CN206112945U - Mechanical stoker formula waste gasification system of burning and synthetic gas parameter feedback burner - Google Patents

Abstract

The utility model discloses a mechanical stoker formula waste gasification system of burning and synthetic gas parameter feedback burner, burner's inner chamber include combustion passage, V awl passageway, flying dust deposit room, the taper slag notch that from the top down set gradually and encircle ring -shaped stack gas passage, the annular exhaust uptake that V awl passageway set up, and V awl passageway big -end -up, the diameter of flying dust deposit room are greater than the diameter of V awl passageway upper end, ring -shaped stack gas passage 's ventilation area from the bottom up diminishes gradually, ring -shaped stack gas passage 's lower extreme and flying dust deposit room intercommunication, annular exhaust uptake's lower extreme and ring -shaped stack gas passage 's upper end intercommunication, taper slag notch big -end -up. Using this waste gasification synthetic gas parameter feedback's burner, having higher dust collection efficiency and combustion efficiency, higher heat recycling efficiency can realize controllable burning and controllable collection, reduces the heat loss, and the pollution abatement thing discharges effectively.

Description

Stoker fired grate formula refuse gasification CIU and synthesis gas parameter feedback burner

Technical field

This utility model belongs to solid waste incineration processing technology field, more particularly to a kind of stoker fired grate formula rubbish gas Change CIU and synthesis gas parameter feedback burner.

Background technology

Existing technology of garbage disposal mainly has burning, sanitary landfills, compost, waste recovery etc..In garbage disposal routine In technology, burning disposal has reduced training substantially, and innoxious thorough, occupation of land amount is little, and waste heat energy is obtained by, and secondary pollution is few The advantages of, meet the strategic requirement of China's sustainable development.But with to the continuous improvement of environmental requirement, how strengthening both at home and abroad Control to secondary pollution is particularly important.Therefore, refuse pyrolysis gasification burning technology is gradually shifted onto the road of industrial applications On, all kinds of incineration technologies are primarily now used especially for domestic rubbish, the extensive industrialization of gasification burning technology will The technological innovation for bringing domestic garbage disposal industry is regenerated.

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 of laboratory Plinth research is a lot, also has applied research, such as：Rotary kiln type, vertical and fluidized bed type destructive gasifying or temperature gasification and high melting skill Art etc..But in Technique Popularizing application or there is a definite limitation, 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, wherein having in body of heater using mechanical type backstepping fire grate, forwards fire grate or combined fire grate, also adopts With fire grates such as chain-plate type and drum-types.

In sum, typical incinerator, respectively there is its own advantage, but needs 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 is used, to rubbish Conveying capacity needs emphasis to consider.

2. being on the increase with refuse production, sanitary fill such as mountain, garbage treatment quantity must be effectively improved, Could meeting the market requirement.

3. require in the face of strict pollutant emission, 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 using boiler produce steam shift steam turbine power generation onto, whole transition heat efficiency losses are larger, place Reason identical quantity of refuse, relative thermal losses and the raising heat exchanger effectiveness of reducing can just improve the thermal efficiency.

5. conventional garbage is burned in mode and boiler applications, and high-temperature dust removal is less or does not have, and some efficiency is also not high enough, high Less, the easy dust stratification of boiler that effect dedusting and burning are had both, declines thermal conversion efficiency, and so as to lower power production, maintenance period is short Deng.

The for example following two utility model patents 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 Reason model comparision falls behind, and be simply dried-burns-burns, and solid combustion discharges the process of heat；Thermal chemical reaction is aoxidizing in stove Based on reaction, reduction reaction auxiliary is also easy to produce secondary pollution；When rubbish burns in stove, it is big to cross oxygen quotient, First air, two Secondary wind infeed amount is big, and dust content is higher in flue gas, affects larger to heat reclaiming system and smoke processing system, easily product Ash, exhaust gas volumn is larger, reduces thermal conversion efficiency；The gasification furnace not being separately provided and incinerator, can only by several times process rubbish, Large-scale rubbish continuous gasification burning disposal cannot be realized, garbage treatment quantity is less.

Utility model content

The purpose of this utility model is to overcome the deficiencies in the prior art, there is provided a kind of stoker fired grate formula refuse gasification is burned System and synthesis gas parameter feedback burner, burner efficiency of dust collection, efficiency of combustion are higher, can reduce thermal losses, heat The organic efficiency of amount is higher, and can efficiently reduce pollutant emission.

What the purpose of this utility model was realized in：

A kind of synthesis gas parameter feedback burner, arranges combustion chamber ignition combustion-supporting hole on the top board of the burner, The tangentially-arranged burner entrance of upper end edge of burner side wall, the inner chamber of the burner include from top to bottom according to The burning gallery of secondary setting, V bore passage, flying dust expansion chamber, taper slag notch and the ring smoke around V cone passage settings and lead to Road, annular vent flue, are separated between the ring smoke passage, annular vent flue and V cone passage by annular inducing QI pier, Some combustion airs are arranged on the side wall of the burning gallery supplies air port, each combustion air to be respectively positioned on burner entrance for air port Lower section, V cone passage is up big and down small, the diameter that passage upper end is bored with diameter greater than V of the flying dust expansion chamber, the annular The breathing area of exhaust gases passes is tapered into from top to bottom, and the lower end of ring smoke passage connects with flying dust expansion chamber, the ring The lower end of shape exhaust uptake connects with the upper end of ring smoke passage, and tangential outlet flue is arranged on the side wall of burner with annular Exhaust uptake is connected, and the taper slag notch is up big and down small.

Preferably, the top of the ring smoke passage is circumferentially arranged some up-narrow and down-wide point of gas piers, adjacent point Narrow wide flue gas ring road under being formed between gas pier.

Preferably, the burner entrance is connected to feed the high-temperature flue of high-temperature flue gas, on the high-temperature flue Smoke movement parameter acquisition unit is set, and the burner entrance arranges variable synthesis gas approach, the smoke movement ginseng Counting collection unit includes that sensing is received and signal processing unit, cooling unit, heat-insulated pedestal and sensing element, the heat-insulated pedestal It is fixed on the tube wall of high-temperature flue, the sensing element edge is fixed on heat-insulated pedestal perpendicular to the direction of high-temperature flue axis On, the measurement end of sensing element is stretched in high-temperature flue, and the sensing is received and signal processing unit is fixed on sensing element position One end outside high-temperature flue, the flue gas stream that sensing is received and signal processing unit is measured in high-temperature flue by sensing element Amount, flow velocity, the cooling unit is enclosed in one of sensing element between heat-insulated pedestal, sensing reception and signal processing unit Duan Shang, the variable synthesis gas approach includes actuator, fire resisting bore adjustment seat, one end of the fire resisting bore adjustment seat Stretch in burner entrance, other end connection actuator, also including the first flue gas composition detection means and control unit, institute The first flue gas composition detection means is stated on high-temperature flue for the flue gas composition detected in high-temperature flue, the control list Unit receives with the first flue gas composition detection means, sensing respectively and signal processing unit, actuator are electrically connected, at control unit Reason smoke movement parameter, synthesis flue gas composition parameter, and by the flexible of actuating mechanism controls fire resisting bore adjustment seat, and then control The pore size of the variable synthesis gas approach of system.

Preferably, the 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 the fireproof flue is U-shaped, and the opening of fireproof flue is adjusted by compressing thermal insulation layer sealing, the fire resisting bore Section seat is stretched in fireproof flue through thermal insulation layer is compressed, and fire resisting bore conditioned seat width of one end in fireproof flue is big In fire resisting bore conditioned seat in the width of the outer one end of fireproof flue, arrange between fire resisting bore adjustment seat and fireproof flue side wall Elevated-temperature seal, between fire resisting bore adjustment seat and compression thermal insulation layer heat-insulating and sealing is arranged.

A kind of stoker fired grate formula refuse gasification CIU, including incinerator, the 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 falls the front lower place of cinder notch positioned at gasification furnace, the rear of incinerator for incinerator slag notch, on the grate Garbage pusher device is provided with, 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, being respectively arranged below with for the lower section of gasification furnace moving hearth and incinerator moving hearth at least one is independently arranged once Air compartment, is provided with windrow seal section between the feed hopper, gasification furnace, stay on the grate part between the gasification furnace and incinerator There is transition to fall slag section, the transition slag section that falls is provided with residue pusher, for the rubbish fallen in gasification furnace residue to be pushed In incinerator；

The gasification furnace, incinerator include respectively furnace shell, moving hearth, and the forward and backward side of the gasification furnace passes through respectively heap Material seal section, transition fall the sealing of slag section, and the transition falls slag section isolation gasification furnace, incinerator, makes gasification furnace, incinerator mutually only It is vertical；

The gasification furnace, incinerator are respectively provided with secondary air feed respectively in arching upward shape on the face arch of the gasification furnace, rear arch Mouthful, the vault of the gasification furnace arranges the first exhanst gas outlet, and the vault of the incinerator arranges the second exhanst gas outlet, the gasification Igniting combustion supporting hole is respectively equipped with stove, incinerator；

Also include burner, the burner entrance is connected 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 is by pipeline and the The inlet end connection of one blower fan, the outlet side of first blower fan connects the house steward of the first manifold, the arm of first manifold Connect with the secondary confession air port on each air compartment and gasification trimmer arch, rear arch of the lower section of gasification furnace moving hearth respectively, The first regulating valve is respectively provided with each arm of first manifold, the air inlet and atmosphere of second blower fan are described The gas outlet of the second blower fan connects the house steward of the second manifold, the arm of second manifold respectively with incinerator moving hearth lower section Each air compartment and dust arrester inlet end, outlet side connection, the is respectively provided with each arm of second manifold Two regulating valves, also including the 3rd manifold, the house steward of the 3rd manifold connects with the gas outlet of the second blower fan, the 3rd manifold Each arm connect for air port with each combustion air respectively, be respectively provided with the 3rd regulating valve on each arm of the 3rd manifold.

Preferably, first manifold also has an arm being connected with burner entrance, and the arm is provided with right The regulating valve answered, what the first blower fan was extracted is not injected into burning dress using complete remainder flue gas by burner entrance Put, and by corresponding regulation valve regulation wind supply quantity.

Preferably, the arm that first manifold is connected with burner entrance be provided with flue gas amount detecting device, second Flue gas composition detection means, the flue gas amount detecting device, the second flue gas composition detection means and the 3rd regulating valve respectively with Control unit electrically connect, described control unit process the second flue gas composition detection means collection synthesis flue gas composition parameter and The synthesis flue gas flow parameter of flue gas amount detecting device collection, and by the 3rd governor valve control combustion air wind supply quantity.

In order to effectively to the high-temperature flue gas that incinerator is discharged carry out dedusting, 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 Aerator.

In order to prevent that wind is altered between gasification furnace, incinerator, it is preferable that the transition fall be provided with 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 is inclined upwardly structure for rear end.

As a result of above-mentioned technical proposal, this utility model has the advantages that：

V cone passages are up big and down small, and volume reduces, pressure increase, and flow velocity increase accelerates rotation to inject flying dust expansion chamber, body Product charges into increase, and reduced pressure, flow velocity is reduced, the effect rapid drawdown of cyclone centrifugal power, flying dust sedimentation, and dust removing effects are further；Ring Shape exhaust gases passes flue gas size is gradually reduced, and into trapezoidal flue gas ring road, reduces the sucking-off of flying dust, and dedusting is more favourable；Due to ring The pyramidal structure of shape exhaust gases passes, less the closer to discharge area, flue gas ring road wide at the top and narrow at the bottom is made in ring smoke passage High-temperature flue gas flow velocity is uniform.Burning gallery section cyclonic separation dedusting, back taper passage, flying dust expansion chamber, ring smoke passage, ring road Combination is set and improves efficiency of dust collection, flue gas is synthesized during dedusting and obtains being sufficiently mixed burning, improve efficiency of combustion.

Control unit processes smoke movement parameter (speed, flow, fluid force etc.), synthesis flue gas composition and high-temperature blower and goes out To the flue gas composition and flow of burner, control actuator adjusts gas approach aperture to mouth, while combustion-supporting air quantity is controlled, The regulation of the fluctuations such as unstability is brought in waste component and heat treatment process synthesis exhaust gas volumn and component is realized, so as to Smoke inlet initial velocity and combustion-supporting oxygen-supplying amount are controlled, to reach the purpose of high-effective dust-removing and burning.Control unit control is variable Synthesis gas approach actuator：Purely mechanic transmission, mechanical parameter enlarger, then actuator is driven, execution efficiency is higher.

Aerator blasts air for incinerator and provides First air and provide homoiothermic air feed for cyclone separator, high-temperature blower, By the second regulation valve regulation wind supply quantity on correspondence pipeline, incinerator residue is set fully to burn；Then, high-temperature blower extracts 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 correspondence pipeline, make rubbish in gasification furnace produce gasification, contain one The flue gas of quantitative synthesis gas, discharges from the first exhanst gas outlet, and into burner processing links, burner provides high temperature cigarette Gas.This utility model is novel, and garbage treatment quantity is big, and the rubbish bed of material experiences drying, gasification and residue on stoker fired grate The stage is burnt, the characteristics such as China's house refuse water content height, complicated component are adapted to, the energy that improve in garbage processing procedure turns Change efficiency and reduce pollutant discharge amount in flue gas, effectively prevent secondary pollution, and the continuous gas of large-scale rubbish can be realized Change burning disposal, it is ensured that refuse gasification burns effect and lime-ash clinker ignition loss, relative to reduce thermal losses and improve heat exchanger effectiveness, Improve the 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 the Two exhanst gas outlets, beneficial to according to the difference of flue gas quality flue gas is processed respectively, while being conducive to flue gas ash removal, can be provided more The flue gas of high-quality, makes the utilization rate of flue gas higher, and the waste residue of discharge is less.

Description of the drawings

Fig. 1 is the structural representation of burner；

Fig. 2 is the structural representation of smoke movement parameter acquisition unit；

Fig. 3 is the A-A cross-sectional schematics of Fig. 1；

Fig. 4 is the B-B cross-sectional schematics of Fig. 1；

Fig. 5 is the C-C cross-sectional schematics 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 confession air port, 116 is slag notch, and 117 is the cinder notch that falls；

2 are 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 regulating valve, and 208 is the second regulating valve, and 209 are adjusted for the 3rd Valve；

3 is burner, and 301 is combustion chamber ignition combustion-supporting hole, and 302 is taper slag notch, and 303 is burner entrance, 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 flying dust expansion chamber, 309 is ring smoke passage, and 310 is annular vent flue, and 311 are annular inducing QI pier, and 312 are a point gas pier, and 313 is flue gas circle Road, 314 is high-temperature flue, and 315 receive and signal processing unit for sensing, and 316 is cooling unit, and 317 is heat-insulated pedestal, 318 For sensing element, 319 is actuator, and 320 is fire resisting bore adjustment seat, and 321 is the first flue gas composition detection means, and 322 are Control unit, 323 is fireproof flue, and 324 is heat-insulating and sealing, and 325 to compress thermal insulation layer, and 326 is elevated-temperature seal, and 327 is flue gas Amount detecting device, 328 is the second flue gas composition detection means.

Specific embodiment

It is a kind of preferred embodiment of synthesis gas parameter feedback burner referring to Fig. 1 to Fig. 5, the burner 3 Top board on combustion chamber ignition combustion-supporting hole 301, the tangentially-arranged burner entrance of upper end edge of the side wall of the burner 3 are set 303, the inner chamber of the burner 3 includes burning gallery 306, V cone passage 307, the flying dust sedimentation for setting gradually from top to bottom Room 308, taper slag notch 302 and the ring smoke passage 309, the annular vent flue 310 that arrange around V cone passages 307, institute State and separated by annular inducing QI pier 311 between ring smoke passage 309, annular vent flue 310 and V cone passage 307, the combustion Some combustion airs are set for air port 305, each combustion air is respectively positioned on burner for air port 305 on the side wall in burn through road 306 The lower section of entrance 303, V cone passage 307 is up big and down small, the flying dust expansion chamber 308 with diameter greater than on V cone passages 307 The diameter at end, the breathing area of the ring smoke passage 309 is tapered into from top to bottom, the lower end of ring smoke passage 309 Connect with flying dust expansion chamber 308, the lower end of the annular vent flue 310 connects with the upper end of ring smoke passage 309, described The top of ring smoke passage 309 is circumferentially arranged some up-narrow and down-wide point gas piers 312, shape between adjacent point of gas pier 312 The narrow wide flue gas ring road 313 under.Arrange tangential outlet flue 304 on the side wall of burner 3 to connect with annular vent flue 310 Logical, the taper slag notch 302 is up big and down small.

The burner entrance 303 is connected to feed the high-temperature flue 314 of high-temperature flue gas, the high-temperature flue 314 Upper setting smoke movement parameter acquisition unit, the burner entrance 303 arranges variable synthesis gas approach, the flue gas fortune Dynamic parameter acquisition unit includes that sensing is received and signal processing unit 315, cooling unit 316, heat-insulated pedestal 317 and sensing element 318, the heat-insulated pedestal 317 is fixed on the tube wall of high-temperature flue 314, and the sensing element 318 is along perpendicular to high-temperature flue The direction of 314 axis is fixed on heat-insulated pedestal 317, and the measurement end of sensing element 318 is stretched in high-temperature flue 314, the sense Should receive and signal processing unit 315 is fixed on the one end of sensing element 318 outside high-temperature flue 314, sensing is received and believed Number processing unit 315 measures flue gas flow, flow velocity in high-temperature flue 314, the cooling unit 316 by sensing element 318 Be enclosed in sensing element 318 positioned at heat-insulated pedestal 317, sensing receive and signal processing unit 315 between one section on, it is described every Hot radical seat 317, cooling unit 316 prevent the heat of high-temperature flue 314 from conducting to sensing reception and signal processing unit 315.Institute Stating variable synthesis gas approach includes actuator 319, fire resisting bore adjustment seat 320, and the actuator 319 can adopt gas Cylinder, oil cylinder etc..One end of the fire resisting bore adjustment seat 320 is stretched in burner entrance 303, other end connection actuator 319, also including the first flue gas composition detection means 321 and control unit 322, the first flue gas composition detection means 321 is pacified Being mounted on high-temperature flue 314 is used for the flue gas composition that detects in high-temperature flue 314, described control unit 322 respectively with the first cigarette Gas component detection means 321, sensing are received and signal processing unit 315, actuator 319 are electrically connected, and control unit 322 is processed Smoke movement parameter, synthesis flue gas composition parameter, and the flexible of fire resisting bore adjustment seat 320 is controlled by actuator 319, enter And control the pore size of variable synthesis gas approach.

In the present embodiment, the variable synthesis gas approach also includes that fireproof flue 323, heat-insulating and sealing 324, compression are heat-insulated Layer 325, elevated-temperature seal 326, the fireproof flue 323, elevated-temperature seal 326 can be made using conventional exotic material, it is described every Heat seal 324, compression thermal insulation layer 325 can be made using conventional heat-barrier material.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 fire resisting bore adjustment seat 320 is located at the width of one end in fireproof flue 323 and is more than fire resisting bore Adjustment seat 320 is located at the width of the outer one end of fireproof flue 323, sets 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.

It is a kind of preferred embodiment of stoker fired grate formula refuse gasification CIU referring to Fig. 6, including incinerator 1, the incinerator 1 includes grate 101, and the feed hopper 102, gas set gradually along feedstock direction on grate 101 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 siege 105 of gasification furnace 103 and incinerator 104 is using the independent mechanical kiln for driving of 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 driving means.Machine Used as the carrier of conveying garbage, embodiments thereof can be all types of moving hearths 105 to tool grate-type moving hearth 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 in 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 least one air compartment 107 being independently arranged, in the present embodiment, with gasification furnace The corresponding fire grate of air compartment 107 of 103 first halfs, driving means, as the dryer section of the siege 105 of gasification furnace 103, with gasification The gasification section of the latter half of corresponding fire grate of an air compartment 107 of stove 103, driving means as the siege 105 of gasification furnace 103.Gasification The dryer section of the siege 105 of stove 103, gasification section can be respectively adopted a 1-2 independent air feed of air compartment 107, it is also possible to respectively Using a 3-4 independent air feed of air compartment 107.Certainly, fire grate, driving means and an air compartment 107 also can not be correspondingly arranged, Preferably adjust bed of material movement and air distribution relation on moving hearth 105.Incinerator 104 can adopt 1-4 independent First air The air feed of room 107, burns rear lime-ash and excludes from slag notch, into next step treatment process.

It is provided with windrow seal section 108 between the feed hopper 102, gasification furnace 103, the work of garbage pusher device 106 is entered and located in place In windrow seal section 108, garbage raw material is put into from feed hopper 102 and falls, and garbage pusher device 106 is retreated, then is advanced, reciprocal many Secondary pusher forms windrow in windrow seal section 108, makes the entrance of gasification furnace 103 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, The forward impelling half stroke again of garbage pusher device 106, rubbish is pushed completely in gasification furnace 103, loses the entrance of gasification furnace 103 Windrow sealing effectiveness.Leave transition on the part of grate 101 between the 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 to be pushed into incinerator In 104, the transition slag section 109 that falls can be at windrow sealing state when rubbish residue is piled up, and strengthen the sealing effectiveness of gasification furnace 103, Solve the problems, such as string wind between gasification furnace 103, incinerator 104.In the present embodiment, falls in the transition, and be provided with slag section 109 can The isolating door 111 of opening and closing, the isolating door 111 is used to separate gasification furnace 103, incinerator 104.The furnace lifting initial stage or need control When altering wind between gasification furnace processed 103 and incinerator, isolating door 111 is closed, 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, coordinate to use with the residue pusher 110 that lower section is arranged, to realize that rubbish is continuous Gasification burning process.

, respectively in the shape that arches upward, the face arch of the gasification furnace 103 is for the upper end of the gasification furnace 103, the upper end of incinerator 104 Flat construction, or, the face arch of gasification furnace 103 is inclined upwardly structure for rear end.The vault of the gasification furnace 103 arranges the first cigarette Gas outlet 112, the vault of the incinerator 104 arranges the second exhanst gas outlet 113, and the upper end of the gasification furnace 103 is arched upward, burns Igniting combustion supporting hole 114 is respectively equipped with the arching upward of the upper end of stove 104.Gasification flue gas is from the first exhanst gas outlet 112, the second exhanst gas outlet 113 exclude, and also including burner 3, the burner entrance is connected with the first exhanst gas outlet.The furnace cavity of gasification furnace 103 It is relatively reduced compared with traditional incinerator；Forward and backward arch diminishes with the relative position of moving hearth 105, reduces incinerator The space of occupancy, is also easier to insulation, reduces the amount of leakage of heat, is conducive to rubbish fully to gasify.The gasification furnace 103 Secondary confession air port 115 is respectively provided with face arch, 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 is 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 aerator.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 is by pipeline and the The inlet end connection of one blower fan 202, the outlet side of first blower fan 202 connects the house steward of the first manifold 204, first discrimination The arm of pipe 204 each air compartment 107 and the face arch of gasification furnace 103 respectively with the lower section of the moving hearth 105 of gasification furnace 103, Secondary confession air port 115 on rear arch connects, and the first regulating valve 207 is respectively provided with each arm of first manifold 204, 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 In the corresponding air compartment 107 in the lower section of dynamic siege 105, then by an air holes spray penetration rubbish on moving hearth 105, enter Circulation of qi promoting, by the first regulating valve 207 on each arm of correspondence wind supply quantity is adjusted.The secondary wind of gasification furnace 103 is that high-temperature blower is taken out The flue gas for taking incinerator 104 produces certain pressure and blasts 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 confession air port 115 is provided with forward and backward arch, gasification efficiency is improved, is strengthened polymer substance in flue gas and is decomposed.Afterwards Igniting combustion supporting hole 114 is provided with arch, temperature is used in furnace lifting, baker and stable gasification furnace 103, by the on each arm of correspondence 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 is blasted 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 the arm of the second manifold 205 respectively with each air compartment 107 and dust arrester of the lower section of 104 moving hearth of incinerator 105 201 inlet end, outlet side connection, is respectively provided with the second regulating valve 208 on each arm of second manifold 205.Incinerator 104 First airs are that the air of certain pressure is blasted the corresponding air compartment in the lower section of stoker fired grate formula moving hearth 105 by aerator In 107, then by an air holes spray penetration residue on moving hearth 105, residual burning is carried out, by each arm of correspondence The first regulating valve 207 adjust wind supply quantity.The inlet end of dust arrester 201, the air intake of outlet side be homoiothermic air feed, homoiothermic air feed It is that the air of certain pressure is blasted incinerator 104 and export (i.e. cyclone inlet) and carries out homoiothermic by aerator, meanwhile, whirlwind Separator outlet (i.e. high-temperature blower entrance) blasts further homoiothermic, is adjusted by the first regulating valve 207 on each arm of correspondence 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 arm of the 3rd manifold 206 is connected respectively with each combustion air for air port 305, is respectively provided with each arm of the 3rd manifold 206 3rd regulating valve 209.Burner entrance 303 and combustion-supporting confession air port are arranged in the circumferential wall of burner 3, can be combustions The flue gas burnt in device 3 is longer with air mixture time, and mixing is more uniformly distributed, and more fully burns.The combustion-supporting confession of burner 3 Wind is that the air of certain pressure is blasted combustion-supporting confession air port and is injected into burner 3 by aerator, and combustion-supporting air feed approach axis can Being radially or tangentially；Carry out syngas combustion.Meanwhile, high-temperature blower extracts the flue gas of incinerator 104 and produces certain pressure drum Enter two on the corresponding air compartment 107 in the lower section of 103 stoker fired grate formula moving hearth of gasification furnace 105 and the forward and backward arch of gasification furnace 103 Secondary air compartment, first manifold 204 also has an arm being connected with burner smoke inlet, and the arm is provided with correspondence Regulating valve.What high-temperature blower was extracted has not utilized remainder flue gas, then is injected into combustion by the smoke inlet of burner 3 Device 3 is burnt, syngas combustion is carried out, by corresponding regulation valve regulation wind supply quantity, this structure can reduce thermal losses and raising Heat exchanger effectiveness, substantially increases the organic efficiency of heat, and can efficiently reduce pollutant discharge amount.

Further, the arm that first manifold is connected with burner entrance be provided with flue gas amount detecting device 327, Second flue gas composition detection means 328, the flue gas amount detecting device, the second flue gas composition detection means and the 3rd regulating valve Electrically connect with control unit respectively, described control unit processes 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 by the 3rd governor valve control combustion air wind supply quantity.

The incinerator 104 is provided with cinder notch 117, and the slag notch 116 of the incinerator 104 falls cinder notch positioned at incinerator 117 underface, it is described fall cinder notch 117 connected with the slag notch of dust arrester 201 by pipeline.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, the method is carried out according to the following steps：

Step A, the gate for closing stoker fired grate formula refuse gasification incinerator 1 and atmospheric vent, start mechanical grate-type rubbish Rubbish incinerator 1, by garbage raw material feed hopper 102 is put into, and the pusher back and forth of garbage pusher device 106 will be from feed hopper 102 The garbage raw material for falling pushes the windrow seal section 108 between feed hopper 102, gasification furnace 103, forms windrow seal section 108 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 is conveyed into into transition to fall slag section 109, the pusher back and forth of residue pusher 110, the transition rubbish in slag section 109 that falls is 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 piled up can protect mobile stove Bed 105, prevents scaling loss siege 105.Stop being fed 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, treats that this process stabilization is completed, and makes gasification furnace 103 and the burner hearth of incinerator 104 reach 600-700 DEG C of predetermined temperature；Baker Purpose be in order to remove lining in Natural Water and water of crystallization, in order to avoid when going into operation because furnace temperature rises too fast, moisture is a large amount of Expansion causes body of heater spalling, bubbling or deformation even furnace wall to collapse, and affects the intensity and service life of heating furnace furnace wall.

Step B, startup adjust circulation air feed system 2, adjust gasification furnace 103, incinerator 104 and circulation air feed system 2 Technological parameter (pusher speed, fire grate speed, pathogenic wind-warm, blast and an 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 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 piled up to form windrow sealing at transition falls 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, each technological parameter (the pusher speed for adjusting 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 an air quantity, secondary air temperature, blast and air quantity, furnace temperature, stove Deng), gasification furnace 103 gradually gasifies to rubbish, and gasification temperature is stable between 700-800 DEG C, gasification furnace 103 is stably produced The raw high-temperature flue gas containing 10%-20% synthesis gas, it is equal that the vaporized state of gasification furnace 103 stably carries out low temperature, middle temperature or high-temperature gasification Can.Make the fired state temperature stabilization of incinerator 104 to more than 850 DEG C, realize rubbish continuous gasification burning disposal；Need to adjust simultaneously Each technological parameter of burner 3, makes the tangential temperature stabilization of outlet flue 304 of burner 3 to more than 850 DEG C.

Step D, need to overhaul or during blowing out, stop feeding intake, adjust gasification furnace 103, incinerator 104 and circulation air feed system 2 technological parameter, 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 adjusting burner 3 simultaneously is needed, gasification furnace is made 103 are gradually restored to fired state.

Finally illustrate, preferred embodiment above is only unrestricted to illustrate the technical solution of the utility model, to the greatest extent Gutron crosses above preferred embodiment and this utility model is described in detail, but those skilled in the art should manage Solution, can make in the form and details various changes, without departing from this utility model claims institute to it The scope of restriction.

Claims (10)

1. a kind of synthesis gas parameter feedback burner, it is characterised in that：Combustor point is set on the top board of the burner Fiery combustion-supporting hole, the tangentially-arranged burner entrance of upper end edge of burner side wall, the inner chamber of the burner includes Burning gallery, V cone passages, flying dust expansion chamber, taper slag notch and the circular V for setting gradually from top to bottom bores what passage was arranged Ring smoke passage, annular vent flue, by annular between the ring smoke passage, annular vent flue and V cone passage Inducing QI pier separates, and some combustion airs is arranged on the side wall of the burning gallery and supplies air port, each combustion air to be respectively positioned on for air port The lower section of burner entrance, V cone passage is up big and down small, and the flying dust expansion chamber bores passage upper end with diameter greater than V Diameter, the breathing area of the ring smoke passage is tapered into from top to bottom, and lower end and the flying dust of ring smoke passage are settled Room connects, and the lower end of the annular vent flue connects with the upper end of ring smoke passage, arranges on the side wall of burner and cut Connect with annular vent flue to outlet flue, the taper slag notch is up big and down small.

2. a kind of synthesis gas parameter feedback burner according to claim 1, it is characterised in that：The ring smoke leads to The top in road is circumferentially arranged some up-narrow and down-wide point gas piers, narrow wide flue gas circle under being formed between adjacent point of gas pier Road.

3. a kind of synthesis gas parameter feedback burner according to claim 1, it is characterised in that：The burner enters Mouth is connected to feed the high-temperature flue of high-temperature flue gas, and smoke movement parameter acquisition unit is arranged on the high-temperature flue, described Burner entrance arranges variable synthesis gas approach, and the smoke movement parameter acquisition unit is included at sensing reception and signal Reason unit, cooling unit, heat-insulated pedestal and sensing element, the heat-insulated pedestal is fixed on the tube wall of high-temperature flue, the sense Answer element along being fixed on heat-insulated pedestal perpendicular to the direction of high-temperature flue axis, the measurement end of sensing element stretches into high-temperature flue Interior, the sensing is received and signal processing unit is fixed on the one end of sensing element outside high-temperature flue, and sensing is received and believed Number processing unit measures flue gas flow, flow velocity in high-temperature flue by sensing element, and the cooling unit is enclosed in sensing unit Part is located on a section between heat-insulated pedestal, sensing reception and signal processing unit, and the variable synthesis gas approach includes holding Row mechanism, fire resisting bore adjustment seat, one end of the fire resisting bore adjustment seat is stretched in burner entrance, and other end connection is held Row mechanism, also including the first flue gas composition detection means and control unit, the first flue gas composition detection means is arranged on height Be used to detecting flue gas composition in high-temperature flue on warm flue, described control unit respectively with the first flue gas composition detection means, Sensing is received and signal processing unit, actuator electrical connection, and control unit processes smoke movement parameter, synthesis flue gas composition ginseng Number, and by the flexible of actuating mechanism controls fire resisting bore adjustment seat, and then control the pore size of variable synthesis gas approach.

4. a kind of synthesis gas parameter feedback burner according to claim 3, it is characterised in that：The variable synthesis cigarette Gas import also includes fireproof flue, heat-insulating and sealing, compresses thermal insulation layer, elevated-temperature seal, and the cross section of the fireproof flue is U-shaped, The opening of fireproof flue stretches into fireproof flue by compressing thermal insulation layer sealing, the fire resisting bore adjustment seat through thermal insulation layer is compressed Interior, the width of described fire resisting bore conditioned seat one end in fireproof flue is more than fire resisting bore conditioned seat outside fireproof flue The width of one end, arranges elevated-temperature seal, fire resisting bore adjustment seat and compression between fire resisting bore adjustment seat and fireproof flue side wall Heat-insulating and sealing is set between thermal insulation 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 along feedstock direction on grate, the rear of gasification furnace is The cinder notch that falls of gasification furnace, incinerator falls the front lower place of cinder notch positioned at gasification furnace, the rear of incinerator for incinerator slag notch, 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 independently sets The air compartment put, is provided with windrow seal section, the grate between the gasification furnace and incinerator between the feed hopper, gasification furnace Leave transition on part to fall slag section, the transition slag section that falls is provided with residue pusher, for the rubbish that will be fallen in gasification furnace Residue is pushed in incinerator；

The gasification furnace, incinerator include respectively furnace shell, moving hearth, and the forward and backward side of the gasification furnace is close by windrow respectively Envelope section, transition fall the sealing of slag section, and the transition falls slag section isolation gasification furnace, incinerator, makes gasification furnace, incinerator separate；

The gasification furnace, incinerator are respectively provided with secondary confession air port respectively in arching upward shape on the face arch of the gasification furnace, rear arch, Vault first exhanst gas outlet of setting of the gasification furnace, vault second exhanst gas outlet of setting of the incinerator, the gasification furnace, Igniting combustion supporting hole is respectively equipped with incinerator；

Also include the arbitrary described burner of claim 1-4, the burner entrance is connected 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, 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 is by pipeline and the first wind The inlet end connection of machine, the outlet side of first blower fan connects the house steward of the first manifold, the arm difference of first manifold Connect with the secondary confession air port on each air compartment and gasification trimmer arch, rear arch of the lower section of gasification furnace moving hearth, it is described It is respectively provided with the first regulating valve on each arm 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 arm of second manifold respectively with incinerator moving hearth below it is each The inlet end of air compartment and dust arrester, outlet side connection, on each arm of second manifold the second tune is respectively provided with Section valve, also including the 3rd manifold, the house steward of the 3rd manifold connects with the gas outlet of the second blower fan, the 3rd manifold it is each Arm is connected respectively with each combustion air for air port, and on each arm of the 3rd manifold the 3rd regulating valve is respectively provided with.

6. a kind of stoker fired grate formula refuse gasification CIU according to claim 5, it is characterised in that：First discrimination Pipe also has an arm being connected with burner entrance, and the arm is provided with corresponding regulating valve, what the first blower fan was extracted Burner is not injected into by burner entrance using complete remainder flue gas, and by corresponding regulation valve regulation Wind supply quantity.

7. a kind of stoker fired grate formula refuse gasification CIU according to claim 6, it is characterised in that：First discrimination The arm that pipe is connected with burner entrance is 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 are electrically connected respectively with control unit, and the control is single Unit processes the synthesis of the synthesis flue gas composition parameter of the second flue gas composition detection means collection and the collection of flue gas amount detecting device Flue gas flow parameter, and by the 3rd governor valve control combustion air wind supply quantity.

8. a kind of 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 aerator.

9. a kind of 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.

10. a kind of 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.