward of the upper end of stove 104.Flue gas gasify from the first exhanst gas outlet 112, the second exhanst gas outlet
113 exclude, in addition to cavity combustion chamber 3 in inverted cone-shaped, inverted cone-shaped inner chamber entry of combustion chamber connect with the first exhanst gas outlet.Gas
Change the furnace cavity of stove 103 compared with traditional waste incinerator, it is relatively reduced；Forward and backward arch becomes with the relative position of moving hearth 105
It is small, reduce the space of incinerator occupancy, be also easier to be incubated, reduce the amount of leakage of heat, be advantageous to rubbish and fully gasify.
Secondary air feed mouth 115 is set respectively on the face arch of the gasification furnace 103, rear arch.
Also include circulation air feed system 2, the circulation air feed system 2 includes dust arrester 201, the first blower fan 202, second
Blower fan 203, the dust arrester 201 are cyclone separator or hot precipitator, in the present embodiment, the dust arrester 201
For cyclone separator.First blower fan 202 is high-temperature blower, and second blower fan 203 is air blower.The dust arrester
201 inlet end is connected by pipeline with the second exhanst gas outlet 113, and the outlet side of the dust arrester 201 passes through pipeline and
The inlet end connection of one blower fan 202, the outlet side of first blower fan 202 connect the house steward of the first manifold 204, first discrimination
The branch pipe of pipe 204 respectively each the air compartment 107 and the face arch of gasification furnace 103 with the lower section of the moving hearth 105 of gasification furnace 103,
Secondary air feed mouth 115 on rear arch connects, and sets the first regulating valve 207 on each branch pipe of first manifold 204 respectively, gasification
The First air of stove 103 is that the flue gas generation certain pressure of high-temperature blower extraction incinerator 104 blasts the shifting of the stoker fired grate formula of gasification furnace 103
Corresponding to the dynamic lower section of siege 105 in an air compartment 107, then by an air holes spray penetration rubbish on moving hearth 105, enter
Promoting the circulation of qi, wind supply quantity is adjusted by the first regulating valve 207 on corresponding each branch pipe.The Secondary Air of gasification furnace 103 is that high-temperature blower is taken out
Take the flue gas of incinerator 104 to produce certain pressure and blast the burner hearth of gasification furnace 103, its spray-hole be arranged on the face arch of gasification furnace 103 and
On rear arch.Secondary air feed mouth 115 is provided with forward and backward arch, improves gasification efficiency, strengthens polymer substance in flue gas and decomposes.Afterwards
It is provided with igniting combustion supporting hole 114 on arch, temperature uses in furnace lifting, baker and stable gasification furnace 103, passes through the on corresponding each branch pipe
One regulating valve 207 adjusts wind supply quantity.The air inlet and atmosphere of second blower fan 203, the air that the second blower fan 203 blasts
Can be cold wind or the hot blast after heating.The gas outlet of second blower fan 203 connects the house steward of the second manifold 205, institute
State each air compartment 107 and dust arrester of the branch pipe of the second manifold 205 respectively with the lower section of 104 moving hearth of incinerator 105
201 inlet end, outlet side connection, the second regulating valve 208 is set respectively on each branch pipe of second manifold 205.Incinerator
104 First airs are that the air of certain pressure is blasted an air compartment corresponding to the lower section of stoker fired grate formula moving hearth 105 by air blower
In 107, then by an air holes spray penetration residue on moving hearth 105, residual burning is carried out, by corresponding each branch pipe
The first regulating valve 207 regulation wind supply quantity.The inlet end of dust arrester 201, the air intake of outlet side are temperature adjustment air feed, temperature adjustment air feed
To be air blower by the air of certain pressure, which blast incinerator 104, exports (i.e. cyclone inlet) and carries out temperature adjustment, meanwhile, whirlwind
Separator outlet (i.e. high-temperature blower entrance) blasts further temperature adjustment, is adjusted by the first regulating valve 207 on corresponding each branch pipe
Wind supply quantity.
Also include the 3rd manifold 206, the house steward of the 3rd manifold 206 connects with the gas outlet of the second blower fan 203, described
Each branch pipe of 3rd manifold 206 connects with each combustion air air feed mouth 305 respectively, is set respectively on each branch pipe of the 3rd manifold 206
3rd regulating valve 209.Inverted cone-shaped inner chamber entry of combustion chamber 303 and combustion-supporting air feed mouth are arranged at cavity combustion chamber 3 in inverted cone-shaped
Can be that the flue gas in inverted cone-shaped in cavity combustion chamber 3 is longer with air mixture time, mixing is more uniformly distributed, more in circumferential wall
Sufficiently burning.3 combustion-supporting air feed of cavity combustion chamber is that the air of certain pressure is blasted combustion-supporting air feed mouth spray by air blower in inverted cone-shaped
Cavity combustion chamber 3 in inverted cone-shaped are injected, combustion-supporting air feed approach axis can be radially or tangentially；Carry out syngas combustion.Meanwhile
The flue gas generation certain pressure that high-temperature blower extracts incinerator 104 blasts the lower section of 103 stoker fired grate formula moving hearth of gasification furnace 105
Secondary air chamber on 103 forward and backward arch of a corresponding air compartment 107 and gasification furnace, first manifold 204 also have one with falling
The branch pipe of tapered inner chamber gas fume of combustion chamber entrance connection, the branch pipe are provided with corresponding regulating valve.High-temperature blower extracts not sharp
Remainder flue gas is finished, then cavity combustion chamber 3 in inverted cone-shaped are injected into by the smoke inlet of cavity combustion chamber in inverted cone-shaped 3, is entered
Row syngas combustion, by corresponding regulation valve regulation wind supply quantity, this structure can reduce thermal losses and improve heat exchanger effectiveness,
The organic efficiency of heat is substantially increased, and pollutant discharge amount can be efficiently reduced.
Further, first manifold detects with the branch pipe that inverted cone-shaped inner chamber entry of combustion chamber is connected provided with exhaust gas volumn
Device 327, the second flue gas composition detection means 328, the flue gas amount detecting device, the second flue gas composition detection means and
Three regulating valves electrically connect with control unit respectively, and described control unit handles the synthesis cigarette of the second flue gas composition detection means collection
Gas component parameter and the synthesis flue gas flow parameter of flue gas amount detecting device collection, and pass through the 3rd governor valve control combustion air
Wind supply quantity.
The incinerator 104 is provided with slag mouth 117, and the slag notch 116 of the incinerator 104 is located at incinerator slag mouth
117 underface, the slag mouth 117 are connected by pipeline with the slag notch of dust arrester 201.This sealing structure effect is good,
Reduction pollutant discharge amount can effectively be held.
A kind of waste disposal method of stoker fired grate formula refuse gasification CIU, this method are carried out according to the following steps：
Step A, the gate of stoker fired grate formula refuse gasification incinerator 1 and atmospheric vent is closed, starts mechanical grate-type rubbish
Rubbish incinerator 1, garbage raw material is put into feed hopper 102, the pusher back and forth of garbage pusher device 106 will be from feed hopper 102
The garbage raw material fallen is pushed into the windrow seal section 108 between feed hopper 102, gasification furnace 103, forms windrow seal section 108
Windrow sealing state, unnecessary rubbish fall into the moving hearth 105 of gasification furnace 103, and the moving hearth 105 of gasification furnace 103 works,
Rubbish is conveyed into transition slag section 109, the pusher back and forth of residue pusher 110, the rubbish in transition slag section 109 pushed away
Enter in incinerator 104, the work conveying garbage of moving hearth 105 of incinerator 104, until rubbish is in gasification furnace 103, incinerator
104 moving hearth 105 is accumulated to required thickness：0.6-0.8m, during baker, the rubbish accumulated can protect mobile stove
Bed 105, prevents scaling loss siege 105.Stop 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, in the presence of start-up burner, gasification furnace 103 and incinerator 104 are carried out furnace lifting,
Baker, treat that this process stabilization is completed, gasification furnace 103 and the burner hearth of incinerator 104 is reached 600-700 DEG C of predetermined temperature；Baker
Purpose be in order to remove the Natural Water and the crystallization water in lining, in order to avoid when going into operation due to furnace temperature rise it is too fast, moisture content is a large amount of
Expansion causes body of heater spalling, bubbling or deformation even furnace wall to collapse, and influences the intensity and service life of heating furnace furnace wall.
Step B, regulation circulation air feed system 2, regulation gasification furnace 103, incinerator 104 and circulation air feed system 2 are started
Technological parameter (pusher speed, fire grate speed, a wind-warm syndrome, blast and air quantity, secondary air temperature, blast and air quantity, furnace temperature,
Negative pressure, thickness of feed layer etc. in stove), fed intake to feed hopper 102, the work conveying garbage of moving hearth 105 of gasification furnace 103, rubbish
Burning is proceeded by the burner hearth of gasification furnace 103, rubbish residue is accumulated to form windrow sealing at transition slag section 109, made
The stove chamber inner combustion state temperature of gasification furnace 103 is stabilized to more than 850 DEG C, the work output combustion of moving hearth 105 of incinerator 104
Rubbish residue after cinder.
Step C, gasification furnace 103, incinerator 104 and each technological parameter (the pusher speed for circulating air feed system 2 are adjusted
Degree, fire grate speed, a wind-warm syndrome, blast and air quantity, secondary air temperature, blast and air quantity, furnace temperature, negative pressure, thickness of feed layer in stove
Deng), gasification furnace 103 gradually gasifies to rubbish, and gasification temperature is stable between 700-800 DEG C, makes gasification furnace 103 is stable to produce
The high-temperature flue gas of the raw synthesis gas containing 10%-20%, it is equal that the vaporized state of gasification furnace 103 stably carries out low temperature, medium temperature or high-temperature gasification
Can.The fired state temperature stabilization of incinerator 104 is set to realize rubbish continuous gasification burning disposal to more than 850 DEG C；It need to adjust simultaneously
Each technological parameter of cavity combustion chamber 3 in inverted cone-shaped, make in inverted cone-shaped the tangential temperature stabilization of outlet flue 304 of cavity combustion chamber 3 to 850 DEG C
More than.
Step D, it need to overhaul or during blowing out, stop feeding intake, regulation gasification furnace 103, incinerator 104 and circulation air feed system
2 technological parameter, gasification furnace 103 is gradually restored to fired state, after rubbish and rubbish residue are burnt, close stoker fired grate
Formula refuse gasification incinerator 1 and circulation air feed system 2.Each technological parameter of cavity combustion chamber 3 in inverted cone-shaped need to be adjusted simultaneously, made
Gasification furnace 103 is gradually restored to fired state.
Finally illustrate, preferred embodiment above is merely illustrative of the technical solution of the present invention and unrestricted, although logical
Cross above preferred embodiment the present invention is described in detail, it is to be understood by those skilled in the art that can be
Various changes are made to it in form and in details, without departing from claims of the present invention limited range.
Claims (10)
- A kind of 1. cavity combustion chamber in inverted cone-shaped, it is characterised in that：Combustion chamber is set on the top plate of cavity combustion chamber in the inverted cone-shaped Igniting combustion supporting hole, the tangentially-arranged inverted cone-shaped inner chamber entry of combustion chamber of upper end edge of inverted cone-shaped inner chamber sidewall of combustion chamber are described The inner chamber of cavity combustion chamber includes burning gallery, conial channel, flying dust expansion chamber, the taper set gradually from top to bottom in inverted cone-shaped Slag notch and the ring smoke passage set around conial channel, annular vent flue, the ring smoke passage, annular row Separated between gas flue and conial channel by annular air guide pier, some combustion air air feeds are set in the side wall of the burning gallery Mouthful, each combustion air air feed mouth is respectively positioned on the lower section of inverted cone-shaped inner chamber entry of combustion chamber, and the conial channel is up-small and down-big, institute The diameter for stating flying dust expansion chamber is more than the diameter of conial channel lower end, and the ring smoke passage is in up-small and down-big taper, ring The lower end of shape exhaust gases passes connects with flying dust expansion chamber, and the lower end of the annular vent flue connects with the upper end of ring smoke passage It is logical, set tangential outlet flue to be connected with annular vent flue in the side wall of cavity combustion chamber in inverted cone-shaped, on the taper slag notch It is small under big.
- 2. cavity combustion chamber in a kind of inverted cone-shaped according to claim 1, it is characterised in that：The ring smoke passage it is upper Portion is circumferentially arranged to be had and some up-narrow and down-wide divides gas pier, narrow wide flue gas ring road under being formed between adjacent point of gas pier.
- 3. cavity combustion chamber in a kind of inverted cone-shaped according to claim 1, it is characterised in that：Cavity combustion chamber in the inverted cone-shaped Entrance is connected to feed the high-temperature flue of high-temperature flue gas, and smoke movement parameter acquisition unit, institute are set on the high-temperature flue State inverted cone-shaped inner chamber entry of combustion chamber and variable synthesis gas approach is set, the smoke movement parameter acquisition unit connects including sensing Receive and signal processing unit, cooling unit, heat-insulated pedestal and sensing element, the heat-insulated pedestal are fixed on the tube wall of high-temperature flue On, the sensing element along being fixed on perpendicular to the direction of high-temperature flue axis on heat-insulated pedestal, stretch by the measurement end of sensing element Enter in high-temperature flue, the sensing receives and signal processing unit is fixed on one end that sensing element is located at outside high-temperature flue, feels It should receive and signal processing unit measures flue gas flow, flow velocity in high-temperature flue, the cooling unit bag by sensing element It is trapped among on one section that sensing element is located between heat-insulated pedestal, sensing reception and signal processing unit, the variable synthesis flue gas Import includes executing agency, fire resisting bore adjustment seat, and cavity combustion chamber in inverted cone-shaped is stretched into one end of the fire resisting bore adjustment seat Enter intraoral, other end connection executing agency, in addition to the first flue gas composition detection means and control unit, the first flue gas group Point detection means, which is arranged on high-temperature flue, is used to detecting the flue gas composition in high-temperature flue, and described control unit is respectively with first Flue gas composition detection means, sensing receives and signal processing unit, executing agency's electrical connection, control unit processing smoke movement ginseng Number, synthesis flue gas composition parameter, and by the flexible of actuating mechanism controls fire resisting bore adjustment seat, and then control variable synthesis cigarette The pore size of gas import.
- 4. cavity combustion chamber in a kind of inverted cone-shaped according to claim 3, it is characterised in that：The variable synthesis gas approach Also include fireproof flue, heat-insulating and sealing, compress thermal insulation layer, elevated-temperature seal, the cross section of the fireproof flue is U-shaped, fire resisting cigarette The opening in road is sealed by compressing thermal insulation layer, and the fire resisting bore adjustment seat is stretched into fireproof flue through thermal insulation layer is compressed, institute State fire resisting bore adjustment seat and be located at the width of one end in fireproof flue and be located at the outer one end of fireproof flue more than fire resisting bore adjustment seat Width, elevated-temperature seal is set between fire resisting bore adjustment seat and fireproof flue side wall, fire resisting bore adjustment seat and is compressed heat-insulated Heat-insulating and sealing is set between layer.
- 5. a kind of stoker fired grate formula refuse gasification CIU, including incinerator, it is characterised in that：The incinerator Including grate, and feed hopper, gasification furnace and the incinerator set gradually on grate along feedstock direction, the rear of gasification furnace are The slag mouth of gasification furnace, incinerator are located at the front lower place of gasification furnace slag mouth, and the rear of incinerator is the slag notch of incinerator, institute State grate and be provided with garbage pusher device, the garbage pusher device is located at the lower section of feed hopper, for the rubbish in feed hopper to be pushed away Enter in gasification furnace, being respectively arranged below with for the lower section of gasification furnace moving hearth and incinerator moving hearth at least one is independently set The air compartment put, windrow seal section, the grate between the gasification furnace and incinerator are provided between the feed hopper, gasification furnace Transition slag section is left on part, the transition slag section is provided with residue pusher, for the rubbish that will be fallen in gasification furnace In residue push-in incinerator；The gasification furnace, incinerator include furnace shell, moving hearth respectively, and the forward and backward side of the gasification furnace is close by windrow respectively Section, the sealing of transition slag section are sealed, the transition slag section isolation gasification furnace, incinerator, makes gasification furnace, incinerator separate；The gasification furnace, incinerator set secondary air feed mouth respectively respectively in arching upward shape on the face arch of the gasification furnace, rear arch, Vault the first exhanst gas outlet of setting of the gasification furnace, vault the second exhanst gas outlet of setting of the incinerator, the gasification furnace, Igniting combustion supporting hole is respectively equipped with incinerator；Also include cavity combustion chamber in any described inverted cone-shapeds of claim 1-4, inverted cone-shaped inner chamber entry of combustion chamber and the One exhanst gas outlet connects；Also include circulation air feed system, the circulation air feed system includes dust arrester, the first blower fan, the second blower fan, described to remove The inlet end of dirt device is connected by pipeline with the second exhanst gas outlet, and the outlet side of the dust arrester passes through pipeline and the first wind The inlet end connection of machine, the outlet side of first blower fan connect the house steward of the first manifold, the branch pipe difference of first manifold Connected with the secondary air feed mouth on each air compartment and gasification trimmer arch, rear arch of the lower section of gasification furnace moving hearth, it is described First regulating valve is set respectively on each branch pipe of the first manifold, the air inlet and atmosphere of second blower fan, described second The gas outlet of blower fan connects the house steward of the second manifold, the branch pipe of second manifold respectively with it is each below incinerator moving hearth The inlet end of air compartment and dust arrester, outlet side are connected, and the second tune is set respectively on each branch pipe of second manifold Save valve, in addition to the 3rd manifold, the house steward of the 3rd manifold connect with the gas outlet of the second blower fan, the 3rd manifold it is each Branch pipe is connected with each combustion air air feed mouth respectively, and the 3rd regulating valve is set respectively on each branch pipe of the 3rd manifold.
- A kind of 6. stoker fired grate formula refuse gasification CIU according to claim 5, it is characterised in that：First discrimination Pipe also has a branch pipe being connected with inverted cone-shaped inner chamber entry of combustion chamber, and the branch pipe is provided with corresponding regulating valve, the first wind The remainder flue gas not utilized that machine extracts is injected into inverted cone-shaped inner chamber by inverted cone-shaped inner chamber entry of combustion chamber and burnt Room, and pass through corresponding regulation valve regulation wind supply quantity.
- A kind of 7. stoker fired grate formula refuse gasification CIU according to claim 6, it is characterised in that：First discrimination Manage the branch pipe being connected with inverted cone-shaped inner chamber entry of combustion chamber and be provided with flue gas amount detecting device, the second flue gas composition detection means, The flue gas amount detecting device, the second flue gas composition detection means and the 3rd regulating valve electrically connect with control unit respectively, institute The synthesis flue gas composition parameter and flue gas amount detecting device for stating control unit processing the second smoke composition detection means collection are adopted The synthesis flue gas flow parameter of collection, and pass through the 3rd governor valve control combustion air wind supply quantity.
- A kind of 8. stoker fired grate formula refuse gasification CIU according to claim 5, it is characterised in that：The dedusting dress It is set to cyclone separator or hot precipitator；First blower fan is high-temperature blower, and second blower fan is air blower.
- A kind of 9. stoker fired grate formula refuse gasification CIU according to claim 5, it is characterised in that：The transition falls Isolating door to be opened/closed is provided with slag section, the isolating door is used to separate gasification furnace, incinerator.
- A kind of 10. stoker fired grate formula refuse gasification CIU according to claim 5, it is characterised in that：The gasification The face arch of stove is flat construction, or, the face arch of gasification furnace is inclined upwardly structure for rear end.
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| CN201610801181.7A CN106224970B (en) | 2016-09-05 | 2016-09-05 | Cavity combustion chamber in stoker fired grate formula refuse gasification CIU and inverted cone-shaped |
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| CN201610801181.7A CN106224970B (en) | 2016-09-05 | 2016-09-05 | Cavity combustion chamber in stoker fired grate formula refuse gasification CIU and inverted cone-shaped |
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| CN112664961B (en) * | 2020-12-23 | 2022-06-17 | 淄博鸿润新材料有限公司 | Kiln for treating high-salinity high-organic-matter wastewater |
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| CN2232107Y (en) * | 1995-08-12 | 1996-07-31 | 郑州锅炉厂 | Reverse combustion type garbage cremation furnace |
| CN2872113Y (en) * | 2005-11-10 | 2007-02-21 | 宜兴市官林工业环保设备厂 | Sludge reversed incinerator |
| CN105465793B (en) * | 2015-12-31 | 2017-10-13 | 重庆科技学院 | Double-deck stoker fired grate formula refuse gasification burns double boiler electricity generation system |
| CN105588131B (en) * | 2015-12-31 | 2017-11-07 | 重庆科技学院 | Stoker fired grate formula refuse gasification incinerator and its double boiler energy-saving power generation system |
| CN206112944U (en) * | 2016-09-05 | 2017-04-19 | 重庆科技学院 | Mechanical stoker formula waste gasification system of burning and inverted cone inner chamber combustion chamber |
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Effective date of registration: 20230315 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 |
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