CN108730985A - A kind of drying unit of refuse pyrolysis gasification furnace - Google Patents

A kind of drying unit of refuse pyrolysis gasification furnace Download PDF

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Publication number
CN108730985A
CN108730985A CN201810574556.XA CN201810574556A CN108730985A CN 108730985 A CN108730985 A CN 108730985A CN 201810574556 A CN201810574556 A CN 201810574556A CN 108730985 A CN108730985 A CN 108730985A
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CN
China
Prior art keywords
drying
drying unit
air
pyrolysis gasification
gasification furnace
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Pending
Application number
CN201810574556.XA
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Chinese (zh)
Inventor
李智
孙强林
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Shanghai Ancient Blue Environmental Engineering Co Ltd
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Shanghai Ancient Blue Environmental Engineering Co Ltd
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Priority to CN201810574556.XA priority Critical patent/CN108730985A/en
Publication of CN108730985A publication Critical patent/CN108730985A/en
Pending legal-status Critical Current

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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/02Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
    • F23G5/027Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage
    • F23G5/0276Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage using direct heating
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/02Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
    • F23G5/04Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment drying
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/08Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating
    • F23G5/14Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating including secondary combustion
    • F23G5/16Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating including secondary combustion in a separate combustion chamber
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/44Details; Accessories
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/44Details; Accessories
    • F23G5/46Recuperation of heat

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Gasification And Melting Of Waste (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

The invention discloses a kind of drying units of refuse pyrolysis gasification furnace.The drying unit of refuse pyrolysis gasification includes recycling connected drying unit, fan house, pyrolysis gasification furnace, dual firing chamber and heat exchanger successively, drying unit includes drying material pond, air compartment, discharge pipe and blast pipe, the air compartment is multiple, multiple air compartments are located at the outer pars intramuralis of the drying material pond, blast pipe is connected with the hot air outlet of heat exchanger, hot wind is entered from the blast pipe in air compartment, is then entered in the drying material pond from discharge pipe.The drying structure of the present invention can allow rubbish directly to be contacted with hot wind, save drying time, in the case where consuming energy without increasing, drying efficiency is obviously improved, the energy is saved, and percolate has also obtained effective evaporation, ensure that refuse pyrolysis gasification furnace stablizes gasification, the firing rate for accelerating rubbish improves the production capacity of garbage disposal.

Description

A kind of drying unit of refuse pyrolysis gasification furnace
Technical field
The present invention relates to technical field of waste treatment, more particularly to a kind of drying unit of refuse pyrolysis gasification furnace.
Background technology
As process of modernization constantly accelerates, crude waste waste discharge capacity is growing day by day, traditional garbage disposal Method causes serious soil and atmosphere pollution, it is difficult to adapt to sustainable development, rubbish is often used in current many garbage disposals Rubbish pyrolysis gasifying device carries out it pyrolysis and carbonization at low temperature gasification, makes organic matter using the thermal instability of organic matter in garbage The process that cracking forms various new fuel gas is generated, it is more environmentally-friendly compared to burning method, realize that sustainable energy utilizes.But mesh The refuse pyrolysis gasification installation of preceding mainstream in the market is primarily present following disadvantage:
Drying structure, it is traditional one is being dried in stove, one is the drum-type drying equipment of pretreating zone, dried in stove The shortcomings that be that the refuse gasification time is slow, and after rubbish enters in stove, with temperature rise, a large amount of vapor generates, meeting The combustible gas for diluting refuse pyrolysis generation, causes the temperature of dual firing chamber to decline.And drum-type drying equipment because be hot wind into Chuck is dried, and is dried rubbish through steel plate, is not in direct contact with rubbish, and drying efficiency is low, and thermal losses is very big, and dries The operating cost of equipment is also big, and landfill leachate also bad processing.
It slags tap structure, every suit incinerator is required for slagging tap, and artificial slags tap from initial to current rotary fire grate, machine Tool fire grate is slagged tap mode, is manually slagged tap dangerous big, and the feature of environmental protection is poor, and rotary fire grate, which is slagged tap, or stoker fired grate is slagged tap has investment Greatly, corollary equipment is more, the high problem of operating cost.Because the continuous operation of slag-tapping system, there is also do not burn for traditional slag-tapping system The phenomenon that saturating slag comes out, and bulk clinker is but unable to come down lives slag notch by water seal when due to slagging tap and realizes that sealing, clinker are fallen In puddle, vapor is big in workshop, and stink is big, and sewage, sludge are difficult, be easy to cause secondary pollution.
Fire grate is the critical piece of pyrolysis gasification furnace, but the fire grate generally existing currently used for pyrolysis gasification furnace is manufactured into This height cannot manufacture again very complicated to the problem of supplying oxygen of burning, although some increase some improvement in functionality.
Feed intake structure, and conventionally employed is open type charging, even if some occasions are in security consideration and also take closing It feeds, but still without solving sealing problem, having air while charging or work enters pyrolysis gasification furnace, causes non-negative Work is pressed, has smoke spillage during pyrolytic gasification, affects pyrolytic gasification effect, also have gas explosion sometimes.
Fire observation device, common fire observation device is usually by flame-observing hole transparent cover cap, asbestos rubber pad, pyroceram piece, sight fire The compositions such as hole pipe have an other burner glass surface of seeing in order to prevent to cover tar, dust, have installed baffle additional.Disadvantage: (1) dust protection baffle influences observation sight.Dust protection baffle is typically all to be mounted on the center for seeing fire tube, affects observation Sight.(2) without provision for thermal insulation, the generation of safety accident is easily led to.Seeing fire tube is directly protruding into kiln, and metal material is usually selected Material makes, and heat conduction is fast, and entire fire observation device can be made to form high temperature, is be easy to cause during the uses such as observation, replacement glass boiling hot Hinder safety accident.(3) it is narrow to see fiery visual angle.Sight fire tube is straight tube structure so that the fiery visual angle of sight is narrow, and the range for seeing fire is small.
External air flue, the common typically no independent gas flue of gasification furnace is all air-introduced machine under the action of air-introduced machine, directly The gasification layer from rubbish is connect, gasification furnace is extracted out by each layer of rubbish.Also a small amount of gasification furnace sets built-in air flue, but due to It is influenced that flue gas can be caused to burn in gasification furnace by in-furnace temperature, affects gasification result, while built-in air flue also affects The working conditions such as spice of the rubbish in gasification furnace.Shortcoming and defect:(1) flow of flue gas speed is slow.Due to by gasification layer upper layer The influence of rubbish stacking pressure causes flue gas discharge to be obstructed, and circulation is unsmooth, and draw speed is slow.(2) gasification efficiency is low.Due to flue gas stream Logical unsmooth, flowing velocity is slow, and leading to the combustible gas for gasifying, some has just been burned off in gasification furnace, causes simultaneously The in-furnace temperature that gasifies is excessively high, and adverse effect is caused to gasification result.(3) fume treatment effect is influenced, by flow of flue gas speed Slowly, the low influence of gasification efficiency, the flammable tolerance that flue gas enters combustion chamber is inadequate, causes chamber temperature too low, has in flue gas Evil ingredient cannot be destroyed, and influence the effect of fume treatment.
Invention content
According to an aspect of the invention, there is provided a kind of drying unit of refuse pyrolysis gasification furnace, including recycle successively Connected drying unit, fan house, pyrolysis gasification furnace, dual firing chamber and heat exchanger,
Drying unit includes drying material pond, air compartment, discharge pipe and blast pipe, and the air compartment is multiple, and multiple air compartments are located at The outer pars intramuralis of the drying material pond, blast pipe are connected with the hot air outlet of heat exchanger, and hot wind enters from the blast pipe Into air compartment, then entered in the drying material pond from discharge pipe.Advantage is that drying structure can allow rubbish direct It is contacted with hot wind, saves drying time.Heat-exchanger rig keeps the heat exchanged in flue gas cooling procedure empty for rubbish drying Gas is fully used, and in the case where consuming energy energy without increasing, drying efficiency is obviously improved, and percolate Effective evaporation has been obtained, ensure that refuse pyrolysis gasification furnace stablizes gasification, accelerate the firing rate of rubbish, improve rubbish The production capacity of processing, has saved the energy.
Heat exchanger is the heat-exchanger rig that fume treatment is used for flue gas cool-down in the process, and main purpose is for fume treatment Flue gas cooling in the process.Heat exchanger is equipped with inlet of cold air, exhanst gas outlet and hot air outlet, dual firing chamber and heat exchanger phase Connection, the hot air outlet are connected with the drying unit.
The drying unit of above-mentioned refuse pyrolysis gasification, advantage is that drying unit carries out rubbish to dry pre- place Reason, the foul smell etc. for drying generation is extracted by fan house in pyrolysis gasification furnace, the rubbish of drying be transferred in pyrolysis gasification furnace into It goes and is pyrolyzed, be pyrolyzed flue gas of generation etc. and be all pumped down to progress fully burning generation heat in dual firing chamber, into heat exchanger, with cold sky Gas exchanges heat, and becomes to enter after hot-air then to dry Other Waste in drying unit, is recycled with this, take full advantage of rubbish The gas and energy generated during rubbish pyrolytic gasification, significantly reduces environmental pollution, more environmentally-friendly, and sustainable use provides Source meets the environmental protection concept of sustainable development.
In some embodiments, drying unit further includes driving grab bucket, and driving grab bucket includes drive a vehicle grab bucket portion and track, Driving grab bucket portion can be moved along track, and track is located at the top of drying unit, fan house and pyrolysis gasification furnace.It is beneficial to effect Fruit is that the rubbish in pond is periodically stirred in driving grab bucket under operator control, reaches better drying effect;And grab bucket can The rubbish of drying is transferred into sealed feeder unit.
In some embodiments, drying unit region is the pretreatment workshop of sealing, at it close to fan house one Side is equipped with air-inlet window, and hollow out filter screen is housed on air-inlet window, and interface channel is closed structure between fan house and pyrolysis gasification furnace. Advantage is that wind turbine indoor primary air fan after overfire air fan starts, continuously pulls the smelly of pretreatment workshop Gas forms tiny structure, prevents foul smell excessive.Hollow out filter screen is to prevent wind turbine from sucking rubbish solid, and outside has vehicle to send rubbish Rubbish is fed, and is opened pretreated electrically operated gate, is then shut after car charging, garbage truck starts to unload rubbish to drying pool, unsnatches it Afterwards, gate is opened, garbage truck exits, and gate is shut automatically, because being negative pressure state, the keying gate of short time does not have smelly Gas escapes, and ensure that plant environment free from extraneous odour.
In some embodiments, air compartment includes being located at drying material pond side wall and bottom two.Positioned at the rubbish of drying material pond The water of rubbish exudation is dropped onto from bottom discharge pipe in the air compartment of bottom, and the water of exudation is oven-dried in turn.Blast pipe be located at The air compartment of bottom is connected to, and blast pipe is located at bottom surface of the height higher than bottom plenum of the indoor end of wind.
More than, drying structure of the invention can allow rubbish directly to be contacted with hot wind, save drying time, without increasing In the case of adding energy consumption, drying efficiency is obviously improved, and has saved the energy, and percolate has also obtained effective steaming Hair ensure that refuse pyrolysis gasification furnace stablizes gasification, accelerate the firing rate of rubbish, improve the production capacity of garbage disposal.
Description of the drawings
Fig. 1 is a kind of overall structure diagram of the drying unit of refuse pyrolysis gasification furnace of an embodiment of the present invention;
Fig. 2 is a kind of structural schematic diagram of the pyrolysis gasification furnace of the drying unit of refuse pyrolysis gasification furnace shown in Fig. 1;
Fig. 3 is a kind of structural schematic diagram of the drying unit of the drying unit of refuse pyrolysis gasification furnace shown in FIG. 1;
Fig. 4 is a kind of structural schematic diagram of the deslagging device of the drying unit of refuse pyrolysis gasification furnace shown in Fig. 2;
Fig. 5 is a kind of structural schematic diagram of the fire grate device of the drying unit of refuse pyrolysis gasification furnace shown in Fig. 2;
Fig. 6 is that a kind of another angled arrangement of the fire grate device of the drying unit of refuse pyrolysis gasification furnace shown in fig. 5 shows It is intended to;
Fig. 7 is a kind of structural schematic diagram of the sealed feeder unit of the drying unit of refuse pyrolysis gasification furnace shown in Fig. 2;
Fig. 8 is a kind of cross section structure of the sealed feeder unit of the drying unit of refuse pyrolysis gasification furnace shown in Fig. 2 Schematic diagram;
Fig. 9 is a kind of cross section structure schematic diagram of the fire observation device of the drying unit of refuse pyrolysis gasification furnace shown in Fig. 2;
Figure 10 is a kind of overall structure signal of fire observation device of the drying unit of refuse pyrolysis gasification furnace shown in Fig. 2 Figure;
Figure 11 is a kind of structural representation of the external airway device of the drying unit of refuse pyrolysis gasification furnace shown in Fig. 2 Figure;
Figure 12 is a kind of structure of a side of the fire grate device of the drying unit of refuse pyrolysis gasification furnace shown in fig. 5 Schematic diagram;
Figure 13 is a kind of knot of another side of the fire grate device of the drying unit of refuse pyrolysis gasification furnace shown in fig. 5 Structure schematic diagram.
Specific implementation mode
The invention will now be described in further detail with reference to the accompanying drawings.
Fig. 1~Figure 13 schematically shows a kind of a kind of refuse pyrolysis gasification furnace of embodiment according to the present invention Drying unit.As shown, the drying unit of refuse pyrolysis gasification includes recycling connected drying unit 1, fan house successively 2, pyrolysis gasification furnace 3, dual firing chamber 4 and heat exchanger 5, pyrolysis gasification furnace 3 include burner hearth 31, sealed feeder unit 32, fire grate device 35, fire observation device 34, deslagging device 36 and external airway device 33, burner hearth 31 are located at the inside of the pyrolysis gasification furnace 3, sealing Feeding equipment 32 is located at the top of pyrolysis gasification furnace 3, and fire grate device 35 is horizontally placed on the middle part of burner hearth 31, fire observation device 34 In on the outer wall of pyrolysis gasification furnace 3, deslagging device 36 is located at the bottom of pyrolysis gasification furnace 3, and heat exchanger 5 is equipped with inlet of cold air 51, exhanst gas outlet 53 and hot air outlet 52, dual firing chamber 4 are connected with heat exchanger 5, the hot air outlet 52 and the drying Device 1 is connected.
Rubbish is carried out drying pretreatment, dries generation by the drying unit of above-mentioned refuse pyrolysis gasification, drying unit 1 Foul smell etc. is extracted by fan house 2 in pyrolysis gasification furnace 3, and the rubbish of drying, which is transferred in pyrolysis gasification furnace 3, to be pyrolyzed, pyrolysis Flue gas of generation etc. is all pumped down in dual firing chamber 4 the generation heat that fully burn and is changed into heat exchanger 5 with cold air Heat, the hot-air after heat exchange are entered in drying unit 1 and then dry Other Waste, recycled with this, and rubbish heat is taken full advantage of The gas and energy that solution gasification generates in the process, significantly reduce environmental pollution, more environmentally-friendly, and sustainable use resource, symbol Close the environmental protection concept of sustainable development.
Drying unit 1 includes drying material pond 11, air compartment 12, discharge pipe 14 and blast pipe 13, the air compartment 12 be it is multiple, it is more A air compartment 12 is located at the outer pars intramuralis of the drying material pond 11, and blast pipe 13 is connected with the hot air outlet 52 of heat exchanger 5, heat Wind is entered from the blast pipe 13 in air compartment 12, is then entered in the drying material pond 11 from discharge pipe 14.Drying unit 1 Further include driving grab bucket, driving grab bucket includes grab bucket portion 15 and track 16, and grab bucket portion 15 can be moved along track 16, track 16 Positioned at the top of drying unit 1, fan house 2 and pyrolysis gasification furnace 3.Air compartment 12 includes being located at drying 11 side wall of material pond and bottom two Place.Water positioned at the rubbish exudation of drying material pond 11 is dropped onto from bottom discharge pipe 14 in the air compartment 12 of bottom, exudation Water is oven-dried in turn.Blast pipe 13 is connected to the air compartment 12 positioned at bottom, and the height that blast pipe is located at the end in air compartment 12 is high In the bottom surface of bottom plenum 12.1 region of drying unit is the pretreatment workshop of sealing, can be opened up at the top of pretreatment workshop For the opening of driving grab bucket disengaging, it is equipped with air-inlet window 10 close to 2 side of fan house at it, hollow out filter screen is housed on air-inlet window 10 101, interface channel is closed structure between fan house 2 and pyrolysis gasification furnace 3.Driving grab bucket is periodically turned under operator control Rubbish in dynamic pond, reaches better drying effect;And the rubbish of drying can be transferred into sealed feeder unit 32 by grab bucket In.Primary air fan in fan house 2 after overfire air fan starts, continuously pulls the foul smell of pretreatment workshop, forms Tiny structure, foul smell will not be excessive.Outside has vehicle to send garbage feeding, opens pretreated electrically operated gate, is then shut after car charging, Garbage truck starts to unload rubbish to drying pool, after unsnatching, opens gate, garbage truck exits, and gate is shut automatically, because being negative pressure State, the keying gate of short time do not have foul smell effusion, while supplementing fresh air for workshop, ensure that plant environment is no different Taste.Drying structure can allow rubbish directly to be contacted with hot wind, save drying time, in the case where not increasing energy consumption, drying Efficiency is obviously improved, and has saved the energy, and percolate has also obtained effective evaporation, ensure that refuse pyrolysis gasifies Stove 3 stablizes gasification, accelerates the firing rate of rubbish, improves the production capacity of garbage disposal.
Deslagging device 36 includes residue outlet 361, hydraulic cylinder 362, push-rod piston 363, broken slag device 364 and mobile sealing Slag case 365, the lower section of fire grate device 35 are equipped with slag bucket 312, and 312 lower section of slag bucket is equipped with slag mouth 3615, slag mouth 3615 with go out Slag pipe 361 is connected, and hydraulic cylinder 362 is connected with push-rod piston 363, and air inlet is equipped with above one end of residue outlet 361 3611, broken slag device 364 is located at the top of the other end of residue outlet 361, and the side of broken slag device 364 is provided with air outlet 3612, goes out Air port 3612 is connected with slag bucket 312, and the other end of residue outlet 361 is equipped with slag notch 3613, and slag notch 3613 is equipped with backplate 3614, the length of the setting corresponding with mobile sealing slag case 365 of slag notch 3613, push-rod piston 363 is more than slag mouth 3615 Length.Residue outlet 361 is round or rectangular or polygon, is fixed on the bottom of 31 rectangle slag bucket of burner hearth, position of opening with Rectangle slag mouth 3615 coincide, and makees rigid sealed connection, and movable push bar piston 363 is slightly larger than the length of rectangle slag mouth 3615 Degree, closely agrees with, width is fully met, when the push-rod piston 363 because the push-rod piston 363 and residue outlet 361 belong to Extreme position is opened, just seals rectangle slag notch 3613 completely, forms sealing.After the promotion of push-rod piston 363 is slagged tap, clinker Mobile sealing slag case 365 is fallen into, push-rod piston 363 to extra undischarged clinker between slag notch is stored in residue outlet 361, As sealing, prevent extraneous air from entering in burner hearth.And the tube head position in 361 hydraulic cylinder of residue outlet, 362 direction is equipped with sealing Air inlet 3611, connect, continually blow into residue outlet 361, First air is by slagging tap with the primary air fan in fan house 2 Pipe 361 is blown into an open piston, then is sent into burner hearth 31 (air outlet can also install baffle additional), Er Qieyi by air outlet 3612 It is directly in blowing state, blocking will not be formed, ensures the air quantity supply of burner hearth 31, while in turn ensuring the cold of this deslagging device 36 But during refuse gasification, the big inorganic matter of weight first falls into bottom, and it is dirt, brick, stone that result in bottom, which be major part, The inorganic matters such as block, so bottom temp is very low relative to 31 temperature of burner hearth, generally at 80 DEG C or so, while cold wind passes through residue outlet 361 heat exchange action, the wind for being sent into burner hearth 31 become hot wind, play the role of air preheater, ensure that temperature, subtract Energy expenditure is lacked and has not only solved that traditional slag-tapping system is numerous and jumbled, and ancillary equipment is more, energy consumption is big, the high problem of O&M cost, also The problem of solving stifled slag, preventing secondary pollution realizes simplicity reliably, and O&M cost is low, slags tap quantitative, smooth, burns thorough Bottom, the low effect of burn decrement rate.
Fire grate device 35 includes fire grate 351, fire grate axis 352, driving unit 353 and cooling unit, and fire grate 351 is multiple flat Row setting, cooling unit include that cooling water inlet pipe 354 and cooling water outlet pipe 355, fire grate 351 are located on fire grate axis 352, and driving is single Member 353 is connected with fire grate axis 352, and fire grate 351 is equipped with multiple air ventilation holes 3511.Fire grate 351 is installed on pyrolytic gasification Bearing 3531 is installed at 3 burning position bottom of stove, two ends, the rotation support overturn as fire grate 351.Fire grate axis 352 is using hollow Structure, water receiving pipe in parallel therebetween cool down fire grate 351 by cooling water, to protect fire grate 351, fire grate axle bearing 3531 It can work normally at high temperature.351 ontology working face of fire grate designs multiple air ventilation holes 3511, is used for air air feed.Fire grate Driving device is installed at 352 end of axis, drives 351 rotary work of fire grate.Driving unit 353 includes bearing 3531, gear 3532, rack 3533, oil cylinder 3534 and cylinder bracket 3535, the oil cylinder 3534 are located on cylinder bracket 3535,3534 sliding tooth of the oil cylinder Item 3533 drives the rotation of the gear 3532, the gear 3532 to drive the rotation of the bearing 3531, the bearing 3531 Drive the overturning of the fire grate axis 352, fire grate axis 352 that fire grate 351 is driven to rotate, 351 direction of rotation of adjacent fire grate is opposite.It is adjacent Two 351 reverse turns of fire grate be conducive to attrition crushing clinker and facilitate discharge.Fire grate 351 is installed on pyrolysis gasification furnace 3 Burning position bottom, fire grate 351 use when being failure to actuate as fire grate.Air ventilation holes 3511, gasification furnace are designed on fire grate 351 First air, to 351 lower section of fire grate, is carried out air feed to burning by air ventilation holes 3511, provides burning requisite oxygen by wind turbine air feed Gas, volume of air supply are adjusted by controlling the wind turbine in fan house 2.When needing to slag tap, revolved by driving device driving fire grate 351 Turn, lime-ash is fallen.
Sealed feeder unit 32 includes hopper 321, brake application board group 322, feed bin 323, lower flashboard group 324,325 and of driving portion Sealing 326, hopper 321 are located at the top of brake application board group 322, and feed bin 323 is located at the lower section of hopper 321,322 He of brake application board group Lower flashboard group 324 is located at the upper and lower of feed bin 323, and brake application board group 322 and lower flashboard group 324 are equipped with sealing 326.On Flashboard group 322 and lower flashboard group 324 include flashboard 3221 and flashboard frame 3222, are equipped between flashboard 3221 and flashboard frame 3222 Sealing 326, sealing 326 include that side seal 3261, preceding sealing 3262 and external seal 3263, flashboard frame 3222 are equipped with guide rail 32223, flashboard holder 32222 and sealing clamp 32221, flashboard holder 32222 are located at the periphery of flashboard frame 3222, sealing clamp 32221 connect with sealing 326, and preceding sealing 3262 and external seal 3263 are fixing seal, and side seal 3261 is to be slidingly sealed, side Sealing 3261 can be slided on guide rail 32223 simultaneously with flashboard 3221.Hopper 321 is installed on the top of brake application board group 322, expands Big feed inlet ensures that material is not scattered outward in order to concentrate charging;In normal work, brake application board group 322 and lower flashboard group 324 must not open simultaneously, to ensure that gasification furnace is constantly in closed working environment;Ensure that lower flashboard group 324 is in before charging Closed state, otherwise, upper flashboard 3221 can not be opened, and when ensureing charging, work negative pressure is unaffected in stove, and smokeless is let out Leakage.After confirmation, the flashboard 3221 of brake application board group 322 to be opened by drive cylinder, material enters feed bin 323 by hopper 321, It falls on lower flashboard 3221.Inlet amount is controlled by control grab bucket volume or other charging equipments, to ensure the volume of charging It must not exceed 323 volume of feed bin;After feeding, upper flashboard 3221 is closed, again opens lower flashboard 3221 after closing in place, The upper and lower action of flashboard 3221, from lock control, has one group of flashboard 3221 to be closed forever using position with guarantee;Upper flashboard After 3221 close, lower flashboard 3221 is opened, material is fallen into gasification furnace, then lower flashboard 3221 is closed.Sealed feeder unit 32 brake application board group 322 and lower flashboard group 324 design, is conveniently operated control;When charging, brake application board group 322 and lower flashboard group 324 It alternately opens, close, holding is closed not less than one group of flashboard 3221, to ensure that burner hearth 31 is in the building ring of sealing Border;Upper lower flashboard 3221 has sealing 326, and to ensure that no air enters gasification furnace, gasification furnace smokeless is let out from flashboard 3221 Leakage;From lock control, securely and reliably;321 wide-angle of hopper expands feed inlet, and charging equipment is adaptable, is dissipated without material when feeding It falls.
Fire observation device 34 includes flame-observing hole transparent cover 341, asbestos rubber pad 342, pyroceram piece 343, shaft 346, rotation It changes hands handle 345, arc fireguard 344, appearance fire tube 347, thermal insulation layer 348, see burner 349 and interior wide-angle sight fire tube 3410, 347 mouthfuls of ends of appearance fire tube are equipped with flame-observing hole transparent cover 341 and pyroceram piece 343, pyroceram piece 343 and flame-observing hole transparent cover Annular asbestos rubber pad 342 is padded between 341 and the faying face of appearance fire tube 347, appearance fire tube 347 sees fire tube with interior wide-angle Thermal insulation layer 348 is equipped between 3410, appearance fire tube 347 installs one piece of arc fireguard 344, arc gear at close up burner 349 Fiery plate 344 is fixed on by shaft 346 on the tube wall of appearance fire tube 347, and rotating handle 345 is installed in shaft 346.Flame-observing hole is saturating Lid 341 uses thread connection with appearance fire tube 347, and securely and reliably, easy disassembly, replacement and cleaning glass replace asbestos rubber Pad 342 is also more convenient;Pyroceram piece 343 is installed between flame-observing hole transparent cover 341 and appearance fire tube 347, and annular stone is used in combination Celloidin pad is every lining, and for sealing and protecting pyroceram piece 343, permeation high temperature resistant sheet glass 343 is it is observed that burner hearth 31 Interior combustion case;Fireguard 344 uses arc Circular plate structure, radian to be slightly less than 347 outer diameter of appearance fire tube, what fireguard 344 was justified Diameter is slightly less than 347 internal diameter of appearance fire tube, is installed on by the position of close up burner 349, specific installation be by shaft 346 with it is outer It sees fire tube 347 to couple, there are connection holes in 347 outer circle position of appearance fire tube, and shaft 346 is equipped with rotating handle 345 for controlling gear fire The rotation of plate 344, fireguard 344 are eccentrically rotated.When needing to see fire, 344 horizontal opening of fireguard, close to appearance fire tube 347 Inner wall, to ensure that viewing area is as big as possible;It sees fire end fireguard 344 and is in plumbness, by pyroceram and kiln It inside separates, effectively prevent flame, dust attack glass, glass surface area is caused to focus oil, dust etc.;Appearance fire tube 347 is installed On the outside of kiln, interior wide-angle is seen fire tube 3410 and is installed on the inside of kiln, has between appearance fire tube 347 and interior wide-angle sight fire tube 3410 Thermal insulation layer 348 prevents the high temperature that burning generates in kiln to be transmitted to appearance fire tube 347, prevents safety accident;If kiln There is flame retardant coating in inside, then interior wide-angle flame-observing hole directly can utilize fire resisting pouring material to be molded, and interior wide-angle angle determines as needed, and one As be set as 120 °;When necessary, because operation needs that flame-observing hole transparent cover 341, fireguard 344 can be opened, logical stick is put in into sight fire Material such as stirs, dredge at the generally impossible operation of gasification furnace in mouthful 349 pairs of kilns.It burns with anti-eyes, see flint glass It is not easy to cover the influence sight substance such as dust, tar, it is good to see fiery effect;Open and replace glass, sealing in 34 port of fire observation device Circle is convenient;It solves and blocks line-of-sight problems;Interior wide-angle design expands the fiery visual angle of sight, increases range of observation;Design on thermal insulation, Solves safety problem caused by heat transfer;Combustible substance in kiln can be stirred when required by burner 349 is seen, dredged It is logical to wait operation.
External airway device 33 includes external air flue 331, external thermal insulation 336 and exhaust gases passes 332, and external air flue 331 is Enclosed construction, external air flue 331 are equipped with tracheal entrance 333 and air passage outlet 334, and tracheal entrance 333 is located at air passage outlet 334 Lower section,.External thermal insulation 336 is located on the outer wall of pyrolysis gasification furnace 3.33 tracheal entrance 333 of external airway device is arranged in rubbish Dead band above the drying layer of rubbish is arranged in refuse furnace in processing gasification interval, air passage outlet 334, and gasification layer major part flue gas exists Enter external air flue 331 from 331 lower section of external air flue under air-introduced machine effect, is imported from air passage outlet 334 above external air flue 331 To above drying garbage layer, the flue gas of flue gas and drying layer that companion gasification layer minority escapes up together, is acted in air-introduced machine Under from gasification furnace exhanst gas outlet 335 enter combustion furnace.External thermal insulation 336 has heat preservation, heat insulation structural, using castable refractory or water It is jacket structured, to reduce heat radiation.
After the present invention uses the drying unit 1, more pervious roller dryer is compared, drying rubbish in the unit interval Quantity improves 20 times, and drying efficiency has obtained larger promotion, and the moisture content of rubbish falls below 30% from entered stove originally 45%, And percolate has obtained effective evaporation, is not required to add device for treating leachate again, the peculiar smell in entire workshop be under control and Processing, ensure that the improvement of the internal environment of entire refuse disposal plant area, eliminates roller dryer high-power driving motor Operation energy consumption.
In addition, to solve refuse gasification boiler, incinerator tapping mechanism complicated for deslagging device 36, cost of investment is big, operation at The problem of this height and stifled slag and incineration plants secondary pollution, while an air feed has also been taken into account, described device is strong to be pushed away The effect of power and broken slag device 364 efficiently solves the problems, such as stifled slag, and reciprocating motion in 3 seconds, has gone out slag and resetted rapidly, gone out Cinder notch 3613 has part clinker to fill up, and forms slag seal structure, and also movable 3613 backplate 3614 of slag notch protection will not leak Wind does not influence the stabilization of burner hearth 31.
Fire grate device 35, fire grate 351 is simple in structure, reasonable design.It takes into account fire grate 351 and fire grate uses, it is highly practical.Stove It arranges 351 working faces and send oxygen hole, have the function of burning oxygen supply.351 2 end of fire grate is equipped with gear (3532), has rotary slag discharge Function.Fire grate axis 352 is hollow shaft, and two sections of connection cooling water pipes can be with water flowing circulating cooling.Fire grate 351 uses hydraulic-driven, Two groups of 351 relative rotation of fire grate, the rotation of multiple fire grates 351 share a driving.
The feature into charging device stabilization reliable for operation is sealed, existing sealing is fed to solve existing pyrolysis gasification furnace 3 Problem.
Fire observation device 34 can observe combustion position in kiln, and observation visual angle is big, and effect is good, while can be in normal combustion The operation that general gasification furnace cannot be completed such as disturbed, dredged under state to material in stove.
External air flue 331 is designed using external, solves the problems such as flow of flue gas is unsmooth, gasification efficiency is low, while To ensure that later stage fume treatment effect provides the guarantee of gasifying section early period.Pyrolysis gasification furnace 3 is set to solve flow of flue gas not Freely, the problems such as gasification efficiency is low, while the guarantee of gasifying section early period is also provided for guarantee later stage fume treatment effect.Simultaneously Have many advantages, such as to manufacture convenience, low manufacture cost.
More than, refuse pyrolysis of the invention gasification drying unit in have drying unit, deslagging device, fire grate device, It seals into charging device, fire observation device and external airway device;Wherein, drying structure can allow rubbish directly to be contacted with hot wind, Drying time is saved, in the case where consuming energy without increasing, drying efficiency is obviously improved, and the energy has been saved, and Percolate has also obtained effective evaporation, ensure that refuse pyrolysis gasification furnace stablizes gasification, accelerates the firing rate of rubbish, carry The high production capacity of garbage disposal;
Deslagging device not only solves that traditional slag-tapping system is numerous and jumbled, and ancillary equipment is more, and energy consumption is big, and O&M cost is high to ask The problem of inscribing, but also having taken into account primary air-supply, solved stifled slag by break, prevent secondary pollution, easy to operate reliable, fortune It ties up at low cost, slags tap quantitative, smooth, burn thorough, the low effect of burn decrement rate;
Fire grate device, take into account solve the problems, such as to slag tap, oxygen supply, have it is simple in structure, it is easy to make, stabilization reliable for operation Feature.
Sealed feeder unit has simple in structure, easy to make, the feature of stabilization reliable for operation, to solve existing pyrolysis The existing sealing problem of gasification furnace charging, No leakage are more environmentally friendly.
Fire observation device can observe safely combustion position in kiln, and the fiery effect of sight is good, and the fiery visual angle of sight is big, the fiery glass of protection sight Glass is taken into account when solving burning to the impossible operation of the general gasification furnace such as agitation, dredging of material in stove.
External air flue is designed using external, solve flow of flue gas it is unsmooth caused by combustible gas is burned, gasification efficiency The problems such as low, while the guarantee of gasifying section early period is also provided for guarantee later stage fume treatment effect.
It should be noted that above-mentioned hydraulic cylinder or oil cylinder can also change and make cylinder or other power drives and should belong to guarantor Protect range, other power drives such as turbine worm reducer.
Above-described is only some embodiments of the present invention.For those of ordinary skill in the art, not Under the premise of being detached from the invention design, various modifications and improvements can be made, these belong to the protection model of the present invention It encloses.

Claims (5)

1. a kind of drying unit of refuse pyrolysis gasification furnace, which is characterized in that including recycle successively connected drying unit (1), Fan house (2), pyrolysis gasification furnace (3), dual firing chamber (4) and heat exchanger (5),
The drying unit (1) includes drying material pond (11), air compartment (12), discharge pipe (14) and blast pipe (13), the air compartment (12) it is multiple, multiple air compartments (12) are located at the outer pars intramuralis of the drying material pond (11), the blast pipe (13) and institute The hot air outlet (52) for stating heat exchanger (5) is connected, and hot wind is entered from the blast pipe (13) in air compartment (12), then from The discharge pipe (14) enters in the drying material pond (11).
2. the drying unit of refuse pyrolysis gasification according to claim 1, which is characterized in that set on the heat exchanger (5) There are inlet of cold air (51), exhanst gas outlet (53) and hot air outlet (52), the dual firing chamber (4) to be connected with heat exchanger (5), The hot air outlet (52) is connected with the drying unit (1).
3. the drying unit of refuse pyrolysis gasification according to claim 1, which is characterized in that the drying unit (1) is also It grabs bucket including driving, the driving grab bucket includes driving grab bucket portion (15) and track (16), and the driving grab bucket portion (15) can Mobile along the track (16), the track (16) is located at the drying unit (1), fan house (2) and the pyrolytic gasification The top of stove (3).
4. the drying unit of refuse pyrolysis gasification according to claim 3, which is characterized in that drying unit (1) institute It is the pretreatment workshop of sealing in region, is equipped with air-inlet window (10) close to fan house (2) side at it, air-inlet window is equipped on (10) Hollow out filter screen (101), interface channel is closed structure between fan house (2) and the pyrolysis gasification furnace (3).
5. the drying unit of refuse pyrolysis gasification according to claim 1, which is characterized in that the air compartment (12) includes position At drying material pond (11) side wall and bottom two, the water for being located at the rubbish exudation of drying material pond (11) is dripped from bottom discharge pipe (14) It falls in the air compartment (12) for being located at bottom, the water of exudation is oven-dried in turn, and blast pipe (13) connects with the air compartment (12) positioned at bottom Logical, blast pipe (13) is located at bottom surface of the height higher than bottom plenum (12) of the end in air compartment (12).
CN201810574556.XA 2018-06-06 2018-06-06 A kind of drying unit of refuse pyrolysis gasification furnace Pending CN108730985A (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110906347A (en) * 2019-11-14 2020-03-24 西安交通大学 A deodorization drying system for domestic waste thermal treatment
CN113587103A (en) * 2021-07-28 2021-11-02 中国铁建重工集团股份有限公司 Pyrolysis gasifier

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5642010A (en) * 1979-09-13 1981-04-20 Kubota Ltd Incinerator
CN101216176A (en) * 2008-01-14 2008-07-09 吉林省三意环保锅炉有限公司 Garbage burning processing method and device capable of accomplishing dioxin and dust zero discharge
CN107418602A (en) * 2017-09-12 2017-12-01 深圳市龙吉顺实业发展有限公司 A kind of pyrolytic gasification refuse disposal system and refuse disposal system

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5642010A (en) * 1979-09-13 1981-04-20 Kubota Ltd Incinerator
CN101216176A (en) * 2008-01-14 2008-07-09 吉林省三意环保锅炉有限公司 Garbage burning processing method and device capable of accomplishing dioxin and dust zero discharge
CN107418602A (en) * 2017-09-12 2017-12-01 深圳市龙吉顺实业发展有限公司 A kind of pyrolytic gasification refuse disposal system and refuse disposal system

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110906347A (en) * 2019-11-14 2020-03-24 西安交通大学 A deodorization drying system for domestic waste thermal treatment
CN113587103A (en) * 2021-07-28 2021-11-02 中国铁建重工集团股份有限公司 Pyrolysis gasifier

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