CN107794065A - A kind of discarded object chain type carbonizes the circulatory system - Google Patents
A kind of discarded object chain type carbonizes the circulatory system Download PDFInfo
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- CN107794065A CN107794065A CN201711078603.3A CN201711078603A CN107794065A CN 107794065 A CN107794065 A CN 107794065A CN 201711078603 A CN201711078603 A CN 201711078603A CN 107794065 A CN107794065 A CN 107794065A
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- import
- pyrolysis oven
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- feed bin
- discarded object
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Classifications
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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
- C10B47/18—Destructive distillation of solid carbonaceous materials with indirect heating, e.g. by external combustion with moving charge
-
- 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)
Abstract
A kind of discarded object chain type carbonizes the circulatory system, including feed bin（1）, belted electronic balance（2）, feeding warehouse（3）, pyrolysis oven（4）With pyrolytic carbon feed bin（5）, pyrolysis oven（4）Inner upper is disposed with heat conducting pipe（6）, pyrolysis oven（4）Bottom is provided with discharge port, described feed bin（1）Outlet is located at belted electronic balance（2）Above import, belted electronic balance（2）Outlet is located at feeding warehouse（3）Above import, feeding warehouse（3）Outlet and pyrolysis oven（4）The charging aperture at top is connected, pyrolysis oven（4）Discharge port and pyrolytic carbon feed bin（5）Import is connected.Discarded object passes through belted electronic balance（2）Automatic gauge, pass through pyrolysis oven（4）It is pyrolyzed output charcoal cooling metering dress bag, automatically derived charging discharging ratio, it is possible to achieve it is foolproof to automatically control, facilitate simple and direct.
Description
Technical field
The present invention relates to a kind of system and device, more specifically to a kind of discarded object chain type charing circulatory system, belong to
Resources circulation reutilization technology field.
Background technology
Biomass energy is to be only second to the 4th big energy of the world of oil, coal and natural gas, is had renewable and environment-friendly
Double attribute, account for world's regenerative resource consumption figure 78%；The development and application of biomass energy are to Sustainable Socioeconomic Development
It is significant.Meanwhile a variety of discarded objects such as cow dung, domestic waste, sludge are if recycled, then to the mankind
Living environment produces considerable influence；Therefore, a variety of discarded objects such as biomass and cow dung, domestic waste, sludge synthesis is followed
The discarded object co-generation system that ring utilizes arises at the historic moment.
At present, discarded object declines simultaneously according to own wt in body of heater in pyrolysis oven in existing discarded object carbonization system
It is pyrolyzed, heating-up temperature is also general 450 or so, and uncontrollable pyrolysis of waste time and speed；Therefore product be present
The problems such as quality is not high, energy conversion and utilization rate are low, fuel forming power consumption is high.
The content of the invention
It is an object of the invention to for the uncontrollable pyrolysis of waste time existing for existing discarded object carbonization system
And the problems such as speed, there is provided a kind of discarded object chain type carbonizes the circulatory system.
To achieve the above object, institute is the present invention using technical solution：A kind of discarded object chain type carbonizes the circulatory system,
Including feed bin, belted electronic balance, feeding warehouse, pyrolysis oven and pyrolytic carbon feed bin, described pyrolysis oven inner upper is disposed with heat conduction
Pipe, pyrolysis furnace bottom are provided with discharge port, and described bin outlet is located above belted electronic balance import, described electronic belt
Scale outlet is above feeding warehouse import, and the feeding warehouse outlet is connected with the charging aperture at the top of pyrolysis oven, pyrolysis oven discharging
Mouth is connected with pyrolytic carbon feed bin import.
Also include gas storage system, the gas storage system is connected with the heat conducting pipe import in pyrolysis oven.
Vibrating bunker is provided between described feed bin and belted electronic balance, described bin outlet is located on vibrating bunker
Side, the outlet of described vibrating bunker is above belted electronic balance import.
Described feeding warehouse import is provided with hopper, and the outlet of described belted electronic balance is located above hopper import,
Described hopper outlet is connected with feeding warehouse import.
Also include drive device and PLC, described pyrolysis oven is internally provided with flight chain device, pyrolysis oven
Both ends are respectively arranged with active transmission device and slave drive device, and described flight chain device includes chain, described chain
Multiple scraper plates are provided with bar, chain is connected with active transmission device and slave drive device respectively, described active transmission
Device is connected with drive device, and temperature sensor is provided with described heat conducting pipe, and described temperature sensor controls with PLC
Device is connected, and described drive device is connected with PLC.
Inside described pyrolysis oven heat-preservation cotton is disposed with above heat conducting pipe.
Cooling screw and rubber conveyer are provided between described pyrolysis oven discharge port and pyrolytic carbon feed bin import, institute
The pyrolysis oven discharge port stated is located above cooling screw import, and the outlet of described cooling screw is located at rubber conveyer import
Top, the outlet of described rubber conveyer is above the import of pyrolytic carbon feed bin.
Water cooling hopper and star blanking machine, described pyrolysis oven discharge port are provided with above described cooling screw import
Above water cooling hopper throat, described water cooling hopper outlet is connected with star blanking machine import, described star blanking
Machine outlet is connected with cooling screw import.
Described pyrolytic carbon bin outlet is provided with vibrating bunker.
Compared with prior art, the beneficial effects of the invention are as follows：
1st, discarded object by vibrating bunker electron belt conveyer scale automatic gauge, is pyrolyzed output charcoal by pyrolysis oven and cooled down in the present invention
Metering dress bag, automatically derived charging discharging ratio, it is possible to achieve it is foolproof to automatically control, facilitate simple and direct.
2nd, middle scraper chain device moving belt discarded object movement heating of the present invention, by controlling flight chain device movement speed
Degree and discharging, feed time, it can be controlled so that discarded object stops pyrolysis time.
3rd, the present invention in pyrolysis oven go out caused by gas can give oneself provide the heating power energy；Heating-up temperature is 300-700
Degree and automatic control regulation.
Brief description of the drawings
Fig. 1 is schematic structural view of the invention.
Fig. 2 is pyrolysis oven structural representation in the present invention.
In figure, feed bin 1, belted electronic balance 2, feeding warehouse 3, pyrolysis oven 4, pyrolytic carbon feed bin 5, heat conducting pipe 6, vibrating bunker 7,
Hopper 8, drive device 9, flight chain device 10, heat-preservation cotton 11, cooling screw 12, rubber conveyer 13, water cooling hopper
14, star blanking machine 15, gas cylinder group 16, active transmission device 17, slave drive device 18.
Embodiment
Below in conjunction with brief description of the drawings, the present invention is described in further detail with embodiment.
Referring to Fig. 1, a kind of comprehensive resources regenerate the Poly-generation circulatory system, including feed bin 1, belted electronic balance 2, feeding warehouse 3,
Pyrolysis oven 4 and pyrolytic carbon feed bin 5；The described inner upper of pyrolysis oven 4 is disposed with heat conducting pipe 6, and the bottom of pyrolysis oven 4 is provided with discharging
Mouthful, the discharge port of pyrolysis oven 4 is connected with the import of pyrolytic carbon feed bin 5.The described outlet of feed bin 1 is in the import of belted electronic balance 2
Side, the outlet of described belted electronic balance 2 is above the import of feeding warehouse 3；The described outlet of feeding warehouse 3 and the top of pyrolysis oven 4
Charging aperture is connected.
Referring to Fig. 1, the system also includes gas storage system, described gas storage system and leading in pyrolysis oven 4
The import of heat pipe 6 is connected.The gas storage system is usually gas cylinder group 16.
Referring to Fig. 1, vibrating bunker 7, described feed bin 1 outlet position are provided between described feed bin 1 and belted electronic balance 2
Above vibrating bunker 7, the outlet of described vibrating bunker 7 is above the import of belted electronic balance 2.
Referring to Fig. 1, the outlet of belted electronic balance 2 that the described import of feeding warehouse 3 is provided with described in hopper 8 is located at hopper
Above 8 imports, the outlet of described hopper 8 is connected with the import of feeding warehouse 3.
Referring to Fig. 2, the system also includes drive device 9 and PLC, and described pyrolysis oven 4, which is internally provided with, to be scraped
Plate chain device 10, the both ends of pyrolysis oven 4 are respectively arranged with active transmission device 17 and slave drive device 18.Described scraper chain
Strip device 10 includes chain, is provided with multiple scraper plates on described chain, chain respectively with active transmission device 17 and driven biography
Dynamic device 18 is connected；Described active transmission device 17 is connected with drive device 9.Temperature is provided with described heat conducting pipe 6
Spend sensor；Described temperature sensor is connected with PLC, and described drive device 9 is connected with PLC.
Drive device 9 is moved by the moving belt discarded object of flight chain device 10 and heated, and then controls flight chain device 10 to move speed
Degree and discharging, feed time, it can be controlled so that discarded object stops pyrolysis time.
Referring to Fig. 1, the described top of 4 inside heat conducting pipe of pyrolysis oven 6 is disposed with heat-preservation cotton 11.
Referring to Fig. 1, be provided between the described discharge port of pyrolysis oven 4 and the import of pyrolytic carbon feed bin 5 cooling screw 12 and
Rubber conveyer 13, the described discharge port of pyrolysis oven 4 are located above the import of cooling screw 12；Described cooling screw 12 goes out
Mouth is above the import of rubber conveyer 13, and the outlet of described rubber conveyer 13 is positioned at the import of pyrolytic carbon feed bin 5 top.
Referring to Fig. 1, water cooling hopper 14 and star blanking machine 15 are provided with above the described import of cooling screw 12, it is described
The discharge port of pyrolysis oven 4 be located above the import of water cooling hopper 14, the outlet of described water cooling hopper 14 and the import of star blanking machine 15
It is connected；The described outlet of star blanking machine 15 is connected with the import of cooling screw 12.
Referring to Fig. 1, the outlet of described pyrolytic carbon feed bin 5 is provided with vibrating bunker 7.
Referring to Fig. 1 to Fig. 2, material enters the automatic gauge of belt scale metering 2 by feed bin 1 through vibrating bunker 7, then under
Hopper 8 is pyrolyzed to pyrolysis oven 4.Heated inside pyrolysis oven 4 by heat conducting pipe 6, heating-up temperature is 300-700 degree and automatic control is adjusted
Section；Flight chain device 10 in pyrolysis oven 4 drives material to run, and the temperature on temperature sensor passes to PLC, PLC
Controller controls drive device 9, and then and then control the translational speed of flight chain device 10 and pyrolysis oven 4 discharge, feed time,
So as to realize that pyrolysis rate speed is automatically adjustable.Discarded object discharging is cooled to 280 degree by the temperature of water cooling hopper 14 from 400 degree,
Dropped to again by star blanking machine 15 to the temperature of cooling screw 12 from 280 degree within 60 degree；Entered again by rubber conveyer 13
Enter to the windrow of pyrolytic carbon feed bin 5, then to expecting that pyrolytic carbon hand-filling packs under vibrating bunker 7, pass through pyrolysis oven 4 and be pyrolyzed output
Charcoal cooling metering dress bag, it is automatically derived charging discharging ratio, so as to realize it is foolproof automatically control, facilitate simple and direct.Meanwhile
And first carry out heat supply, pyrolysis oven when temperature reaches 560 degree using the delivery of fuel gas of gas cylinder group 16 to heat conducting pipe 6 during device power-up
4 are discharged by pyrolysis of waste gas and supplies the heating of heat conducting pipe 6 using being the heat supply of pyrolysis oven 4, there are about 68% pyrolysis oven according to statistics
Gas supply heat conducting pipe 6 heats caused by 4.
Referring to Fig. 1 to Fig. 2, cow dung, biomass, domestic waste, sludge etc. are handled using the present apparatus, discarded object is led to
Cross after pyrolysis oven 6 is pyrolyzed and eat the net generation charcoal of dry squeezing, gas, oil product.The charcoal class caused by pyrolysis when pyrolysis temperature is spent for 600-700
（Cow dung charcoal, biomass carbon, municipal refuse inorganic matter, sludge etc.）Equal 4000-7000 kilocalories, incendivity combustion gas（Biological fuel gas,
Cow dung gas, rubbish gas etc.）Equal 2300-3800 kilocalories, combustion oil（Bio-oil, rubbish oil firing）Equal 7000-8000 kilocalories.And
Pyrolysis oven 4 itself produces gas by the conducting self-heating of heat conducting pipe 6, and consumption can maintain to balance from about 68% combustion gas is produced；Heat simultaneously
It is hermetically sealed to solve the casing of stove 4, gaseous-pressure controls -500 to 500 kPas or so, and the temperature of pyrolysis oven 4 can reach 600-900 degree, energy
It is enough that Non-oxygen pyrolytic is carried out to discarded object.
Above content is to combine specific preferred embodiment further description made for the present invention, it is impossible to is assert
The specific implementation of the present invention is confined to these explanations.For general technical staff of the technical field of the invention,
On the premise of not departing from present inventive concept, some simple deduction or replace can also be made, said structure should be all considered as belonging to
Protection scope of the present invention.
Claims (9)
1. a kind of discarded object chain type carbonizes the circulatory system, it is characterised in that：Including feed bin（1）, belted electronic balance（2）, feeding warehouse
（3）, pyrolysis oven（4）With pyrolytic carbon feed bin（5）, described pyrolysis oven（4）Inner upper is disposed with heat conducting pipe（6）, pyrolysis oven（4）
Bottom is provided with discharge port, described feed bin（1）Outlet is located at belted electronic balance（2）Above import, described belted electronic balance
（2）Outlet is located at feeding warehouse（3）Above import, the feeding warehouse（3）Outlet and pyrolysis oven（4）The charging aperture at top is connected,
Pyrolysis oven（4）Discharge port and pyrolytic carbon feed bin（5）Import is connected.
A kind of 2. discarded object chain type charing circulatory system according to claim 1, it is characterised in that：Also include combustion gas storage
Deposit system, the gas storage system and pyrolysis oven（4）In heat conducting pipe（6）Import is connected.
A kind of 3. discarded object chain type charing circulatory system according to claim 1, it is characterised in that：Described feed bin（1）
With belted electronic balance（2）Between be provided with vibrating bunker（7）, described feed bin（1）Outlet is located at vibrating bunker（7）Top, institute
The vibrating bunker stated（7）Outlet is located at belted electronic balance（2）Above import.
A kind of 4. discarded object chain type charing circulatory system according to claim 1, it is characterised in that：Described feeding warehouse
（3）Import is provided with hopper（8）, described belted electronic balance（2）Outlet is located at hopper（8）Above import, under described
Hopper（8）Outlet and feeding warehouse（3）Import is connected.
A kind of 5. discarded object chain type charing circulatory system according to claim 1, it is characterised in that：Also include driving dress
Put（9）And PLC, described pyrolysis oven（4）It is internally provided with flight chain device（10）, pyrolysis oven（4）Distinguish at both ends
It is provided with active transmission device（17）With slave drive device（18）, described flight chain device（10）It is described including chain
Chain on be provided with multiple scraper plates, chain respectively with active transmission device（17）With slave drive device（18）It is connected, institute
The active transmission device stated（17）With drive device（9）It is connected, described heat conducting pipe（6）On be provided with temperature sensor, institute
The temperature sensor stated is connected with PLC, described drive device（9）It is connected with PLC.
A kind of 6. discarded object chain type charing circulatory system according to claim 1, it is characterised in that：Described pyrolysis oven
（4）Internal heat conducting pipe（6）Top is disposed with heat-preservation cotton（11）.
A kind of 7. discarded object chain type charing circulatory system according to claim 1, it is characterised in that：Described pyrolysis oven
（4）Discharge port and pyrolytic carbon feed bin（5）Cooling screw is provided between import（12）And rubber conveyer（13）, described heat
Solve stove（4）Discharge port is located at cooling screw（12）Above import, described cooling screw（12）Outlet conveys positioned at adhesive tape
Machine（13）Above import, described rubber conveyer（13）Outlet is located at pyrolytic carbon feed bin（5）Above import.
A kind of 8. discarded object chain type charing circulatory system according to claim 7, it is characterised in that：Described spiral cooling
Machine（12）Water cooling hopper is provided with above import（14）With star blanking machine（15）, described pyrolysis oven（4）Discharge port is located at water
Cold burden bucket（14）Above import, described water cooling hopper（14）Outlet and star blanking machine（15）Import is connected, described star
Shape blanking machine（15）Outlet and cooling screw（12）Import is connected.
A kind of 9. discarded object chain type carbonization cycle system according to claim 1, it is characterised in that：Described pyrolytic carbon material
Storehouse（5）Outlet is provided with vibrating bunker（7）.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711078603.3A CN107794065A (en) | 2017-11-06 | 2017-11-06 | A kind of discarded object chain type carbonizes the circulatory system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711078603.3A CN107794065A (en) | 2017-11-06 | 2017-11-06 | A kind of discarded object chain type carbonizes the circulatory system |
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| CN107794065A true CN107794065A (en) | 2018-03-13 |
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| CN201711078603.3A Pending CN107794065A (en) | 2017-11-06 | 2017-11-06 | A kind of discarded object chain type carbonizes the circulatory system |
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Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2004174426A (en) * | 2002-11-28 | 2004-06-24 | Asia Plant Service Kk | Waste treatment apparatus |
| DE102004008621A1 (en) * | 2004-02-21 | 2005-09-08 | Jeschar, Rudolf, Prof. Dr.-Ing. Dr.-Ing. E.h. | Transportable or stationary hearth-type furnace reactor, to transform solid and paste organic materials to processed gas, comprises cubic reactor, vapor inlet, a chain conveyor, a cover with passages and a supporting flame mechanism |
| CN106833696A (en) * | 2017-01-23 | 2017-06-13 | 武汉光谷蓝焰新能源股份有限公司 | A kind of biomass pyrolytic polygenerations systeme |
| CN207619332U (en) * | 2017-11-06 | 2018-07-17 | 华中农业大学 | A kind of waste chain type charing circulatory system |
-
2017
- 2017-11-06 CN CN201711078603.3A patent/CN107794065A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2004174426A (en) * | 2002-11-28 | 2004-06-24 | Asia Plant Service Kk | Waste treatment apparatus |
| DE102004008621A1 (en) * | 2004-02-21 | 2005-09-08 | Jeschar, Rudolf, Prof. Dr.-Ing. Dr.-Ing. E.h. | Transportable or stationary hearth-type furnace reactor, to transform solid and paste organic materials to processed gas, comprises cubic reactor, vapor inlet, a chain conveyor, a cover with passages and a supporting flame mechanism |
| CN106833696A (en) * | 2017-01-23 | 2017-06-13 | 武汉光谷蓝焰新能源股份有限公司 | A kind of biomass pyrolytic polygenerations systeme |
| CN207619332U (en) * | 2017-11-06 | 2018-07-17 | 华中农业大学 | A kind of waste chain type charing circulatory system |
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