CN105202546B - Solid organic castoff recycling unit - Google Patents
Solid organic castoff recycling unit Download PDFInfo
- Publication number
- CN105202546B CN105202546B CN201510743438.3A CN201510743438A CN105202546B CN 105202546 B CN105202546 B CN 105202546B CN 201510743438 A CN201510743438 A CN 201510743438A CN 105202546 B CN105202546 B CN 105202546B
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- chamber
- heater
- interlayer cavity
- preheating
- solid organic
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Abstract
The invention discloses a kind of solid organic castoff recycling unit, including feed system, cracking body of heater, heating system and discharge system etc..Wherein, the equipment is disposed with feeding preheating chamber, body of heater and grit chamber, and frame from top to bottom.The upper end of feeding preheating chamber is provided with charging aperture, and lower end is provided with discharging opening；The side wall outer layer of feeding preheating chamber is provided with preheating interlayer cavity, chimney, and bottom sets bullet to be beneficial to heat exchange.The side wall outer layer of body of heater is provided with body of heater burning interlayer cavity and body of heater burning interlayer cavity bottom is provided with Gas Pipe, air hose and igniter；The bottom of body of heater inner chamber is provided with tower setting gauge with grit chamber's connecting portion.Grit chamber bottom is provided with slag-drip opening.The present invention can continuously carry out cracking processing to solid waste, and continuous production is not shut down in realization, and production efficiency is very high.The present invention has three-level residual heat utilizing function, realizes that high efficiency of energy utilizes.
Description
Technical field
The invention belongs to solid organic castoff utilization technology field, and in particular to a kind of solid organic castoff money
Source makeup is put.
Background technology
While continuous development with society, debirs quantity is increasing, and it is difficult that debirs carry out harmless treatment
Degree is big, cost is high, and common process mode can cause environmental pollution.The discarded organic matter in town and country belongs to macromolecule nytron mostly
Thing, decompose needs more than 200 years in its natural state, and environment is polluted, and takes substantial amounts of arable land.With life rubbish
Exemplified by rubbish, conventionally employed burning disposal mode can produce secondary pollution in gas and waste residue and with heavy metal pollution.
And need oil spout combustion-supporting during burning disposal, it is too high to directly result in processing cost.
On the other hand, as the disposable resource of the sustainable fast development, oil, natural gas, coal gas etc. of China's economy supplies
Breach is needed to increase year by year, there is an urgent need to a kind of low price, energy-conservation, safe, clean New-type fuel to enter market by people.
Based on above present situation, people constantly explore and fuel oil are produced by way of organic cracking, existing to discarded organic
The cleavage method of thing is to load organic matter as cracked in reactor, produces crude oil and waste residue.Debirs can not only be carried out
Processing, and crude oil fuel can be prepared, turn waste into wealth.It is a kind of economy the most, science to extract fuel oil by cracking process, is carried
Take the fuel oil extracting mode that rate is high.
Organic cracking equipment had produced number for improvement project, and respectively after long-term use, or be eliminated
Or be continuing with, yet with debirs broad categories, a variety of different articles are admixed in organic waste in addition containing metal or
Stone etc., prior art are often suitable only for the debirs of specific composition.Although existing cracking apparatus once passes through repeatedly essence
The development and improvement of property, but the defects of continuous production is poor, seriously polluted, efficiency is low and cost is high is still suffered from so far.
The content of the invention
For existing solid organic castoff cracking apparatus has poor continuity, seriously polluted, efficiency is low and cost is high etc.
Defect and problem, present invention offer is a kind of continuously waste to be handled and efficiently be disguised using the solid organic castoff resource of heat energy
Put.
Scheme is used by the present invention solves its technical problem：A kind of solid organic castoff recycling unit, including
Feed system, cracking body of heater, heating system and discharge system etc..Wherein, the equipment is disposed with feeding preheating from top to bottom
Room, body of heater and grit chamber, and frame.The upper end of feeding preheating chamber is provided with charging aperture, and lower end is provided with discharging opening；Feeding preheats
The side wall outer layer of room is provided with preheating interlayer cavity, and preheating interlayer cavity top is provided with chimney, the discharging opening of feeding preheating chamber
Position is arranged to bullet wide at the top and narrow at the bottom, and bullet is advantageous to heat exchange.Bullet forms heat exchanging chamber, heat exchange with furnace wall top
Chamber side connects with the chamber that confluxes, and the heat using body of heater inner chamber to chamber discharge of confluxing, bullet is heated, realizes heat exchange purpose.
The side wall outer layer of body of heater be provided with body of heater burning interlayer cavity and be provided with body of heater burning interlayer cavity bottom Gas Pipe,
Air hose and igniter, the top of body of heater burning interlayer cavity are connected by blast pipe with the preheating interlayer cavity.
The bottom of body of heater inner chamber is provided with tower setting gauge with grit chamber's connecting portion.
Grit chamber bottom is provided with slag-drip opening.
Further, vertically run through in the middle part of the grit chamber and setting gauge rotating cylinder, the bottom of setting gauge rotating cylinder and rotating cylinder are installed
Drive mechanism is connected, and setting gauge rotating cylinder top is connected with the tower setting gauge.Further, setting gauge rotating cylinder is provided with
Inner chamber, its bottom are communicated with multifunction additive adding tube, and its top is provided with scattered heat exchanger tube；Scattered heat exchanger tube fitting distribution
In setting gauge rotating cylinder inner side or outer surface, and the outlet of each scattered heat exchanger tube is located at different height.
Further, the tower setting gauge includes centering type cone-shaped hood, the conical surface both sides extension length of centering type cone-shaped hood
Degree is different, and the bottom of the longer extension conical surface and the shorter extension conical surface is respectively arranged with movable swing rod, and the bottom of movable swing rod is hinged
There is fitting scraper plate；Body of heater intracavity bottom is provided with arc surfaced blanking outlet, the fitting scraper plate and arc surfaced blanking outlet
Match somebody with somebody.Further, the outward flange of the centering type cone-shaped hood or upper outer edge are hinged with auxiliary scraper plate, aid in scraper plate and body of heater
Inwall bottom mating fits together.
Further, stirring motor rotating shaft, the upper end of stirring motor rotating shaft are vertically installed in the feeding preheating chamber
It is connected with stirring motor；The bottom of stirring motor rotating shaft is located at conical body portion position and is disposed with tapered material distributor and screw propulsion
Blade.
Further, the side wall of the feeding preheating chamber is arranged to taper wide at the top and narrow at the bottom.
Further, grit chamber's lateral wall is provided with hot blast interlayer cavity, hot blast interlayer cavity bottom is provided with hot blast and entered
Mouthful, hot blast interlayer cavity is respectively communicated with grit chamber and body of heater inner chamber.Further, chimney is provided with breeches pipe, and breeches pipe is returned by waste heat
Pipe connects with hot wind inlet.
Further, the top of combustion chamber of furnace body's interlayer cavity is provided with preheating comb, is set on the outside of material conveyor
Seal closure is equipped with, seal closure bottom is provided with preheating inlet, and top is provided with air outlet；The preheating comb connects with preheating inlet
It is logical.
Further, the bottom of the chamber that confluxes is provided with spiral row's device for asphalt, chamber its end after supercooling of confluxing
It is respectively arranged with oil exit pipe and tail gas comb.Further, the tail gas comb is communicated in body of heater burning folder by drainage pipe
Layer intracavitary, is burned tail gas as fuel.
Further, rotating cylinder drive mechanism includes the gear or sprocket wheel installed in setting gauge cylinder bottom, gear or chain
The master gear or head sprocket of wheel and motor are connected.
Further, feeding preheating chamber side wall is provided with material level detection mechanism.
Beneficial effects of the present invention：
1. the present invention can continuously carry out cracking processing to solid waste, continuous production, production efficiency are not shut down in realization
It is very high.
2. the present invention has three-level residual heat utilizing function, realize that high efficiency of energy utilizes.First order UTILIZATION OF VESIDUAL HEAT IN is by pre-
Hot comb preheats to material in conveyer, improves temperature of charge；Second level preheating is that the feeding preheating chamber to closing is carried out
Heating, improve temperature of charge；Third level preheating is to set bullet in feeding preheating chamber bottom, because bullet is in boiler intracavity
Top, into the chamber that confluxes before waste heat bullet can be heated, further improve temperature of charge.
3. the tower setting gauge that the present invention is set, its centering type cone-shaped hood can promote slag charge to make under it under rotary action
Material, and coordinate movable scraping plate to clear up feed opening accumulated slag automatically, and hard metal or stone are automatically bypassed, make it not to equipment
Inside damages.
4. the setting gauge rotating cylinder set in grit chamber, its hollow structure is used to convey multifunction additive, multifunction additive
Effective temperature-reducing can be carried out to setting gauge rotating cylinder top by scattered heat exchanger tube, at the same multifunction additive be heated after be changed into gas
Liquid mixed state, it is easy to participate in cracking reaction in from bottom of furnace body into body of heater inner chamber.
5. be arranged to taper inside feeding preheating chamber, bottom is also arranged to taper, heat to it is up when be beneficial to heat the conical surface,
The conical surface is set to fully absorb heat energy.In addition tripper and the effect of screw propulsion blade, make material fit in inwall using preheating.
6. exhaust combustion can not only avoid polluting air ambient, and provide combustion heat energy again.
Brief description of the drawings
Fig. 1 is the complete machine structure schematic diagram of the present invention；
Fig. 2 is the enlarged diagram of third level heat exchange structure in Fig. 1；
Fig. 3 is the mplifying structure schematic diagram of blanking part in Fig. 1.
Label in figure, 1 is feeding preheating chamber, and 2 be body of heater inner chamber, and 3 be grit chamber, and 4 be frame, and 5 be charging aperture, and 6 be discharging
Mouthful, 7 be spiral slag-draining device, and 8 be tower setting gauge, and 9 be multifunction additive adding tube, and 10 be stirring motor rotating shaft, and 11 are
Setting gauge rotating cylinder, 12 be Gas Pipe, and 13 be air hose, and 14 be igniter, and 15 be chimney, and 16 be waste heat return pipe, and 17 be blower fan, 18
It is the chamber that confluxes for hot wind inlet, 19,20 be tail gas comb, and 21 be oil exit pipe, and 22 be body of heater burning interlayer cavity, and 23 be preheating interlayer
Chamber, 24 be hot blast interlayer cavity, and 25 be heat exchanging chamber, and 26 be blast pipe, and 27 be tap hole, and 28 be bullet, and 29 be tripper, and 30 are
Screw propulsion blade, 31 be that spiral arranges device for asphalt, and 32 be rotating cylinder drive mechanism, and 33 be scattered heat exchanger tube, and 34 be material-level measure
Mechanism, 35,36,37,38 and 39 be manhole, and 40 be deflector, and 41 be preheating comb.81 be centering type cone-shaped hood, and 82 be activity
Swing rod, 83 be fitting scraper plate, and 84 be auxiliary scraper plate, and 91 be that multifunction additive dredges inner chamber.
Embodiment
The present invention is further described with reference to the accompanying drawings and examples.
Such as Fig. 1, solid organic castoff recycling unit is disposed with feeding preheating chamber 1, body of heater and slag from top to bottom
Room 3, and frame 4, and it is provided with corresponding manhole.
Feeding preheating chamber 1：The upper end of feeding preheating chamber 1 is provided with charging aperture 5, and lower end is provided with discharging opening 6；Feeding preheats
The side wall outer layer of room 1 is provided with preheating interlayer cavity 23, and preheating interlayer cavity 23 top is provided with chimney 15, feeding preheating chamber 1
The position of discharging opening 6 be arranged to bullet 28 wide at the top and narrow at the bottom, bullet 28 is advantageous to heat exchange.Wrapped around in bullet 28
The chamber 19 that confluxes is provided with, the heat using body of heater inner chamber 2 to the discharge of chamber 19 of confluxing, bullet 28 is heated, realizes heat exchange purpose.
Stirring motor rotating shaft 10, the upper end connection of stirring motor rotating shaft 10 are vertically installed in the feeding preheating chamber 1
There is stirring motor；The bottom of stirring motor rotating shaft 10 is located at that the position of bullet 28 is disposed with tapered material distributor 29 and spiral pushes away
Enter blade 30.
The side wall of the feeding preheating chamber 1 is it can also be provided that taper wide at the top and narrow at the bottom, in favor of heat exchange.
The side wall of feeding preheating chamber 1 is provided with material level detection mechanism 34.
Conflux chamber 19：The chamber 19 that confluxes reclaims product after being used for cracking reaction, and the bottom for the chamber 19 that confluxes is provided with spiral row's drip
Blue or green device 31, its end after supercooling of chamber 19 of confluxing are respectively arranged with oil exit pipe 21 and tail gas comb 20.
Body of heater：The side wall outer layer of body of heater is provided with body of heater burning interlayer cavity 22 and set in body of heater burning interlayer cavity 22 bottom
There are Gas Pipe 12, air hose 13 and igniter 14, the top of body of heater burning interlayer cavity 22 passes through blast pipe 26 and the preheating
Interlayer cavity 23 connects.
The bottom of body of heater inner chamber 2 is provided with tower setting gauge 8 with the connecting portion of grit chamber 3.
Tower setting gauge 8：Tower setting gauge 8 includes centering type cone-shaped hood 81, and the conical surface both sides of centering type cone-shaped hood 81 are prolonged
Elongation is different, and the bottom of the longer extension conical surface and the shorter extension conical surface is respectively arranged with movable swing rod 82, movable swing rod 82
Bottom is hinged with fitting scraper plate 83；Arc surfaced blanking outlet, the fitting scraper plate 83 and cambered surface are provided with the bottom of body of heater inner chamber 2
Shape blanking outlet matching.
Be hinged with the outward flange of the centering type cone-shaped hood 81 or upper outer edge auxiliary scraper plate 84, auxiliary scraper plate 84 with
Inboard wall of furnace body bottom mating fits together.
Grit chamber 3：Vertically through setting gauge rotating cylinder 11 is provided with, bottom and the rotating cylinder of setting gauge rotating cylinder 11 drive at the middle part of grit chamber 3
Motivation structure 32 is connected, and the top of setting gauge rotating cylinder 11 is connected with the tower setting gauge 8.In setting gauge rotating cylinder 11 is provided with
Chamber, its bottom are communicated with multifunction additive adding tube 9, and its top is provided with scattered heat exchanger tube 33；Scattered heat exchanger tube 33 is bonded
The inner side of setting gauge rotating cylinder 11 or outer surface are distributed in, and the outlet of each scattered heat exchanger tube 33 is located at different height.The bottom of grit chamber 3
Slag-drip opening is provided with, slag-drip opening is provided with spiral slag-draining device 7.
The lateral wall of grit chamber 3 is provided with hot blast interlayer cavity 24, the bottom of hot blast interlayer cavity 24 is provided with hot wind inlet, heat
Wind interlayer cavity 24 is respectively communicated with grit chamber 3 and body of heater inner chamber 2.
Chimney 15 is provided with breeches pipe, and breeches pipe is connected by waste heat return pipe 16 with hot wind inlet.
The top of combustion chamber of furnace body's interlayer cavity is provided with preheating comb 41, and sealing is provided with the outside of material conveyor
Cover, seal closure bottom are provided with preheating inlet, and top is provided with air outlet；The preheating comb 41 connects with preheating inlet.
The tail gas comb 20 is communicated in body of heater by drainage pipe and burnt in interlayer cavity 22, is fired tail gas as fuel
Burn.
Rotating cylinder drive mechanism 32 includes the gear or sprocket wheel installed in the bottom of setting gauge rotating cylinder 11, gear or sprocket wheel and drive
The master gear of dynamic motor or head sprocket drive connection.
Claims (10)
1. a kind of solid organic castoff recycling unit, including feed system, cracking body of heater, heating system and discharge system,
It is characterized in that：Feeding preheating chamber, body of heater and grit chamber are disposed with from top to bottom；The upper end of the feeding preheating chamber is provided with
Charging aperture, lower end are provided with discharging opening；The side wall outer layer of feeding preheating chamber is provided with preheating interlayer cavity, and in preheating interlayer cavity
Portion is provided with chimney, and the discharging opening position of feeding preheating chamber is arranged to bullet wide at the top and narrow at the bottom, bullet and furnace wall top shape
Into heat exchanging chamber, wrapped around in bullet and be provided with the chamber that confluxes, the heat using body of heater inner chamber to chamber discharge of confluxing, to bullet
Heating, heat exchange is realized, heat exchanging chamber side connects with the chamber that confluxes；The side wall outer layer of body of heater is provided with body of heater burning interlayer cavity and in stove
Body burning interlayer cavity bottom is provided with Gas Pipe, air hose and igniter, and the top of body of heater burning interlayer cavity passes through blast pipe
Connected with the preheating interlayer cavity；The bottom of body of heater inner chamber is provided with tower setting gauge with grit chamber's connecting portion；Grit chamber bottom is set
It is equipped with slag-drip opening.
2. solid organic castoff recycling unit according to claim 1, it is characterised in that：It is vertical in the middle part of the grit chamber
Through setting gauge rotating cylinder is provided with, bottom and the rotating cylinder drive mechanism of setting gauge rotating cylinder are connected, setting gauge rotating cylinder top with
The tower setting gauge connection.
3. solid organic castoff recycling unit according to claim 1, it is characterised in that：The tower setting gauge bag
Centering type cone-shaped hood is included, the conical surface both sides development length of centering type cone-shaped hood is different, the longer extension conical surface and the shorter extension conical surface
Bottom be respectively arranged with movable swing rod, the bottom of movable swing rod is hinged with fitting scraper plate；Body of heater intracavity bottom is provided with arc
Face shape blanking outlet, the fitting scraper plate match with arc surfaced blanking outlet.
4. solid organic castoff recycling unit according to claim 2, it is characterised in that：Setting gauge rotating cylinder is provided with
Inner chamber, its bottom are communicated with multifunction additive adding tube, and its top is provided with scattered heat exchanger tube；Scattered heat exchanger tube fitting distribution
In setting gauge rotating cylinder inner side or outer surface, and the outlet of each scattered heat exchanger tube is located at different height.
5. solid organic castoff recycling unit according to claim 3, it is characterised in that：In the centering type taper
The outward flange of cover or upper outer edge are hinged with auxiliary scraper plate, and auxiliary scraper plate fits together with inboard wall of furnace body bottom mating.
6. according to the solid organic castoff recycling unit described in claim any one of 1-5, it is characterised in that：Sent described
Stirring motor rotating shaft is vertically installed in material preheating chamber, the upper end of stirring motor rotating shaft is connected with stirring motor；Stirring motor turns
The bottom of axle is located at conical body portion position and is disposed with tapered material distributor and screw propulsion blade.
7. solid organic castoff recycling unit according to claim 1, it is characterised in that：In grit chamber's lateral wall
Hot blast interlayer cavity is provided with, hot blast interlayer cavity bottom is provided with hot wind inlet, and hot blast interlayer cavity is respectively communicated with grit chamber and body of heater
Inner chamber；Chimney is provided with breeches pipe, and breeches pipe is connected by waste heat return pipe with hot wind inlet.
8. solid organic castoff recycling unit according to claim 1, it is characterised in that：Combustion chamber of furnace body's folder
The top of layer chamber is provided with preheating comb, is provided with seal closure on the outside of material conveyor, seal closure bottom be provided with preheat into
Mouthful, top is provided with air outlet；The preheating comb connects with preheating inlet.
9. solid organic castoff recycling unit according to claim 1, it is characterised in that：The bottom of the chamber that confluxes
Spiral row's device for asphalt is provided with, chamber its end after supercooling of confluxing is respectively arranged with oil exit pipe and tail gas comb.
10. solid organic castoff recycling unit according to claim 9, it is characterised in that：The tail gas comb leads to
Cross drainage pipe to be communicated in body of heater burning interlayer cavity, be burned tail gas as fuel.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510743438.3A CN105202546B (en) | 2015-11-05 | 2015-11-05 | Solid organic castoff recycling unit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510743438.3A CN105202546B (en) | 2015-11-05 | 2015-11-05 | Solid organic castoff recycling unit |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN105202546A CN105202546A (en) | 2015-12-30 |
| CN105202546B true CN105202546B (en) | 2017-11-14 |
Family
ID=54950371
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510743438.3A Expired - Fee Related CN105202546B (en) | 2015-11-05 | 2015-11-05 | Solid organic castoff recycling unit |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105202546B (en) |
Families Citing this family (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105670694B (en) * | 2016-01-05 | 2018-07-24 | 刘勇 | Biomass gasifying furnace |
| CN105782992B (en) * | 2016-03-21 | 2017-11-03 | 安徽未名生物环保有限公司 | A kind of rubbish is heat-treated impurity feeding control system |
| CN105698190B (en) * | 2016-03-21 | 2018-07-20 | 安徽未名生物环保有限公司 | A kind of rubbish heat-treatment furnace classification impurity removal control system |
| CN107381995A (en) * | 2017-09-19 | 2017-11-24 | 来江 | A kind of oil-containing mud sand hazardous waste disposal system |
| CN110307549A (en) * | 2019-07-09 | 2019-10-08 | 江苏维尔思环境工程股份有限公司 | A kind of minimum discharge can UTILIZATION OF VESIDUAL HEAT IN three industrial wastes furnace |
| CN114058409A (en) * | 2021-02-02 | 2022-02-18 | 长沙稻香农业科技有限公司 | Method for preparing steam by using gas prepared from wood chips and bamboo chips in gas-fired boiler |
| CN113757680B (en) * | 2021-08-12 | 2022-06-28 | 合肥工业大学 | Energy-saving and environment-friendly organic waste incineration device |
Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2119571U (en) * | 1992-02-18 | 1992-10-21 | 张士华 | Multipurpose refuse incinerator |
| JPH07233915A (en) * | 1994-02-25 | 1995-09-05 | Hitachi Zosen Corp | High speed circulation type fluidized bed incinerator |
| CN101434846A (en) * | 2008-12-15 | 2009-05-20 | 黄荣胜 | Method and apparatus for biomass ion catalytic pyrolysis gasification |
| CN202322753U (en) * | 2011-11-20 | 2012-07-11 | 张忠成 | Downdraft biomass fuel gasifier |
| CN104119959A (en) * | 2013-04-27 | 2014-10-29 | 穆华 | Inverse-combustion dual-medium domestic waste gasifier |
| CN205261566U (en) * | 2015-11-05 | 2016-05-25 | 杨西建 | Solid organic waste resource is made up and is put |
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2015
- 2015-11-05 CN CN201510743438.3A patent/CN105202546B/en not_active Expired - Fee Related
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| CN105202546A (en) | 2015-12-30 |
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