CN104913316A - Ash discharging device of rubbish thermal decomposition gasification furnace - Google Patents
Ash discharging device of rubbish thermal decomposition gasification furnace Download PDFInfo
- Publication number
- CN104913316A CN104913316A CN201510349468.6A CN201510349468A CN104913316A CN 104913316 A CN104913316 A CN 104913316A CN 201510349468 A CN201510349468 A CN 201510349468A CN 104913316 A CN104913316 A CN 104913316A
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- ash
- pan
- lime
- gasification furnace
- slag
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B47/00—Destructive distillation of solid carbonaceous materials with indirect heating, e.g. by external combustion
- C10B47/28—Other processes
- C10B47/32—Other processes in ovens with mechanical conveying means
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Combustion & Propulsion (AREA)
- Processing Of Solid Wastes (AREA)
- Gasification And Melting Of Waste (AREA)
Abstract
The invention discloses an ash discharging device of a rubbish thermal decomposition gasification furnace. The ash discharging device comprises a breaking conveying cutter and a disc-shaped spiral ash-stop conveying plate. The breaking conveying cutter is fixed to a triangular ash pan protrusion, and blades on the breaking conveying cutter are symmetrically and spirally distributed. The spiral ash-stop conveying plate is arranged in an ash pan, fixed to the furnace wall of the rubbish thermal decomposition gasification furnace and provided with an ash inlet and an ash outlet. The ash inlet is located in the bottom of the ash pan, and the ash outlet is higher than the upper edge of the ash pan. The ash pan is connected with a speed-adjustable motor to enable the ash pan to rotate relative to the rubbish thermal decomposition gasification furnace, and ash firstly enters the ash inlet accordingly and is conveyed to the ash outlet along with rotation of the ash pan to be discharged out of the rubbish thermal decomposition gasification furnace. The ash discharging device is simple in structure, even in breaking and good in breaking effect; meanwhile, the ash discharging effect is good, and normal running of the rubbish thermal decomposition gasification furnace is facilitated.
Description
Technical field
The present invention relates to field of solid waste treatment, be specifically related to a kind of slag-draining device of refuse pyrolysis gasification furnace.
Background technology
The processing mode of current countries in the world municipal refuse mainly contains landfill, compost and burning, pyrolytic gasification 4 kinds.Landfill disposal floor space is large, and its percolate produced and foul gas can cause serious secondary pollution to soil, underground water and surrounding air environment, destroy ecological environment; Composting technology needs to carry out pre-treatment to rubbish, requires the higher content of organic matter, and composting process needs to take larger area soil, also has dusty gas and percolate generation simultaneously, deals with improperly and can cause serious environmental pollution; The essence of burning is that organic waste is oxidized to gaseous inert gas thing and inorganic noncombustibles under the condition of high temperature and oxygen supply abundance, to form stable solid residue, the toxic gases such as a large amount of stench, sulfur-bearing can be discharged during burning, dust and fine particle thing fly upward with the wind, cause that sulfur dioxide suspended particulate substance in air exceeds standard, the dust pollution of acid rain phenomenon occurs again and again; Pyrolytic gasification technology, pyrolytic gasification refers under anaerobic or anoxia condition, material is decomposed under high temperature action, is finally converted into the thermochemical process of combustible gas, organic liquid, solid residue.Because it carries out pyrolytic gasification under anaerobic condition, stopped the generation of dioxin preferably, simultaneously it processes at any time, the feature that thoroughly processes makes to which obviate stench and produce, saved a large amount of soils.
The slag-draining device of refuse pyrolysis gasification furnace, is the important component part of gasification furnace, carries out fragmentation and discharge fast and effectively to lime-ash, is conducive to the normal operation ensureing gasification furnace.
Summary of the invention
The object of this invention is to provide a kind of slag-draining device of refuse pyrolysis gasification furnace, with fragmentation fast and effectively and discharge lime-ash
For achieving the above object, the slag-draining device of refuse pyrolysis gasification furnace provided by the invention, comprising:
One broken conveying blade, be fixed in ash-pan projection triangular in shape, this ash-pan projection is fixed in the middle of ash-pan;
Blade on the cutter hub of this broken conveying blade is symmetrical spiral distribution;
One discoidal spiral pushing off the slag delivery board, is placed in ash-pan, and is fixed on the furnace wall of refuse pyrolysis gasification furnace, and this spiral pushing off the slag delivery board has lime-ash entrance and lime-ash outlet, and lime-ash entrance is positioned at the bottom of ash-pan, and lime-ash outlet is higher than the top edge of ash-pan;
Ash-pan connects the motor of an adjustable speed, and ash-pan is rotated relative to refuse pyrolysis gasification furnace, makes lime-ash be introduced into lime-ash entrance, and Ash water is discharged refuse pyrolysis gasification furnace to lime-ash outlet along with the rotation of ash-pan.
The slag-draining device of described refuse pyrolysis gasification furnace, wherein, the blade bottom of broken conveying blade is lowered gradually to the height of projection on blade top, and cutter hub front end reduces gradually to the height of projection of cutter hub rear end; In adjacent two blades, last blade rear end and the protruding smooth connection of ash-pan, a rear blade front end is adjacent connection.
The slag-draining device of described refuse pyrolysis gasification furnace, wherein, it is that 5 ° of-15 ° of uniform spiral rise to lime-ash outlet that spiral pushing off the slag delivery board has lime-ash entrance.
The slag-draining device of described refuse pyrolysis gasification furnace, wherein, lime-ash entrance is higher than 1cm to 3cm bottom ash-pan, and lime-ash outlet is higher than grey plate edge 20cm to 30cm.
The slag-draining device of described refuse pyrolysis gasification furnace, wherein, leaves the working clearance between spiral pushing off the slag delivery board and ash-pan.
The slag-draining device of described refuse pyrolysis gasification furnace, wherein, is regulated the velocity of rotation of ash-pan by adjustable speed motor.
The invention has the beneficial effects as follows:
The present invention can not only realize the broken conveying blade of lime-ash to the fragmentation of lime-ash and release effect, and then by spiral pushing off the slag delivery board, lime-ash after fragmentation is discharged pyrolysis gasification furnace.Structure of the present invention is simple, and evenly broken, ash-slag delivery efficiency is high, simultaneously adjustable lime-ash rate of discharge.
Accompanying drawing explanation
Fig. 1 is partial thermal decomposition gasification furnace schematic diagram;
Fig. 2 is broken conveying blade schematic diagram.
Fig. 3 is spiral pushing off the slag delivery board schematic diagram.
1 refuse pyrolysis gasification furnace; 2 ash-pans; 3 broken conveying blades; 4 ash-pans are protruding; 5 spiral pushing off the slag delivery boards; 6 cutter hub rear ends; 7 cutter hub bottoms; 8 cutter hub tops; 9 cutter hub front ends; 10 lime-ash drop passage; 11 power set (adjustable speed motor); 12 high-end lime-ash outlets; 13 low side lime-ash entrances; 14 slag tap capstan winch; 15 spiral pushing off the slag delivery boards and body of heater weld.
Detailed description of the invention
Slag-draining device of the present invention forms primarily of broken conveying blade, spiral pushing off the slag delivery board and dynamical system.Broken conveying blade is mainly used in fragmentation and the propelling movement of lime-ash, and spiral pushing off the slag delivery board mainly makes slag discharge fast and effectively.The velocity of discharge of lime-ash is fast, discharges respond well.
The present invention adopts following scheme:
Broken conveying blade is all connected in ash-pan projection, and front end is broken conveying blade main body, and far-end is connected with another broken conveying blade, lowers gradually from front end to rear end projection, and rear end and the protruding junction of ash-pan seamlessly transit.Broken conveying blade is all welded in ash-pan projection.Ash-pan projection is fixed in the middle of ash-pan.
The body top of broken conveying blade increases gradually to lower lobes.The lower body part height of projection of broken conveying blade can be set to 5cm to 10cm according to pyrolysis gasification furnace output lime-ash.
Blade spiral on broken conveying blade is uniform to be welded in ash-pan projection.
In adjacent two blades, last blade rear end and the protruding smooth connection of ash-pan, a rear blade front end is adjacent connection.
Refuse pyrolysis gasification furnace spiral pushing off the slag delivery board is welded on refuse pyrolysis gasification furnace furnace wall, from low side lime-ash entrance at an angle (5 ° to 15 °) uniform spiral rise to high-end lime-ash outlet.Low side lime-ash entrance is higher than 1cm to 3cm bottom ash-pan, and high-end lime-ash outlet is higher than ash-pan top 20cm to 30cm.
In order to realize Ash water function, ash-pan is with dynamical system, ash-pan can be rotated relative to refuse pyrolysis gasification furnace, lime-ash is made to be fed into low side lime-ash entrance through the broken pusher of crushing cutter, rotation lime-ash along with ash-pan is transported to the outlet of high-end lime-ash gradually, and then is transferred out refuse pyrolysis gasification furnace.
In order to reduce refuse pyrolysis gasification furnace spiral pushing off the slag delivery board and refuse pyrolysis gasification furnace rubs, between plate and ash-pan, leaving certain space (1cm to 3cm), preventing both collisions.
In order to realize the adjustment of lime-ash rate of discharge, ash-pan carries out the adjustment of ash-pan velocity of rotation with adjustable power set.
Be further described below in conjunction with accompanying drawing.
As illustrated in fig. 1 and 2, broken conveying blade 3, comprises cutter hub front end 9 (cutter hub bottom 7, cutter hub top 8) and cutter hub rear end 6.Broken conveying blade 3 is welded in ash-pan projection 4.Cutter hub bottom 7 is lowered gradually to cutter hub top 8 height of projection, and cutter hub front end 9 reduces gradually to cutter hub rear end 6 height of projection.The quantity optimization of the blade of broken conveying blade is 4, raises into symmetrical spiral distribution along ash-pan.Each protruding 10cm in cutter hub bottom 7 is 0cm to cutter hub upper lobes, the protruding 0cm to cutter hub rear end.As shown in Figure 3, the spiral pushing off the slag delivery board 5 of refuse pyrolysis gasification furnace welds mutually with the body of heater of refuse pyrolysis gasification furnace 1 (in Fig. 3 shown in symbol 15 is spiral pushing off the slag delivery board and body of heater weld), to rise to be positioned at high-end lime-ash outlet 12 from the lime-ash entrance 13 being positioned at low side with 10 ° of baffle plate lift angle uniform spiral.Lime-ash entrance 13 is apart from the bottom 1cm of ash-pan 2, and lime-ash outlet 13 is higher than ash-pan 2 top edge 30cm.Workplace is provided with apart from being 1cm between the edge of spiral pushing off the slag delivery board 5 and ash-pan 2.
In the present embodiment, ash-pan 2 by adjustable speed motor 11 with 5 circle/minute speed at the uniform velocity rotate, ash-pan projection 4 is driven at the uniform velocity to rotate, refuse pyrolysis gasification furnace 1 maintains static, be fixed on broken conveying blade in ash-pan projection 43 and refuse pyrolysis gasify relatively rotating of furnace wall, the lime-ash be clipped in the middle fallen to the path 10 that drops from lime-ash and carries out fragmentation, more less by the distance between the furnace wall of ash-pan projection 4 bottoms and broken conveying blade, the present embodiment is 20cm, thus bulk lime-ash is broken gradually.The broken conveying blade 3 of rotation along with ash-pan promotes lime-ash and travels forward, and gradually lime-ash is discharged refuse pyrolysis gasification furnace by capstan winch 14 of slagging tap through the spiral pushing off the slag delivery board 5 be welded on refuse pyrolysis gasification furnace 1.Because broken conveying blade 3 and refuse pyrolysis gasify diminishing of distance between furnace wall, lime-ash is extruded and broken, simultaneously due to the continuous distributed of 4 blades, makes the fragmentation of lime-ash and the better effects if of conveying, and the present embodiment can be broken and export lime-ash 100kg/min.Can better broken lime-ash improve the conveying capacity (150kg/min) of lime-ash when rotating speed higher (7 circle/minute).
Claims (6)
1. a slag-draining device for refuse pyrolysis gasification furnace, comprising:
One broken conveying blade, be fixed in ash-pan projection triangular in shape, this ash-pan projection is fixed in the middle of ash-pan;
Blade on this broken conveying blade is symmetrical spiral distribution;
One discoidal spiral pushing off the slag delivery board, is placed in ash-pan, and is fixed on the furnace wall of refuse pyrolysis gasification furnace, and this spiral pushing off the slag delivery board has lime-ash entrance and lime-ash outlet, and lime-ash entrance is positioned at the bottom of ash-pan, and lime-ash outlet is higher than the top edge of ash-pan;
Ash-pan connects the motor of an adjustable speed, and ash-pan is rotated relative to refuse pyrolysis gasification furnace, makes lime-ash be introduced into lime-ash entrance, and Ash water is discharged refuse pyrolysis gasification furnace to lime-ash outlet along with the rotation of ash-pan.
2. the slag-draining device of refuse pyrolysis gasification furnace according to claim 1, wherein, the blade bottom of broken conveying blade is lowered gradually to the height of projection on blade top, and cutter hub front end reduces gradually to the height of projection of cutter hub rear end; In adjacent two blades, last blade rear end and the protruding smooth connection of ash-pan, a rear blade front end is adjacent connection.
3. the slag-draining device of refuse pyrolysis gasification furnace according to claim 1, wherein, it is that 5 ° of-15 ° of uniform spiral rise to lime-ash outlet that spiral pushing off the slag delivery board has lime-ash entrance.
4. the slag-draining device of refuse pyrolysis gasification furnace according to claim 1, wherein, lime-ash entrance is higher than 1cm to 3cm bottom ash-pan, and lime-ash outlet is higher than grey plate edge 20cm to 30cm.
5. the slag-draining device of refuse pyrolysis gasification furnace according to claim 1, wherein, leaves the working clearance between spiral pushing off the slag delivery board and ash-pan.
6. the slag-draining device of refuse pyrolysis gasification furnace according to claim 1, wherein, is regulated the velocity of rotation of ash-pan by adjustable speed motor.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510349468.6A CN104913316B (en) | 2015-06-23 | 2015-06-23 | A kind of slag-draining device of refuse pyrolysis gasification furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510349468.6A CN104913316B (en) | 2015-06-23 | 2015-06-23 | A kind of slag-draining device of refuse pyrolysis gasification furnace |
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| CN104913316A true CN104913316A (en) | 2015-09-16 |
| CN104913316B CN104913316B (en) | 2018-01-23 |
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| CN201510349468.6A Active CN104913316B (en) | 2015-06-23 | 2015-06-23 | A kind of slag-draining device of refuse pyrolysis gasification furnace |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105950194A (en) * | 2016-06-24 | 2016-09-21 | 康广民 | Edge transmission discharging device for continuous biomass pyrolyzer |
| CN106918046A (en) * | 2017-04-21 | 2017-07-04 | 商丘市恒盛机械制造有限公司 | Refuse gasification boiler rotary grate |
| CN111423907A (en) * | 2020-04-03 | 2020-07-17 | 重庆秋松环保科技有限公司 | Automatic slag removal system of pyrolysis gasifier |
| CN113265271A (en) * | 2021-05-21 | 2021-08-17 | 东莞蓝橙能源热电设备科技有限公司 | High-temperature rotating bed biomass full-gasification furnace |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105950194A (en) * | 2016-06-24 | 2016-09-21 | 康广民 | Edge transmission discharging device for continuous biomass pyrolyzer |
| CN106918046A (en) * | 2017-04-21 | 2017-07-04 | 商丘市恒盛机械制造有限公司 | Refuse gasification boiler rotary grate |
| CN111423907A (en) * | 2020-04-03 | 2020-07-17 | 重庆秋松环保科技有限公司 | Automatic slag removal system of pyrolysis gasifier |
| CN111423907B (en) * | 2020-04-03 | 2021-08-13 | 重庆秋松环保科技有限公司 | Automatic slag removal system of pyrolysis gasifier |
| CN113265271A (en) * | 2021-05-21 | 2021-08-17 | 东莞蓝橙能源热电设备科技有限公司 | High-temperature rotating bed biomass full-gasification furnace |
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| Publication number | Publication date |
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| CN104913316B (en) | 2018-01-23 |
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