CN205261566U - Solid organic waste resource is made up and is put - Google Patents
Solid organic waste resource is made up and is put Download PDFInfo
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- CN205261566U CN205261566U CN201520875695.8U CN201520875695U CN205261566U CN 205261566 U CN205261566 U CN 205261566U CN 201520875695 U CN201520875695 U CN 201520875695U CN 205261566 U CN205261566 U CN 205261566U
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- preheating
- heater
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- setting gauge
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Abstract
The utility model discloses a solid organic waste resource is made up and is put, including charge -in system, schizolysis furnace body, heating system and ejection of compact system etc.. Wherein, this equipment top -down has set gradually pay -off preheating chamber, furnace body and grit chamber, and the frame. The upper end of pay -off preheating chamber is provided with the feed inlet, and the lower extreme is provided with the discharge gate, the lateral wall skin of pay -off preheating chamber is provided with and preheats interlayer cavity, chimney, and the bottom sets up the conical body and does benefit to the heat exchange. The lateral wall skin of furnace body is provided with furnace body burning interlayer cavity and is provided with gas pipe, air hose and some firearm bottom furnace body burning interlayer cavity, the bottom and the grit chamber of furnace body inner chamber are connected the position and are provided with tower setting gauge. The grit chamber bottom row of being provided with cinder notch. The utility model discloses can carry out pyrolysis treatment to solid waste in succession, realize not shutting down lasting and produce, production efficiency is very high. The utility model discloses have tertiary waste heat utilization function, realize the high -efficient utilization of the energy.
Description
Technical field
The utility model belongs to solid organic castoff recovery and utilization technology field, is specifically related to a kind of solid organic castoff recycling unit.
Background technology
Along with social development time, debirs quantity is increasing, and debirs carry out that harmless treatment difficulty is large, cost is high, and common process mode can cause environmental pollution. The discarded organic matter in town and country belongs to high-molecular hydrocarbons mostly, decomposes and need more than 200 years, to environment, and to take a large amount of arable lands under nature. Taking house refuse as example, the burning disposal mode that tradition adopts all can produce secondary pollution and follow heavy metal pollution in gas and waste residue. And need oil spout combustion-supporting in burning disposal process, directly cause processing cost too high.
On the other hand, along with the sustainable fast development of China's economy, the disposable resource supply and demand breach such as oil, natural gas, coal gas increase year by year, and people come into the market in the urgent need to a kind of low price, energy-conservation, safe, clean New-type fuel.
Based on above present situation, people constantly explore and produce fuel oil by the mode of organic cracking, and the existing cleavage method to organic waste is that organic matter is packed into as cracking in reactor, produce crude oil and waste residue. Not only can process debirs, and can prepare former oil fuel, turn waste into wealth. Extracting fuel oil by cracking process is one economy, science the most, the fuel oil extracting mode that recovery rate is high.
Organic cracking equipment had produced number for improvement project, and respectively after long-term use, or be eliminated or continue use, but because debirs kind is numerous and diverse, in organic waste, admix multiple different article and even contain metal or stone etc., prior art is only suitable for the debirs of specific composition conventionally. Although existing cracking apparatus, once by repeatedly substantial development and improvement, still exists so far, continuous production is poor, seriously polluted, efficiency is low and high in cost of production defect.
Utility model content
The defect and the problem that exist for existing solid organic castoff cracking apparatus, the scheme that the utility model technical solution problem adopts is: a kind of solid organic castoff recycling unit, comprises feed system, cracking body of heater, heating system and discharge system etc. Wherein, this equipment is disposed with feeding preheating chamber, body of heater and grit chamber from top to bottom, and frame. The upper end of feeding preheating chamber is provided with charging aperture, and lower end is provided with discharging opening; The sidewall skin of feeding preheating chamber is provided with preheating interlayer chamber, and is provided with chimney on top, preheating interlayer chamber, and the discharging opening position of feeding preheating chamber is set to bullet wide at the top and narrow at the bottom, and bullet is conducive to heat exchange. Heat exchanging chamber is formed at bullet and top, furnace wall, and heat exchanging chamber one side is communicated with the chamber of confluxing, and the heat that utilizes body of heater inner chamber to discharge to the chamber of confluxing, to bullet heating, is realized heat exchange object.
The sidewall skin of body of heater is provided with body of heater burning interlayer chamber and is provided with Gas Pipe, air hose and igniter in bottom, body of heater burning interlayer chamber, and the top in this body of heater burning interlayer chamber is communicated with described preheating interlayer chamber by blast pipe.
The bottom of body of heater inner chamber and grit chamber's connecting portion are provided with tower setting gauge.
Bottom, grit chamber is provided with slag-drip opening.
Further, in the middle part of described grit chamber, vertically run through setting gauge rotating cylinder is installed, the bottom of setting gauge rotating cylinder and rotating cylinder driving mechanism are in transmission connection, and setting gauge rotating cylinder top is connected with described tower setting gauge. Further, setting gauge rotating cylinder is provided with inner chamber, and its bottom is communicated with multifunction additive adding tube, and its top is provided with dispersion heat exchanger tube; Disperse heat exchanger tube laminating to be distributed in setting gauge rotating cylinder inner side or outer surface, and respectively disperse the outlet of heat exchanger tube to be positioned at differing heights.
Further, described tower setting gauge comprises centering type cone-shaped hood, the conical surface both sides development length difference of centering type cone-shaped hood, and long bottom of extending the conical surface and the shorter extension conical surface is respectively arranged with movable fork, and the bottom-hinged of movable fork has laminating scraper plate; Be provided with arc surfaced blanking outlet at body of heater intracavity bottom, described laminating scraper plate mates with arc surfaced blanking outlet. Further, the outward flange of described centering type cone-shaped hood or upper outer edge are hinged with auxiliary scraper plate, and auxiliary scraper plate and inboard wall of furnace body bottom mating fit together.
Further, in described feeding preheating chamber, stirring motor rotating shaft is vertically installed, the upper end of stirring motor rotating shaft is connected with stirring motor; The bottom of stirring motor rotating shaft is positioned at bullet position and is disposed with tapered material distributor and screw propulsion blade.
Further, the sidewall of described feeding preheating chamber is set to taper wide at the top and narrow at the bottom.
Further, be provided with hot blast interlayer chamber at described grit chamber lateral wall, bottom, hot blast interlayer chamber is provided with hot blast import, and hot blast interlayer chamber is communicated in respectively grit chamber and body of heater inner chamber. Further, chimney is provided with breeches pipe, and breeches pipe is communicated with hot blast import by waste heat return pipe.
Further, the top in described combustion chamber of furnace body's interlayer chamber is provided with preheating comb, has seal closure in material conveyor arranged outside, and seal closure bottom is provided with preheating inlet, and top is provided with air outlet; Described preheating comb is communicated with preheating inlet.
Further, described in the conflux bottom in chamber be provided with spiral row device for asphalt, chamber its end after supercooling that confluxes is respectively arranged with oil exit pipe and tail gas comb. Further, described tail gas comb is communicated in body of heater burning interlayer chamber by drainage pipe, and tail gas is burned as fuel.
Further, rotating cylinder driving mechanism comprises the gear or the sprocket wheel that are arranged on setting gauge rotating cylinder bottom, and master gear or the head sprocket of gear or sprocket wheel and drive motors are in transmission connection.
Further, be provided with material level detection mechanism at feeding preheating chamber sidewall.
The beneficial effects of the utility model:
1. the utility model can carry out cracking processing to solid waste continuously, realizes and does not shut down continuous production, and production efficiency is very high.
2. the utlity model has three grades of residual heat utilizing functions, realize high efficiency of energy utilization. First order UTILIZATION OF VESIDUAL HEAT IN is, by preheating comb, material in conveyer is carried out to preheating, improves temperature of charge; Second level preheating is that the feeding preheating chamber of sealing is heated, and improves temperature of charge; Third level preheating is, in feeding preheating chamber bottom, bullet is set, and because bullet is at boiler intracavity top, entering the chamber waste heat before that confluxes can heat bullet, further improves temperature of charge.
3. the tower setting gauge that the utility model arranges, its centering type cone-shaped hood can promote slag charge and make its blanking under rotary action, and coordinate the movable scraping plate can Automatic clearance feed opening accumulated slag, and automatic winding crosses hard metal or stone, and it is not damaged device interior.
4. the setting gauge rotating cylinder arranging in grit chamber, its hollow structure is for delivery of multifunction additive, multifunction additive is by disperseing heat exchanger tube to carry out effective temperature-reducing to setting gauge rotating cylinder top, multifunction additive becomes gas-liquid mixed state after being heated simultaneously, is convenient to enter body of heater inner chamber and participate in cracking reaction from bottom of furnace body.
5. feeding preheating chamber inside is set to taper, and bottom is also set to taper, and heat is beneficial to when up conical surface heating, makes the conical surface can fully absorb heat energy. In addition tripper and the effect of screw propulsion blade, make material fit in inwall and utilize preheating.
6. exhaust combustion not only can be avoided contaminated air environment, and combustion heat energy is provided again.
Brief description of the drawings
Fig. 1 is complete machine structure schematic diagram of the present utility model;
Fig. 2 is the enlarged diagram of third level heat exchange structure in Fig. 1;
Fig. 3 is the structure for amplifying schematic diagram of blanking part in Fig. 1.
Number in the figure, 1 is feeding preheating chamber, 2 is body of heater inner chamber, 3 is grit chamber, 4 is frame, 5 is charging aperture, 6 is discharging opening, 7 is spiral slag-draining device, 8 is tower setting gauge, 9 is multifunction additive adding tube, 10 is stirring motor rotating shaft, 11 is setting gauge rotating cylinder, 12 is Gas Pipe, 13 is air hose, 14 is igniter, 15 is chimney, 16 is waste heat return pipe, 17 is blower fan, 18 is hot blast import, 19 is the chamber of confluxing, 20 is tail gas comb, 21 is oil exit pipe, 22 is body of heater burning interlayer chamber, 23 is preheating interlayer chamber, 24 is hot blast interlayer chamber, 25 is heat exchanging chamber, 26 is blast pipe, 27 is tap hole, 28 is bullet, 29 is tripper, 30 is screw propulsion blade, 31 is spiral row device for asphalt, 32 is rotating cylinder driving mechanism, 33 for disperseing heat exchanger tube, 34 is material level detection mechanism, 35, 36, 37, 38 and 39 is manhole, 40 is deflector, 41 is preheating comb. 81 is centering type cone-shaped hood, and 82 is movable fork, and 83 is laminating scraper plate, and 84 is auxiliary scraper plate, and 91 is multifunction additive dredging inner chamber.
Detailed description of the invention
Below in conjunction with drawings and Examples, the utility model is further illustrated.
As Fig. 1, solid organic castoff recycling unit is disposed with feeding preheating chamber 1, body of heater and grit chamber 3 from top to bottom, and frame 4, and is provided with corresponding manhole.
Feeding preheating chamber 1: the upper end of feeding preheating chamber 1 is provided with charging aperture 5, lower end is provided with discharging opening 6; The sidewall skin of feeding preheating chamber 1 is provided with preheating interlayer chamber 23, and is provided with chimney 15 on 23 tops, preheating interlayer chamber, and discharging opening 6 positions of feeding preheating chamber 1 are set to bullet wide at the top and narrow at the bottom 28, and bullet 28 is conducive to heat exchange. Be surrounded with in bullet 28 outsides the chamber 19 of confluxing, the heat that utilizes body of heater inner chamber 2 to discharge to the chamber 19 of confluxing, heats bullet 28, realizes heat exchange object.
Stirring motor rotating shaft 10 is vertically installed described feeding preheating chamber 1 is interior, the upper end of stirring motor rotating shaft 10 is connected with stirring motor; The bottom of stirring motor rotating shaft 10 is positioned at bullet 28 positions and is disposed with tapered material distributor 29 and screw propulsion blade 30.
The sidewall of described feeding preheating chamber 1 also can be set to taper wide at the top and narrow at the bottom, is beneficial to heat exchange.
Be provided with material level detection mechanism 34 at feeding preheating chamber 1 sidewall.
The chamber 19 of confluxing: the chamber 19 of confluxing is for reclaiming product after cracking reaction, the bottom in the chamber 19 of confluxing is provided with spiral row device for asphalt 31, and chamber 19 its end after supercooling that confluxes is respectively arranged with oil exit pipe 21 and tail gas comb 20.
Body of heater: the sidewall skin of body of heater is provided with body of heater burning interlayer chamber 22 and is provided with Gas Pipe 12, air hose 13 and igniter 14 in body of heater burning 22 bottoms, interlayer chamber, and the top in this body of heater burning interlayer chamber 22 is communicated with described preheating interlayer chamber 23 by blast pipe 26.
The bottom of body of heater inner chamber 2 and grit chamber's 3 connecting portions are provided with tower setting gauge 8.
Tower setting gauge 8: tower setting gauge 8 comprises centering type cone-shaped hood 81, the conical surface both sides development length difference of centering type cone-shaped hood 81, long bottom of extending the conical surface and the shorter extension conical surface is respectively arranged with movable fork 82, and the bottom-hinged of movable fork 82 has laminating scraper plate 83; Be provided with arc surfaced blanking outlet in body of heater inner chamber 2 bottoms, described laminating scraper plate 83 mates with arc surfaced blanking outlet.
Outward flange or upper outer edge at described centering type cone-shaped hood 81 are hinged with auxiliary scraper plate 84, and auxiliary scraper plate 84 fits together with inboard wall of furnace body bottom mating.
Grit chamber 3: vertically run through at 3 middle parts setting gauge rotating cylinder 11 is installed grit chamber, and the bottom of setting gauge rotating cylinder 11 and rotating cylinder driving mechanism 32 are in transmission connection, and setting gauge rotating cylinder 11 tops are connected with described tower setting gauge 8. Setting gauge rotating cylinder 11 is provided with inner chamber, and its bottom is communicated with multifunction additive adding tube 9, and its top is provided with and disperses heat exchanger tube 33; Disperse heat exchanger tube 33 laminatings to be distributed in setting gauge rotating cylinder 11 inner sides or outer surface, and respectively disperse the outlet of heat exchanger tube 33 to be positioned at differing heights. 3 bottoms, grit chamber are provided with slag-drip opening, and slag-drip opening is provided with spiral slag-draining device 7.
In described grit chamber, 3 lateral walls are provided with hot blast interlayer chamber 24, and 24 bottoms, hot blast interlayer chamber are provided with hot blast import, and hot blast interlayer chamber 24 is communicated in respectively grit chamber 3 and body of heater inner chamber 2.
Chimney 15 is provided with breeches pipe, and breeches pipe is communicated with hot blast import by waste heat return pipe 16.
The top in described combustion chamber of furnace body's interlayer chamber is provided with preheating comb 41, has seal closure in material conveyor arranged outside, and seal closure bottom is provided with preheating inlet, and top is provided with air outlet; Described preheating comb 41 is communicated with preheating inlet.
Described tail gas comb 20 is communicated in body of heater burning interlayer chamber 22 by drainage pipe, and tail gas is burned as fuel.
Rotating cylinder driving mechanism 32 comprises the gear or the sprocket wheel that are arranged on setting gauge rotating cylinder 11 bottoms, and master gear or the head sprocket of gear or sprocket wheel and drive motors are in transmission connection.
Claims (10)
1. a solid organic castoff recycling unit, comprises feed system, cracking body of heater, and heating system and discharge system, is characterized in that: be disposed with feeding preheating chamber, body of heater and grit chamber from top to bottom; The upper end of described feeding preheating chamber is provided with charging aperture, and lower end is provided with discharging opening; The sidewall skin of feeding preheating chamber is provided with preheating interlayer chamber, and be provided with chimney on top, preheating interlayer chamber, the discharging opening position of feeding preheating chamber is set to bullet wide at the top and narrow at the bottom, and heat exchanging chamber is formed at bullet and top, furnace wall, and heat exchanging chamber one side is communicated with the chamber of confluxing; The sidewall skin of body of heater is provided with body of heater burning interlayer chamber and is provided with Gas Pipe, air hose and igniter in bottom, body of heater burning interlayer chamber, and the top in this body of heater burning interlayer chamber is communicated with described preheating interlayer chamber by blast pipe; The bottom of body of heater inner chamber and grit chamber's connecting portion are provided with tower setting gauge; Bottom, grit chamber is provided with slag-drip opening.
2. solid organic castoff recycling unit according to claim 1, it is characterized in that: in the middle part of described grit chamber, vertically run through setting gauge rotating cylinder is installed, the bottom of setting gauge rotating cylinder and rotating cylinder driving mechanism are in transmission connection, and setting gauge rotating cylinder top is connected with described tower setting gauge.
3. solid organic castoff recycling unit according to claim 1, it is characterized in that: described tower setting gauge comprises centering type cone-shaped hood, the conical surface both sides development length difference of centering type cone-shaped hood, long bottom of extending the conical surface and the shorter extension conical surface is respectively arranged with movable fork, and the bottom-hinged of movable fork has laminating scraper plate; Be provided with arc surfaced blanking outlet at body of heater intracavity bottom, described laminating scraper plate mates with arc surfaced blanking outlet.
4. solid organic castoff recycling unit according to claim 2, is characterized in that: setting gauge rotating cylinder is provided with inner chamber, and its bottom is communicated with multifunction additive adding tube, and its top is provided with dispersion heat exchanger tube; Disperse heat exchanger tube laminating to be distributed in setting gauge rotating cylinder inner side or outer surface, and respectively disperse the outlet of heat exchanger tube to be positioned at differing heights.
5. solid organic castoff recycling unit according to claim 3, is characterized in that: outward flange or upper outer edge at described centering type cone-shaped hood are hinged with auxiliary scraper plate, and auxiliary scraper plate and inboard wall of furnace body bottom mating fit together.
6. according to the solid organic castoff recycling unit described in claim 1-5 any one, it is characterized in that: in described feeding preheating chamber, stirring motor rotating shaft is vertically installed, the upper end of stirring motor rotating shaft is connected with stirring motor; The bottom of stirring motor rotating shaft is positioned at bullet position and is disposed with tapered material distributor and screw propulsion blade.
7. solid organic castoff recycling unit according to claim 1, is characterized in that: be provided with hot blast interlayer chamber at described grit chamber lateral wall, bottom, hot blast interlayer chamber is provided with hot blast import, and hot blast interlayer chamber is communicated in respectively grit chamber and body of heater inner chamber; Chimney is provided with breeches pipe, and breeches pipe is communicated with hot blast import by waste heat return pipe.
8. solid organic castoff recycling unit according to claim 1, it is characterized in that: the top in described combustion chamber of furnace body's interlayer chamber is provided with preheating comb, have seal closure in material conveyor arranged outside, seal closure bottom is provided with preheating inlet, and top is provided with air outlet; Described preheating comb is communicated with preheating inlet.
9. solid organic castoff recycling unit according to claim 1, is characterized in that: described in the conflux bottom in chamber be provided with spiral row device for asphalt, chamber its end after supercooling that confluxes is respectively arranged with oil exit pipe and tail gas comb.
10. solid organic castoff recycling unit according to claim 9, is characterized in that: described tail gas comb is communicated in body of heater burning interlayer chamber by drainage pipe, and tail gas is burned as fuel.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520875695.8U CN205261566U (en) | 2015-11-05 | 2015-11-05 | Solid organic waste resource is made up and is put |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520875695.8U CN205261566U (en) | 2015-11-05 | 2015-11-05 | Solid organic waste resource is made up and is put |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205261566U true CN205261566U (en) | 2016-05-25 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520875695.8U Expired - Fee Related CN205261566U (en) | 2015-11-05 | 2015-11-05 | Solid organic waste resource is made up and is put |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205261566U (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105202546A (en) * | 2015-11-05 | 2015-12-30 | 杨西建 | Solid organic waste recycling device |
| CN106287739A (en) * | 2016-10-11 | 2017-01-04 | 郭志男 | Feed garbage combustion device on a kind of suspention fence type |
| CN106838912A (en) * | 2017-01-13 | 2017-06-13 | 安徽未名鼎和环保有限公司 | A kind of refuse disposal installation of anti-extinguishing |
| CN108266734A (en) * | 2016-12-30 | 2018-07-10 | 深圳前海中惠能环保技术有限公司 | A kind of high-moisture rubbish cracking apparatus and method |
| CN109028069A (en) * | 2018-05-23 | 2018-12-18 | 柳州东侯生物能源科技有限公司 | Life refuse high temperature cracking reaction furnace |
| CN117139344A (en) * | 2023-09-12 | 2023-12-01 | 四川云华川科技有限公司 | Domestic waste serialization multilayer pyrolysis reation kettle |
-
2015
- 2015-11-05 CN CN201520875695.8U patent/CN205261566U/en not_active Expired - Fee Related
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105202546A (en) * | 2015-11-05 | 2015-12-30 | 杨西建 | Solid organic waste recycling device |
| CN106287739A (en) * | 2016-10-11 | 2017-01-04 | 郭志男 | Feed garbage combustion device on a kind of suspention fence type |
| CN108266734A (en) * | 2016-12-30 | 2018-07-10 | 深圳前海中惠能环保技术有限公司 | A kind of high-moisture rubbish cracking apparatus and method |
| CN108266734B (en) * | 2016-12-30 | 2019-06-11 | 深圳前海中惠能环保技术有限公司 | A kind of high-moisture rubbish cracking apparatus and method |
| CN106838912A (en) * | 2017-01-13 | 2017-06-13 | 安徽未名鼎和环保有限公司 | A kind of refuse disposal installation of anti-extinguishing |
| CN109028069A (en) * | 2018-05-23 | 2018-12-18 | 柳州东侯生物能源科技有限公司 | Life refuse high temperature cracking reaction furnace |
| CN117139344A (en) * | 2023-09-12 | 2023-12-01 | 四川云华川科技有限公司 | Domestic waste serialization multilayer pyrolysis reation kettle |
| CN117139344B (en) * | 2023-09-12 | 2024-04-09 | 四川云华川科技有限公司 | Domestic waste serialization multilayer pyrolysis reation kettle |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160525 Termination date: 20181105 |
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| CF01 | Termination of patent right due to non-payment of annual fee |