CN105485690A - Combustible rubbish treatment device - Google Patents
Combustible rubbish treatment device Download PDFInfo
- Publication number
- CN105485690A CN105485690A CN201511011123.6A CN201511011123A CN105485690A CN 105485690 A CN105485690 A CN 105485690A CN 201511011123 A CN201511011123 A CN 201511011123A CN 105485690 A CN105485690 A CN 105485690A
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- CN
- China
- Prior art keywords
- flue
- pipe
- combustiblerefuse
- treating apparatus
- pyrolysis oven
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/02—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
- F23G5/027—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/02—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
- F23G5/033—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment comminuting or crushing
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/02—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
- F23G5/04—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment drying
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/44—Details; Accessories
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/44—Details; Accessories
- F23G5/442—Waste feed arrangements
- F23G5/444—Waste feed arrangements for solid waste
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2201/00—Pretreatment
- F23G2201/30—Pyrolysing
- F23G2201/301—Treating pyrogases
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
The invention relates to the field of rubbish treatment, in particular to a combustible rubbish treatment device. The combustible rubbish treatment device comprises a feeding system, a pyrolysis treatment system and a smoke treatment system. The combustible rubbish treatment device is characterized in that the feeding system comprises a feeding hopper connected with a feeding opening I in the upper end of a smashing and pushing all-in-one machine; the smashing and pushing all-in-one machine is connected with a pyrolysis furnace; the pyrolysis furnace is connected with a water spraying dust remover, and the water spraying dust remover is connected with the bottom end of a wet method dust remover through a smoke pipe I and a smoke pipe II; and an evacuation pipe is connected to the upper end of the wet method dust remover, the lower end of the wet method dust remover is connected with a water return pipe, and the water return pipe is connected with a circulation water pump arranged in a circulation water pool. According to the combustible rubbish treatment device, rubbish molecule high temperature swarming thermal cracking is adopted, open fire burning is not generated, continuous pyrolysis treatment can be achieved without consuming other energy, the combustible rubbish treatment device is good in adaptability to treated combustible rubbish, the environment is not polluted, and the combustible rubbish treatment device is efficient and environment-friendly.
Description
(1) technical field
The present invention relates to field of garbage disposal, particularly a kind of combustiblerefuse treating apparatus.
(2) background technology
Along with the development of society and the raising of people's living standard, the kind of rubbish is also increasing day by day, the processing mode of rubbish is also constantly being developed, particularly the recycling of rubbish is become to the main trend of garbage disposal, character according to variety classes rubbish recycles rubbish, rubbish can be made to turn waste into wealth, society and country are benefited.
Realize the recycling of rubbish, first to classify to rubbish, although advocating people at present loses in the dustbin of correspondence according to the prompting on dustbin by rubbish when abandoning rubbish, in real life, people seldom abandon rubbish according to classified prompt.Like this, very large difficulty is brought to the recycling of follow-up rubbish.
The current device major part complicated structure that can realize garbage disposal, and cost is higher, utilizes artificial separation rubbish can employ too much manpower.A lot of pernicious gas and dust can be produced in garbage processing procedure, not only be unfavorable for environment but also murder by poisoning is produced to the health of employee.
(3) summary of the invention
The present invention, in order to make up the deficiencies in the prior art, provides a kind of rational in infrastructure, combustiblerefuse treating apparatus easy to use.
The present invention is achieved through the following technical solutions:
A kind of combustiblerefuse treating apparatus, comprises feed system, pyrolysis treatment systems and smoke processing system, it is characterized in that: described feed system comprises loading hopper, and this loading hopper advances the upper end charging aperture I of all-in-one to be connected with pulverizing; Described pulverizing advances all-in-one to be connected with the charging aperture II of pyrolysis oven by feed pipe; Described pyrolysis oven comprises the heat-insulation layer in the middle of inwall, outer wall and inner and outer wall; Described pyrolysis oven lower front part and rear end are respectively provided with a vent; Described pyrolysis oven lower end is provided with circular air inlet pipe, and this blast pipe is provided with hot energy storage interchanger, and hot energy storage interchanger one end other end that is connected with blast pipe is communicated with the inwall of pyrolysis oven; Described pyrolysis oven bottom is provided with spiral automatic ash-removing device, and top is provided with exhanst gas outlet; Described exhanst gas outlet is connected with Water spray deduster, and this Water spray deduster lower end is connected with flue I, and flue I is provided with flue II, and flue I port is provided with air-introduced machine, and this air-introduced machine is connected with flue II by pipeline; Described flue II is provided with electromagnetic induction heater; Described flue II end is connected with Wet-electric duster bottom; Described Wet-electric duster upper end is connected with evacuated tube, and lower end is connected with return pipe, and this return pipe is connected with the water circulating pump be located in circulating water pool; Described water circulating pump is connected with water inlet pipe, and this water inlet pipe is connected with the upper end of Water spray deduster.
Described pulverizing advances all-in-one to comprise fuselage, comprises crushing chamber and advance chamber in this fuselage; Be provided with grinder-mixer in described crushing chamber, this grinder-mixer one end is located on crushing chamber inwall, and the other end is connected with the driven wheel be located at outside crushing chamber; Described driven wheel is located in gear chamber, and this driven wheel is engaged with driving wheel; Described driving wheel respectively with motor I with advance rotating shaft and be connected; Described propelling rotating shaft is located at and advances in chamber, is positioned at grinder-mixer lower end.
Above-mentioned grinder-mixer comprises rotating shaft and is located at the circular knife page in rotating shaft.
Described hot energy storage interchanger comprises ajutage, helical heating pipe and discharge pipe.
Described ajutage one end is connected with blast pipe, and the other end is connected with helical heating pipe; Described helical heating pipe is connected with pyrolysis oven by discharge pipe.
Described ajutage is coated with magnet.
Described blast pipe is provided with tune airduct, and this tune airduct is provided with control valve.
Described spiral automatic ash-removing device comprises taper except ash silo, and should be provided with screw rod except in ash silo, screw rod is driven by motor II; Described one end relative with motor II except ash silo is provided with grey door.
Be provided with control valve I in described flue I, in flue II, be provided with control valve II; Between the pipeline opening that described control valve I is located at flue II and air-introduced machine; Described control valve II is located at the connector place of flue II and flue I.
Described pyrolysis oven is cylindrical shape or cuboid.
The invention has the beneficial effects as follows:
(1) the present invention adopts spiral propeller to carry out the feeding mechanism of pyrolysis oven, and at the charging aperture of spiral propeller, adds crushing knife, first by garbage crushing, is formed to pulverize and advances all-in-one; Solve such as carton, friperie, etc. the difficult problem of large volume rubbish not easily charging;
(2) this device adopts dipping type screw feeding machine to be pyrolysis oven material loading, and solve continuous feed, charging aperture easily produces the difficult problem emitting flue gas;
(3) the hot energy storage heat exchanger of pyrolysis oven is combustion-supporting by entering body of heater again after cold air heating, improves the thermal efficiency.Air inlet has control valve, regulates the size of intake as required, is conducive to keeping constant temperature in stove;
(4) the present invention adopts rubbish molecule high temperature to spring up thermal cracking, does not produce naked light burning, makes full use of rubbish self-energy and carries out heating, drying to the new rubbish added, do not consume other energy and realize continuous pyrolysis process, good to the combustiblerefuse adaptability of process;
(5) the present invention adopts spiral soot blower automatic ash discharge, and the structure of stove inner bottom part plenum area is tapered, is conducive to the collection of lime-ash, improves labour intensity and the working environment of operator;
(6) the present invention adopts electromagnetic induction heater to carry out post bake cracking to flue gas, eliminates the compositions such as pernicious gas bioxin, improves pyrolysis efficiency and consumes energy few.
(7) the present invention is on the basis of spraying and dedusting, and adopt Wet-electric duster to carry out purified treatment to flue gas further, the flue gas cleannes of discharge are high, realize harmless treatment;
(8) the present invention adopts circulating water pool decontamination cycle water, realizes recycling of water, realizes water saving and without sewage discharge.
(4) accompanying drawing explanation
Below in conjunction with accompanying drawing, the present invention is further illustrated.
Fig. 1 is structural representation of the present invention.
Fig. 2 is that the present invention pulverizes the structural representation advancing all-in-one.
Fig. 3 is the Facad structure schematic diagram of pyrolysis oven of the present invention.
Fig. 4 is the side structure schematic diagram of pyrolysis oven of the present invention.
Fig. 5 is the present invention's hot energy storage exchanger arrangement schematic diagram.
Fig. 6 is the structural representation of blast pipe of the present invention.
In figure, 1 loading hopper, 2 pulverize propelling all-in-one, 3 feed pipes, 4 pyrolysis ovens, 5 vents, 6 blast pipes, 7 hot energy storage interchangers, 8 delivery ports, 9 Water spray dedusters, 10 electromagnetic induction heaters, 11 Wet-electric dusters, 12 air-introduced machines, 13 control valves I, 14 control valves II, 15 circulating water pools, 16 water circulating pumps, 17 water inlet pipes, 18 return pipes, 19 evacuated tube, 20 spiral automatic ash-removing devices, 101 charging apertures I, 201 crushing chambers, 202 advance chamber, 203 grinder-mixers, 204 driven wheels, 205 gear chamber, 206 driving wheels, 207 motor I, 208 advance rotating shaft, 401 charging apertures II, 402 exhanst gas outlets, 601 adjust airduct, 602 control valves, 701 ajutages, 702 helical heating pipes, 703 discharge pipes, 704 magnet, 901 flues I, 902 flues II, 2001 except ash silo, 2002 screw rods, 2003 motor II, 2004 grey doors.
(5) detailed description of the invention
Accompanying drawing is a kind of specific embodiment of the present invention.This embodiment comprises feed system, pyrolysis treatment systems and smoke processing system, and described feed system comprises loading hopper 1, and this loading hopper 1 advances the upper end charging aperture I 101 of all-in-one 2 to be connected with pulverizing; Described pulverizing advances all-in-one 2 to be connected with the charging aperture II 401 of pyrolysis oven 4 by feed pipe 3; Described pyrolysis oven 4 comprises the heat-insulation layer in the middle of inwall, outer wall and inner and outer wall; Described pyrolysis oven 4 lower front part and rear end are respectively provided with a vent 5; Described pyrolysis oven 4 lower end is provided with circular air inlet pipe 6, and this blast pipe 6 is provided with hot energy storage interchanger 7, and hot energy storage interchanger 7 one end other end that is connected with blast pipe 6 is communicated with the inwall of pyrolysis oven 4; Described pyrolysis oven 4 bottom is provided with spiral automatic ash-removing device 20, and top is provided with exhanst gas outlet 402; Described exhanst gas outlet 402 is connected with Water spray deduster 9, this Water spray deduster 9 lower end is connected with flue I 901, flue I 901 is provided with flue II 902, and flue I 901 port is provided with air-introduced machine 12, and this air-introduced machine 12 is connected with flue II 902 by pipeline; Described flue II 902 is provided with electromagnetic induction heater 10; Described flue II 902 end is connected with Wet-electric duster 11 bottom; Described Wet-electric duster 11 upper end is connected with evacuated tube 19, and lower end is connected with return pipe 18, and this return pipe 18 is connected with the water circulating pump 16 be located in circulating water pool 15; Described water circulating pump 16 is connected with water inlet pipe 17, and this water inlet pipe 17 is connected with the upper end of Water spray deduster 9.
Described pulverizing advances all-in-one 2 to comprise fuselage, comprises crushing chamber 201 and advance chamber 202 in this fuselage; Be provided with grinder-mixer 203 in described crushing chamber 201, this grinder-mixer 203 one end is located on crushing chamber 201 inwall, and the other end is connected with the driven wheel 204 be located at outside crushing chamber 201; Described driven wheel 204 is located in gear chamber 205, and this driven wheel 204 is engaged with driving wheel 206; Described driving wheel 206 respectively with motor I 207 with advance rotating shaft 208 and be connected; Described propelling rotating shaft 208 is located at and advances in chamber 202, is positioned at grinder-mixer 203 lower end.
Above-mentioned grinder-mixer comprises rotating shaft and is located at the circular knife page in rotating shaft.
Described hot energy storage interchanger 7 comprises ajutage 701, helical heating pipe 702 and discharge pipe 703.
Described ajutage 701 one end is connected with blast pipe 6, and the other end is connected with helical heating pipe 702; Described helical heating pipe 702 is connected with pyrolysis oven 4 by discharge pipe 703.
Described ajutage 701 is coated with magnet 704.
Described blast pipe 6 is provided with adjusts airduct 601, and this tune airduct 601 is provided with control valve 602.
Described spiral automatic ash-removing device 20 comprises rectangle except ash silo 2001, and should be provided with screw rod 2002 except in ash silo 2001, screw rod 2002 is driven by motor II 2003; Described one end relative with motor II 2003 except ash silo 2001 is provided with grey door 2004.
Be provided with control valve I 13 in described flue I 901, in flue II 902, be provided with control valve II 14; Described control valve I 13 is located between the pipeline opening of flue II 902 and air-introduced machine 12; Described control valve II 14 is located at the connector place of flue II 902 and flue I 901.
When the present invention uses, being sent to pulverize by loading hopper 1 by rubbish advances in all-in-one 2, motor I 207 drives grinder-mixer 203 and advances axis of rotation 208, due to driven wheel 204 with driving wheel 206 is in different size makes grinder-mixer 203 and advance axis of rotation 208 rotating speed different, therefore rubbish by grinder-mixer 203 and advance axis of rotation 208 the shearing force that produces carry out rotations segmentation, and then to be carried by the rubbish of propelling axis of rotation 208 to rubbing.
Ignited by vent 5 after the rubbish rubbed enters into pyrolysis oven, the amount simultaneously by regulating the control valve 602 of blast pipe 6 to control the oxygen entered, and then keep the temperature constant in pyrolysis oven 4; Air is heated by hot energy storage interchanger 7 after being magnetized by magnet 704 again, then enters in stove combustion-supporting, by the hot-air after magnetization with adding the flameless combustion contributing to rubbish, burns more abundant.
The flue gas that refuse pyrolysis produces enters Water spray deduster 9 dedusting by flue II 902 under air-introduced machine 12 draft, then pernicious gas is eliminated through electromagnetic induction heater 10 pyrolysis, enter Wet-electric duster 11 dedusting further again, the flue gas after purified treatment is emptying by evacuated tube 19.
Claims (10)
1. a combustiblerefuse treating apparatus, comprises feed system, pyrolysis treatment systems and smoke processing system, it is characterized in that: described feed system comprises loading hopper, and this loading hopper advances the upper end charging aperture I of all-in-one to be connected with pulverizing; Described pulverizing advances all-in-one to be connected with the charging aperture II of pyrolysis oven by feed pipe; Described pyrolysis oven comprises the heat-insulation layer in the middle of inwall, outer wall and inner and outer wall; Described pyrolysis oven lower front part and rear end are respectively provided with a vent; Described pyrolysis oven lower end is provided with circular air inlet pipe, and this blast pipe is provided with hot energy storage interchanger, and hot energy storage interchanger one end other end that is connected with blast pipe is communicated with the inwall of pyrolysis oven; Described pyrolysis oven bottom is provided with spiral automatic ash-removing device, and top is provided with exhanst gas outlet; Described exhanst gas outlet is connected with Water spray deduster, and this Water spray deduster lower end is connected with flue I, and flue I is provided with flue II, and flue I port is provided with air-introduced machine, and this air-introduced machine is connected with flue II by pipeline; Described flue II is provided with electromagnetic induction heater; Described flue II end is connected with Wet-electric duster bottom; Described Wet-electric duster upper end is connected with evacuated tube, and lower end is connected with return pipe, and this return pipe is connected with the water circulating pump be located in circulating water pool; Described water circulating pump is connected with water inlet pipe, and this water inlet pipe is connected with the upper end of Water spray deduster.
2. combustiblerefuse treating apparatus according to claim 1, is characterized in that: described pulverizing advances all-in-one to comprise fuselage, comprises crushing chamber and advance chamber in this fuselage; Be provided with grinder-mixer in described crushing chamber, this grinder-mixer one end is located on crushing chamber inwall, and the other end is connected with the driven wheel be located at outside crushing chamber; Described driven wheel is located in gear chamber, and this driven wheel is engaged with driving wheel; Described driving wheel respectively with motor I with advance rotating shaft and be connected; Described propelling rotating shaft is located at and advances in chamber, is positioned at grinder-mixer lower end.
3. combustiblerefuse treating apparatus according to claim 2, is characterized in that: described grinder-mixer comprises rotating shaft and is located at the circular knife page in rotating shaft.
4. combustiblerefuse treating apparatus according to claim 1, is characterized in that: described hot energy storage interchanger comprises ajutage, helical heating pipe and discharge pipe.
5. combustiblerefuse treating apparatus according to claim 4, is characterized in that: described ajutage one end is connected with blast pipe, and the other end is connected with helical heating pipe; Described helical heating pipe is connected with pyrolysis oven by discharge pipe.
6. combustiblerefuse treating apparatus according to claim 4, is characterized in that: described ajutage is coated with magnet.
7. combustiblerefuse treating apparatus according to claim 1, is characterized in that: described blast pipe is provided with tune airduct, this tune airduct is provided with control valve.
8. combustiblerefuse treating apparatus according to claim 1, is characterized in that: described spiral automatic ash-removing device comprises rectangle except ash silo, and should be provided with screw rod except in ash silo, screw rod is driven by motor II; Described one end relative with motor II except ash silo is provided with grey door.
9. combustiblerefuse treating apparatus according to claim 1, is characterized in that: be provided with control valve I in described flue I, be provided with control valve II in flue II; Between the pipeline opening that described control valve I is located at flue II and air-introduced machine; Described control valve II is located at the connector place of flue II and flue I.
10. combustiblerefuse treating apparatus according to claim 1, is characterized in that: described pyrolysis oven is cylindrical shape or cuboid.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201511011123.6A CN105485690B (en) | 2015-12-30 | 2015-12-30 | A kind of combustiblerefuse processing unit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201511011123.6A CN105485690B (en) | 2015-12-30 | 2015-12-30 | A kind of combustiblerefuse processing unit |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN105485690A true CN105485690A (en) | 2016-04-13 |
| CN105485690B CN105485690B (en) | 2018-07-06 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201511011123.6A Expired - Fee Related CN105485690B (en) | 2015-12-30 | 2015-12-30 | A kind of combustiblerefuse processing unit |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105485690B (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107906528A (en) * | 2017-11-10 | 2018-04-13 | 东台市建东机械制造有限公司 | A kind of incinerator of solid waste processing |
| CN110898597A (en) * | 2019-12-17 | 2020-03-24 | 山东农洁环保有限公司 | Oxygen-control low-temperature carbonization pyrolysis garbage treatment method |
| CN111006216A (en) * | 2019-12-17 | 2020-04-14 | 山东农洁环保有限公司 | Oxygen-control carbonization pyrolysis garbage treatment device |
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| CN205372563U (en) * | 2015-12-30 | 2016-07-06 | 刘清 | Flammable refuse treatment device |
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2015
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| CN2178842Y (en) * | 1993-09-25 | 1994-10-05 | 李正安 | Vertical boiler with ringlike preheating wind channel |
| CN2462252Y (en) * | 2001-01-10 | 2001-11-28 | 武进市常宁环保设备有限公司 | Heat decomposing garbage incinerator |
| JP2006153408A (en) * | 2004-12-01 | 2006-06-15 | Jietsuto Ro:Kk | Induction heating melting furnace |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN107906528A (en) * | 2017-11-10 | 2018-04-13 | 东台市建东机械制造有限公司 | A kind of incinerator of solid waste processing |
| CN110898597A (en) * | 2019-12-17 | 2020-03-24 | 山东农洁环保有限公司 | Oxygen-control low-temperature carbonization pyrolysis garbage treatment method |
| CN111006216A (en) * | 2019-12-17 | 2020-04-14 | 山东农洁环保有限公司 | Oxygen-control carbonization pyrolysis garbage treatment device |
Also Published As
| Publication number | Publication date |
|---|---|
| CN105485690B (en) | 2018-07-06 |
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Granted publication date: 20180706 Termination date: 20191230 |