CN107828433A - A kind of comprehensive castoff regenerative energy multi-connection production. art system - Google Patents
A kind of comprehensive castoff regenerative energy multi-connection production. art system Download PDFInfo
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- CN107828433A CN107828433A CN201711078600.XA CN201711078600A CN107828433A CN 107828433 A CN107828433 A CN 107828433A CN 201711078600 A CN201711078600 A CN 201711078600A CN 107828433 A CN107828433 A CN 107828433A
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- outlet
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- pyrolysis oven
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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
- C10B47/28—Other processes
- C10B47/32—Other processes in ovens with mechanical conveying means
- C10B47/40—Other processes in ovens with mechanical conveying means with endless conveying devices
-
- 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
- C10B57/00—Other carbonising or coking processes; Features of destructive distillation processes in general
-
- 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
- C10B57/00—Other carbonising or coking processes; Features of destructive distillation processes in general
- C10B57/16—Features of high-temperature carbonising processes
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
- Y02P20/133—Renewable energy sources, e.g. sunlight
Abstract
A kind of comprehensive castoff regenerative energy multi-connection production. art system, wherein feed bin（1）Outlet is located at belted electronic balance（3）Above import, belted electronic balance（3）Outlet is located at feeding warehouse（5）Above import, feeding warehouse（5）Outlet and pyrolysis oven（6）The charging aperture at top is connected, pyrolysis oven（6）Gas outlet and tar synthesizer（13）Air inlet is connected, tar synthesizer（13）Gas outlet and spray synthesizer（14）Air inlet is connected, and sprays synthesizer（14）Top gas outlet and absorption synthesizer（16）Air inlet is connected, and sprays synthesizer（14）Outlet at bottom and tar and pyrolkigneous liquid collecting pit（18）It is connected, adsorbs synthesizer（16）Gas outlet and combustion gas surge tank（17）Air inlet is connected, pyrolysis oven（6）Discharge port and pyrolytic carbon feed bin（11）Import is connected.Realize discarded object coproduction comprehensively utilize, and can realize it is foolproof 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 comprehensive castoff regenerative energy multi-connection production. art
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 co-generation 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 co-generation system
A kind of and the problems such as speed, there is provided comprehensive castoff regenerative energy multi-connection production. art system.
To achieve the above object, institute is the present invention using technical solution：A kind of comprehensive castoff regenerative energy multi-connection
Production. art system, including feed bin, belted electronic balance, feeding warehouse, pyrolysis oven, pyrolytic carbon feed bin, tar synthesizer, spray synthesis
Device, circulating water pool, absorption synthesizer, combustion gas surge tank, described pyrolysis oven inner upper are disposed with heat conducting pipe, are pyrolyzed furnace bottom
Be provided with discharge port, described bin outlet is located above belted electronic balance import, the outlet of described belted electronic balance be located at into
Above feed bin import, the feeding warehouse outlet is connected with the charging aperture at the top of pyrolysis oven, described pyrolysis oven gas outlet and Jiao
Oily synthesizer air inlet is connected, and described tar synthesizer gas outlet is connected with spray synthesizer air inlet, tar synthesis
Device liquid outlet is connected with tar and pyrolkigneous liquid collecting pit, and gas outlet is entered with absorption synthesizer at the top of described spray synthesizer
Gas port is connected, and spray synthesizer outlet at bottom is connected with tar and pyrolkigneous liquid collecting pit, described absorption synthesizer outlet
Mouth is connected with combustion gas buffer tank inlet, and absorption synthesizer outlet at bottom is connected with tar and pyrolkigneous liquid collecting pit, is pyrolyzed
Stove discharge port 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.
Described combustion gas buffer tank outlet is connected with the heat conducting pipe import in pyrolysis oven.
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.
Compared with prior art, the beneficial effects of the invention are as follows：
1st, the present invention realizes that discarded object coproduction comprehensively utilizes, and discarded object is led to by vibrating bunker electron belt conveyer scale automatic gauge
Cross pyrolysis oven pyrolysis output charcoal cooling metering dress bag, automatically derived charging discharging ratio, it is possible to achieve foolproof to automatically control, side
Just it is simple and direct.
2nd, moved and heated by flight chain device moving belt discarded object in the present invention, by controlling flight chain device to move
Dynamic speed and discharging, feed time, 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, vibrating bunker 2, belted electronic balance 3, hopper 4, feeding warehouse 5, pyrolysis oven 6, water cooling hopper 7, star
Shape blanking machine 8, cooling screw 9, rubber conveyer 10, pyrolytic carbon feed bin 11, vibrating bunker 12, tar synthesizer 13, spray
Synthesizer 14, circulating water pool 15, adsorb synthesizer 16, combustion gas surge tank 17, tar and pyrolkigneous liquid collecting pit 18, gas cylinder group
19, roots blower 20, heat conducting pipe 21, flight chain device 22, drive device 23, heat-preservation cotton 24, active transmission device 25 is driven
Transmission device 26.
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 castoff regenerative energy multi-connection production. art system, including feed bin 1, belted electronic balance 3, enter
Feed bin 5, pyrolysis oven 6, pyrolytic carbon feed bin 11, tar synthesizer 13, spray synthesizer 14, circulating water pool 15, absorption synthesizer 16,
Combustion gas surge tank 17.The described inner upper of pyrolysis oven 6 is disposed with heat conducting pipe 21, and the bottom of pyrolysis oven 6 is provided with discharge port；Pyrolysis
The discharge port of stove 6 is connected with the import of pyrolytic carbon feed bin 11.
Referring to Fig. 1, above the import of belted electronic balance 3, described belted electronic balance 3 exports the outlet of described feed bin 1
Above the import of feeding warehouse 5；The described outlet of feeding warehouse 5 is connected with the charging aperture at the top of pyrolysis oven 6, the pyrolysis oven 6
Gas outlet be connected with the air inlet of tar synthesizer 13.The described gas outlet of tar synthesizer 13 and the spray air inlet of synthesizer 14
Mouth is connected, and the liquid outlet of tar synthesizer 13 is connected with tar and pyrolkigneous liquid collecting pit 18；Described spray synthesizer 14
Top gas outlet is connected with the absorption air inlet of synthesizer 16.Spray the outlet at bottom of synthesizer 14 and tar and pyrolkigneous liquid collecting pit
18 are connected, and the described gas outlet of absorption synthesizer 16 is connected with the air inlet of combustion gas surge tank 17；Adsorb the bottom of synthesizer 16
Outlet is connected with tar and pyrolkigneous liquid collecting pit 18.
Referring to Fig. 1, the system also includes gas storage system, described gas storage system and leading in pyrolysis oven 6
The import of heat pipe 21 is connected.The gas storage system is usually gas cylinder group 19.
Referring to Fig. 1, vibrating bunker 2, described feed bin 1 outlet position are provided between described feed bin 1 and belted electronic balance 3
Above vibrating bunker 2, the outlet of described vibrating bunker 2 is above the import of belted electronic balance 3.
Referring to Fig. 1, the described import of feeding warehouse 5 is provided with hopper 4, and the outlet of described belted electronic balance 3 is located at blanking
Struggle against above 4 imports, the outlet of described hopper 4 is connected with the import of feeding warehouse 5.
Referring to Fig. 1, the described gas outlet of combustion gas surge tank 17 is connected with the import of heat conducting pipe 21 in pyrolysis oven 6.
Referring to Fig. 2, the system also includes drive device 23 and PLC, and described pyrolysis oven 6, which is internally provided with, to be scraped
Plate chain device 22, the both ends of pyrolysis oven 6 are respectively arranged with active transmission device 25 and slave drive device 26.Described scraper chain
Strip device 22 includes chain, is provided with multiple scraper plates on described chain, chain respectively with active transmission device 25 and driven biography
Dynamic device 26 is connected；Described active transmission device 25 is connected with drive device 23.Temperature is provided with described heat conducting pipe 5
Sensor is spent, described temperature sensor is connected with PLC, and described drive device 23 is connected with PLC.
Drive device 23 is moved by the moving belt discarded object of flight chain device 22 and heated, and then controls flight chain device 22 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 6 inside heat conducting pipe of pyrolysis oven 21 is disposed with heat-preservation cotton 24.
Referring to Fig. 1, be provided between the described discharge port of pyrolysis oven 6 and the import of pyrolytic carbon feed bin 11 cooling screw 9 and
Rubber conveyer 10；The described discharge port of pyrolysis oven 6 is located above the import of cooling screw 9, and described cooling screw 9 exports
Above the import of rubber conveyer 10, the outlet of described rubber conveyer 10 is above the import of pyrolytic carbon feed bin 11.
Referring to Fig. 1, water cooling hopper 7 and star blanking machine 8 are provided with above the described import of cooling screw 9；Described
The discharge port of pyrolysis oven 6 is located above the import of water cooling hopper 7, and the outlet of described water cooling hopper 7 is connected with the import of star blanking machine 8
Connect, the outlet of described star blanking machine 8 is connected with the import of cooling screw 9.
Referring to Fig. 1, the outlet of described pyrolytic carbon feed bin 11 is provided with vibrating bunker 2.
Referring to Fig. 1 to Fig. 2, material enters the automatic gauge of belt scale metering 3 by feed bin 1 through vibrating bunker 2, then under
Hopper 4 is pyrolyzed to pyrolysis oven 6.Heated inside pyrolysis oven 6 by heat conducting pipe 5, heating-up temperature is 300-700 degree and automatic control is adjusted
Section；Flight chain device 22 in pyrolysis oven 6 drives material to run, and the temperature on temperature sensor passes to PLC, PLC
Controller controls drive device 23, and then and then when controlling the translational speed of flight chain device 22 and the pyrolysis oven 6 to discharge, feed
Between, so as to realize that pyrolysis rate speed is automatically adjustable.Discarded object discharging is cooled to 280 by the temperature of water cooling hopper 7 from 400 degree
Degree, then dropped to by star blanking machine 8 to the temperature of cooling screw 9 from 280 degree within 60 degree；Entered again by rubber conveyer 10
Enter to the windrow of pyrolytic carbon feed bin 11, then to expecting that pyrolytic carbon hand-filling packs under vibrating bunker 2, pass through the pyrolysis production of pyrolysis oven 6
Go out 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.Together
When, and first carry out heat supply, heat when temperature reaches 560 degree using the delivery of fuel gas of gas cylinder group 19 to heat conducting pipe 21 during device power-up
Stove 6 is solved by pyrolysis of waste discharging gas, is carried out by the gas outlet of pyrolysis oven 6 to tar synthesizer 13 at dedusting
Reason, then separately receive tar and pyrolkigneous liquid to spray synthesizer 14 purification tar and pyrolkigneous liquid, tar and pyrolkigneous liquid collecting pit 18
Collection；By adsorbing, synthesizer 16 carries out sulphur to gas and acid purification, last combustion gas surge tank 17 are collected and supply heat conducting pipe again
21 heating there are about gas supply heat conducting pipe 21 caused by 68% pyrolysis oven 6 and heat according to statistics using being the heat supply of pyrolysis oven 6；This process
In and pressure feed heat conducting pipe 21 increased by roots blower 20, if gas hypertonia occurs or negative pressure is too low, combustion gas is prevented
Quick-fried valve（Safety-valve）It can automatically turn on and be protected,
Referring to Fig. 1 to Fig. 2, cow dung, biomass, domestic waste, sludge etc. are handled using the present apparatus, discarded object is passed through into heat
Solution stove 6 eats dry squeeze and produces charcoal, gas, oil product only after being pyrolyzed.The charcoal class caused by pyrolysis when pyrolysis temperature is spent for 600-700（Ox
Excrement charcoal, biomass carbon, municipal refuse inorganic matter, sludge etc.）Equal 4000-7000 kilocalories, incendivity combustion gas（Biological fuel gas, ox
Excrement gas, rubbish gas etc.）Equal 2300-3800 kilocalories, combustion oil（Bio-oil, rubbish oil firing）Equal 7000-8000 kilocalories.It is and hot
Solve stove 6 itself production gas and combustion gas ash content is removed by tar synthesizer 13, then oil and pyrolkigneous liquid are removed to spray synthesizer 14
Purification, sulphur and acid in moisture and combustion gas are purified to absorption synthesizer 16, finally to surge tank memory storage.The gas of purification passes through
The conducting self-heating of heat conducting pipe 21, consumption can maintain to balance from about 68% combustion gas is produced；The casing of pyrolysis oven 6 is hermetically sealed simultaneously, gas pressure
Power controls -500 to 500 kPas or so, and the temperature of pyrolysis oven 6 can reach 600-900 degree, and anaerobic heat can be carried out to discarded object
Solution.
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 (10)
- A kind of 1. comprehensive castoff regenerative energy multi-connection production. art system, it is characterised in that：Including feed bin（1）, belted electronic balance （3）, feeding warehouse（5）, pyrolysis oven（6）, pyrolytic carbon feed bin（11）, tar synthesizer（13）, spray synthesizer（14）, circulating water pool （15）, absorption synthesizer（16）, combustion gas surge tank（17）, described pyrolysis oven（6）Inner upper is disposed with heat conducting pipe（21）, heat Solve stove（6）Bottom is provided with discharge port, described feed bin（1）Outlet is located at belted electronic balance（3）Above import, described electronics Belt conveyer scale（3）Outlet is located at feeding warehouse（5）Above import, the feeding warehouse（5）Outlet and pyrolysis oven（6）The charging aperture phase at top Connection, described pyrolysis oven（6）Gas outlet and tar synthesizer（13）Air inlet is connected, described tar synthesizer（13）Go out Gas port and spray synthesizer（14）Air inlet is connected, tar synthesizer（13）Liquid outlet and tar and pyrolkigneous liquid collecting pit （18）It is connected, described spray synthesizer（14）Top gas outlet and absorption synthesizer（16）Air inlet is connected, and spray is comprehensive Clutch（14）Outlet at bottom and tar and pyrolkigneous liquid collecting pit（18）It is connected, described absorption synthesizer（16）Gas outlet and combustion Gas surge tank（17）Air inlet is connected, and adsorbs synthesizer（16）Outlet at bottom and tar and pyrolkigneous liquid collecting pit（18）It is connected Connect, pyrolysis oven（6）Discharge port and pyrolytic carbon feed bin（11）Import is connected.
- A kind of 2. comprehensive castoff regenerative energy multi-connection production. art system according to claim 1, it is characterised in that：Also wrap Gas storage system, the gas storage system and pyrolysis oven are included（6）In heat conducting pipe（21）Import is connected.
- A kind of 3. comprehensive castoff regenerative energy multi-connection production. art system according to claim 1, it is characterised in that：It is described Feed bin（1）With belted electronic balance（3）Between be provided with vibrating bunker（2）, described feed bin（1）Outlet is located at vibrating bunker （2）Top, described vibrating bunker（2）Outlet is located at belted electronic balance（3）Above import.
- A kind of 4. comprehensive castoff regenerative energy multi-connection production. art system according to claim 1, it is characterised in that：It is described Feeding warehouse（5）Import is provided with hopper（4）, described belted electronic balance（3）Outlet is located at hopper（4）Above import, Described hopper（4）Outlet and feeding warehouse（5）Import is connected.
- A kind of 5. comprehensive castoff regenerative energy multi-connection production. art system according to claim 1, it is characterised in that：It is described Combustion gas surge tank（17）Gas outlet and pyrolysis oven（6）In heat conducting pipe（21）Import is connected.
- A kind of 6. comprehensive castoff regenerative energy multi-connection production. art system according to claim 1, it is characterised in that：Also wrap Drive device is included（23）And PLC, described pyrolysis oven（6）It is internally provided with flight chain device（22）, pyrolysis oven （6）Both ends are respectively arranged with active transmission device（25）With slave drive device（26）, described flight chain device（22）Bag Include chain, be provided with multiple scraper plates on described chain, chain respectively with active transmission device（25）With slave drive device （26）It is connected, described active transmission device（25）With drive device（23）It is connected, described heat conducting pipe（5）On be provided with Temperature sensor, described temperature sensor are connected with PLC, described drive device（23）With PLC phase Connection.
- A kind of 7. comprehensive castoff regenerative energy multi-connection production. art system according to claim 1, it is characterised in that：It is described Pyrolysis oven（6）Internal heat conducting pipe（21）Top is disposed with heat-preservation cotton（24）.
- A kind of 8. comprehensive castoff regenerative energy multi-connection production. art system according to claim 1, it is characterised in that：It is described Pyrolysis oven（6）Discharge port and pyrolytic carbon feed bin（11）Cooling screw is provided between import（9）And rubber conveyer（10）, Described pyrolysis oven（6）Discharge port is located at cooling screw（9）Above import, described cooling screw（9）Outlet is located at glue Band conveyer（10）Above import, described rubber conveyer（10）Outlet is located at pyrolytic carbon feed bin（11）Above import.
- A kind of 9. comprehensive castoff regenerative energy multi-connection production. art system according to claim 8, it is characterised in that：It is described Cooling screw（9）Water cooling hopper is provided with above import（7）With star blanking machine（8）, described pyrolysis oven（6）Discharge port Positioned at water cooling hopper（7）Above import, described water cooling hopper（7）Outlet and star blanking machine（8）Import is connected, described Star blanking machine（8）Outlet and cooling screw（9）Import is connected.
- A kind of 10. comprehensive castoff regenerative energy multi-connection production. art system according to claim 8, it is characterised in that：Institute The pyrolytic carbon feed bin stated（11）Outlet is provided with vibrating bunker（2）.
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| CN201711078600.XA CN107828433A (en) | 2017-11-06 | 2017-11-06 | A kind of comprehensive castoff regenerative energy multi-connection production. art system |
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| CN201711078600.XA CN107828433A (en) | 2017-11-06 | 2017-11-06 | A kind of comprehensive castoff regenerative energy multi-connection production. art system |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113462414A (en) * | 2021-06-28 | 2021-10-01 | 黄春华 | Biomass raw material pyrolysis furnace |
| CN115446086A (en) * | 2022-07-27 | 2022-12-09 | 南京中船绿洲环保有限公司 | Low-temperature micro negative pressure pyrolysis test device |
Citations (9)
| 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 |
| US20110136971A1 (en) * | 2007-03-14 | 2011-06-09 | Tucker Richard D | Pyrolysis systems, methods, and resultants derived therefrom |
| CN102206497A (en) * | 2011-05-03 | 2011-10-05 | 武汉天颖环境工程有限公司 | Anaerobic pyrolysis purification process |
| US20130004409A1 (en) * | 2007-03-14 | 2013-01-03 | Tucker Engineering Associates, Inc. | Pyrolysis and gasification systems, methods, and resultants derived therefrom |
| CN104017590A (en) * | 2014-06-24 | 2014-09-03 | 华南农业大学 | Continuous pyrolysis carbonization method of agricultural and forestal biomasses |
| CN106635080A (en) * | 2016-12-30 | 2017-05-10 | 浙江天禄环境科技有限公司 | Process for preparing biochar through reduction gasification of sludge |
| 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 |
| CN207845563U (en) * | 2017-11-06 | 2018-09-11 | 湖北师范大学 | A kind of comprehensive castoff regenerative energy multi-connection production. art system |
-
2017
- 2017-11-06 CN CN201711078600.XA patent/CN107828433A/en active Pending
Patent Citations (9)
| 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 |
| US20110136971A1 (en) * | 2007-03-14 | 2011-06-09 | Tucker Richard D | Pyrolysis systems, methods, and resultants derived therefrom |
| US20130004409A1 (en) * | 2007-03-14 | 2013-01-03 | Tucker Engineering Associates, Inc. | Pyrolysis and gasification systems, methods, and resultants derived therefrom |
| CN102206497A (en) * | 2011-05-03 | 2011-10-05 | 武汉天颖环境工程有限公司 | Anaerobic pyrolysis purification process |
| CN104017590A (en) * | 2014-06-24 | 2014-09-03 | 华南农业大学 | Continuous pyrolysis carbonization method of agricultural and forestal biomasses |
| CN106635080A (en) * | 2016-12-30 | 2017-05-10 | 浙江天禄环境科技有限公司 | Process for preparing biochar through reduction gasification of sludge |
| 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 |
| CN207845563U (en) * | 2017-11-06 | 2018-09-11 | 湖北师范大学 | A kind of comprehensive castoff regenerative energy multi-connection production. art system |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113462414A (en) * | 2021-06-28 | 2021-10-01 | 黄春华 | Biomass raw material pyrolysis furnace |
| CN113462414B (en) * | 2021-06-28 | 2022-12-06 | 辽宁昌盛节能锅炉有限公司 | Biomass raw material pyrolysis furnace |
| CN115446086A (en) * | 2022-07-27 | 2022-12-09 | 南京中船绿洲环保有限公司 | Low-temperature micro negative pressure pyrolysis test device |
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