CN108569696A - A kind of stalk prepares the continuous carbonization furnace of activated carbon - Google Patents

A kind of stalk prepares the continuous carbonization furnace of activated carbon Download PDF

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Publication number
CN108569696A
CN108569696A CN201710660088.3A CN201710660088A CN108569696A CN 108569696 A CN108569696 A CN 108569696A CN 201710660088 A CN201710660088 A CN 201710660088A CN 108569696 A CN108569696 A CN 108569696A
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furnace body
stalk
wheel
body wheel
straw
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CN201710660088.3A
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CN108569696B (en
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徐建玲
王汉席
刘学军
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Northeastern University China
Northeast Normal University
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Northeast Normal University
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    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/10Process efficiency

Abstract

The invention discloses the continuous carbonization furnaces that a kind of stalk prepares activated carbon, it is made of heating system and cycle furnace body two parts, heating system is made of fuel tank (1) and fuel (2) two parts, and cycle furnace body is made up of 4 furnace body wheels (3) the connection of connecting rod (5), main shaft (4) and wheel shaft (6);In the process of running, fuel (2) burning directly heats furnace body wheel (3), the rotating furnace body wheel (3) in heating;After the completion of a furnace body wheel (3) is heated, live spindle (4), heat next furnace body wheel (3), when heating third furnace body wheel (3), open the outer cover of first furnace body wheel (3), the stalk matrix activated carbon that charing is completed is taken out, new stalk is packed into, is so recycled.This method overcomes prior art heat to transmit the shortcomings of slow, heat utilization efficiency is low, low production efficiency, complex process, high operating cost, realizes the preparation of continuous, efficient activated carbon.

Description

A kind of stalk prepares the continuous carbonization furnace of activated carbon
Technical field
The present invention relates to the manufacture of the environment-friendly materials Preparation equipment of environment-friendly engineering and energy recovery technical field more particularly to one Kind stalk prepares the exploitation of the continuously carbonizing furnace apparatus of activated carbon.
Background technology
Chinese Plants stalk resource is abundant, generates a large amount of maize straws, rice straw and wheat stalk every year.Stalk at present It is mainly used for power generation, direct returning to farmland, ferment preparation of sludge gas, rural area peasant household fuel etc., utility value is very low.The especially annual summer Season and autumn, after crop harvesting, stalk fails to obtain timely processing, is piled up arbitrarily or field combustion, environmental pollution are serious. Although various regions government increases management intensity, fail to tackle the problem at its root always.To improve the utility value of stalk, from Fundamentally prevent pollution of the straw burning to environment, it is an effective way that exploitation straw under high temperature charing, which prepares activated carbon technology, Diameter.
The method that current stalk prepares activated carbon is more, but high temperature carbonization process is indispensable processing ring Section, conventional heating furnace fail to realize continuous dosing and continuous production charcoal, and low production efficiency, energy consumption is high, prepares the cost of activated carbon It is high.Therefore, exploitation continuous high-temperature furnace prepares straw base activated carbon technology and is of great significance.The high temperature of activated carbon is prepared at present Stove, main mandate or disclosed patent include:A kind of automatic segmentation control dress of activated carbon fiber material preparation high-temperature furnace body Set (the number of applying for a patent:201120534751.3), a kind of agricultural crop straw continuous carbonization furnace (number of applying for a patent: 201210329884.6), a kind of self-heating stalk coke oven (number of applying for a patent:201110375321.6), stalk coke oven (Shen It please the patent No.:201110262857.7), a kind of regenerated carbon heating furnace (number of applying for a patent:201620156105.0), one Kind stalk coke oven and its method for making charcoal (number of applying for a patent:200810017034.6), a kind of combined bio matter particle charcoal Change stove and its carbonizing method (number of applying for a patent:201110073104.1), a kind of self sealss biomass carbonizing furnace feeding equipment (Shen It please the patent No.:201510912707.4), a kind of swinging continuous pyrolysis stalk coke oven (number of applying for a patent: 201510504032.X), moveable stalk carbonizes returning to the field retort nearby and its carbonizing method (number of applying for a patent nearby: 201310339328.1), the stalk coke oven (number of applying for a patent:201310453207.X), multifunctional stalk coke oven (application The patent No.:200710116239.5), a kind of split type retort group (number of applying for a patent:201610078639.0), one kind is equipped with Self-ignition type pollution-free straw carbonization furnace (the number of applying for a patent of timing means:201610809823.8), stalk continuous low-temperature heat Solve the retort (number of applying for a patent:201220676856.7), a kind of agricultural crop straw continuous carbonization furnace (number of applying for a patent: 201220453391.9), a kind of continuous high-temp carbide furnace (number of applying for a patent:201220132751.5), the stalk in drying storehouse Continuous carbonization furnace (the number of applying for a patent:201020530770.4) the high-efficiency energy-saving horizontal rotation activating oven (number of applying for a patent: 201110462387.9), the high-efficiency energy-saving horizontal rotation activating oven (number of applying for a patent:201110462387.9), activated carbon activation Stove and the method for prodn. of activated carbon (number of applying for a patent:201610897961.6), a kind of multilayer link plate type of producing activated carbon by chemical method Activation furnace (the number of applying for a patent:201610880799.7), the activation furnace (number of applying for a patent of fast activating a kind of: 201410248595.2), low energy consumption, high efficiency, the serialization activated charcoal fiber production furnace (number of applying for a patent: 200920047532.5), the energy-saving apparatus of active carbon activation furnace (number of applying for a patent:200810079602.5) etc., the above The energy consumption of patent high-temperature furnace device is high, and the time for preparing activated carbon is long, efficiency is low.In addition these patent equipments prepare activated carbon and have One or more disadvantages such as complex process, operation and maintenance are difficult, operational efficiency is low, production charcoal period length, operating cost height.Therefore, Exploitation is a kind of simple for process, carbonization time is short, low power consuming, utilization rate of waste heat are high, can continuous dosing, successively carbonize, make With with novel and multifunctional high-temperature furnace device easy to maintenance, the progress for preparing activated carbon technology to propulsion stalk has important reality Meaning.
Invention content
The object of the present invention is to provide the continuously carbonizing furnace apparatus that a kind of stalk prepares activated carbon, can not only effectively carry High straw utilization rate, while pollution of the stalk to environment is reduced, which directly heats mode, heating furnace cycle using wall-attaching type Continuous utilization, stalk UTILIZATION OF VESIDUAL HEAT IN, the device operation and maintenance is convenient, and manufacturing cost is low, and the activated carbon charcoal yield of preparation is high, energy Source utilization rate is high, has high application value.
The technical solution adopted by the present invention is as follows:
A kind of stalk prepares the continuous carbonization furnace of activated carbon, it is characterised in that:The device is by heating system and cycle furnace body Two parts form, and heating system is made of fuel tank and fuel two parts, and cycle furnace body passes through connecting rod, main shaft by 4 furnace body wheels With wheel axis connection composition;In the process of running, fuel combustion directly heats furnace body wheel, the rotating furnace body wheel in heating;First After the completion of a furnace body wheel heating, live spindle heats next furnace body wheel, when heating third furnace body wheel, opens first The outer cover of furnace body wheel takes out the stalk matrix activated carbon that charing is completed, is packed into new stalk, so recycles, continuously prepare straw base Activated carbon.
The furnace body wheel is made of heating shell, stalk and positioning plate, heating shell be steel, thickness be 10~ The outer diameter of 20mm, furnace body wheel are 0.8~1.6m;The thickness of stalk is 100~300mm, and stalk is maize straw, Wheat Straw or rice Careless stalk is detached using the skin and the stalks of rice, wheat, etc. of stalk when maize straw, and the straw skin of separation can be directly added into furnace body wheel, the straw of separation The stalk stalks of rice, wheat, etc. is added after need to being rolled using gravity, and laying depth is 300~500mm when rolling, and it is 150~300kPa to roll intensity, is adopted When with Wheat Straw or rice straw, it is directly added into;It is 5~8mm, positioning plate pair that positioning plate, which uses steel mesh, mesh diameter or the length of side, The pressure of stalk is 5.5~10.6kPa.
The furnace body wheel drives wheel shaft rotation, each furnace body wheel from 2.2~3.6 circle per minute is switched to by auxiliary shaft Heating time be 16~22min, after the completion of the heating of each furnace body wheel, main shaft revolves round the sun 45 degree, and main shaft passes through spindle rod and drives rotation Turn.
The entire furnace body uses furnace body shell seal, and horizontal discharge port is arranged in the furnace body wheel position positioned at top, For the discharging of finished activated charcoal and the charging of new stalk.
Heating temperature is 300~350 DEG C when being packed into straw and Wheat Straw in the furnace body wheel, when being packed into maize straw Heating temperature is 380~420 DEG C.
Gas outlet is arranged in the top of the furnace body shell, and gas outlet is unidirectional gas discharge outlet, and oxygen passes through feed inlet Supply.
Exhaust outlet is arranged in one end of the furnace body wheel, and the tar gas of generation is pipelined to feed inlet and enters combustion It burns.
Advantageous effect:Apparatus of the present invention heat conduction velocity is fast, can effectively utilize the energy of stalk itself, realize continuous Charing reduces activated carbon manufacturing cost;The present apparatus, which can be realized, continuously prepares activated carbon, and treating capacity is big, and apparatus of the present invention are simple, Easy to use, energy consumption is low;Stalk matrix activated carbon charcoal yield prepared by the present apparatus is high, strong adsorption;Apparatus of the present invention are simple, manufacture At low cost, easy to maintain, service life is long, and operability is strong, and application value is high.
Description of the drawings
Fig. 1 is the heating furnace cross-section diagram of the present invention.
Fig. 2 is the heating furnace sectional view of the present invention.
In figure, 1, fuel tank, 2, fuel, 3, furnace body wheel, 4, main shaft, 5, connecting rod, 6, wheel shaft, 7, heating shell, 8, stalk, 9, positioning plate, 10, furnace body shell, 11, auxiliary shaft, 12, feed inlet, 13, gas outlet, 14, spindle rod.
Specific implementation mode
For the present invention using recyclable materials stalk as research object, exploitation stalk prepares activated carbon new equipment;Apparatus of the present invention Direct heat transfer, the preparation efficiency for continuously carbonizing, making full use of stalk itself thermal energy, improving activated carbon, the present invention can realize straw The maximum resourceization of stalk utilizes, and improves the utilization rate of the energy, solves current stalk processing problem.
Below in conjunction with example, the present invention is further described, and specific implementation step is as follows:
Example 1:It is prepared by rice straw matrix activated carbon
The high temperature furnace structure of preparation is as depicted in figs. 1 and 2, which is made of heating system and cycle furnace body two parts, Heating system is made of fuel tank 1 and 2 two parts of fuel, and cycle furnace body passes through connecting rod 5, main shaft 4 and wheel shaft 6 by 4 furnace body wheels 3 Connection composition;In the process of running, the burning of fuel 2 directly heats furnace body wheel 3, the rotating furnace body wheel 3 in heating;In first stove After the completion of body wheel 3 heats, live spindle 4 heats next furnace body wheel 3, when heating third furnace body wheel 3, opens first The outer cover of furnace body wheel 3 takes out the rice straw matrix activated carbon that charing is completed, is packed into new rice straw, so recycles, continuous to make Standby rice straw matrix activated carbon.
Furnace body wheel 3 is made of heating shell 7, stalk 8 and positioning plate 9, and heating shell is steel, thickness 20mm, furnace body The outer diameter of wheel 3 is 1.6m;The thickness of rice straw is 300mm, and rice straw is directly added into;Positioning plate 9 uses steel mesh, mesh straight Diameter or the length of side are 5mm, and positioning plate 9 is 5.5kPa to the pressure of stalk.
Furnace body wheel 3 drives wheel shaft 6 to rotate, the heating of each furnace body wheel 3 from 3.6 circle per minute is switched to by auxiliary shaft 11 Time is 16min, and after the completion of each furnace body wheel 3 heats, main shaft 4 revolves round the sun 45 degree, and main shaft 4 is driven by spindle rod 14 to be rotated.
Entire furnace body is closed using furnace body shell 10, and horizontal discharge port is arranged in 3 position of furnace body wheel positioned at top, is used for The discharging of finished activated charcoal and the charging of stalk, furnace body wheel 3 is interior to be packed into straw, and heating temperature is 300~350 DEG C.
Gas outlet 13 is arranged in the top of furnace body shell 10, and gas outlet 13 is unidirectional gas discharge outlet, and oxygen passes through feed inlet 12 supplies.
Exhaust outlet is arranged in one end of furnace body wheel 3, and the tar gas of generation is pipelined to feed inlet 12 and enters burning.
The rice straw matrix activated carbon prepared as stated above is mixed for the city life of processing with other matrix after processing Sewage living, effect are preferable.
Example 2:It is prepared by maize straw matrix activated carbon
Charing furnace apparatus is made of heating system and cycle furnace body two parts as depicted in figs. 1 and 2, and heating system is by fuel Pond 1 and 2 two parts of fuel composition, cycle furnace body are made up of 4 furnace body wheels 3 connection of connecting rod 5, main shaft 4 and wheel shaft 6;It is transporting During row, the burning of fuel 2 directly heats furnace body wheel 3, the rotating furnace body wheel 3 in heating;It is completed in first heating of furnace body wheel 3 Afterwards, next furnace body wheel 3 is heated in live spindle 4, when heating third furnace body wheel 3, opens the outer cover of first furnace body wheel 3, The stalk matrix activated carbon that charing is completed is taken out, new stalk is packed into, so recycles, continuously prepares stalk matrix activated carbon.
Furnace body wheel 3 is made of heating shell 7, stalk 8 and positioning plate 9, and heating shell is steel, thickness 10mm, furnace body The outer diameter of wheel 3 is 0.8m;The thickness of stalk is 100mm, using maize straw, the skin of stalk and stalks of rice, wheat, etc. separation before being added, separation Straw skin is directly added into furnace body wheel 3, and the stalk stalks of rice, wheat, etc. of separation is added after being rolled using gravity, and laying depth is 300mm when rolling, It is 150kPa to roll intensity;Positioning plate 9 uses steel mesh, and mesh diameter or the length of side are 8mm, and positioning plate 9 is to the pressure of stalk 10.6kPa。
Furnace body wheel 3 drives wheel shaft 6 to rotate, the heating of each furnace body wheel 3 from 2.2 circle per minute is switched to by auxiliary shaft 11 Time is 22min, and after the completion of each furnace body wheel 3 heats, main shaft 4 revolves round the sun 45 degree.
Entire furnace body is closed using furnace body shell 10, discharge port is arranged in the furnace body wheel 3 positioned at top, for finished activated The discharging of charcoal and the charging of stalk, are packed into maize straw, and heating temperature is 380~420 DEG C.
Gas outlet 13 is arranged in the top of furnace body shell 10, and gas outlet 13 is unidirectional gas discharge outlet, and oxygen passes through feed inlet 12 supplies.
Exhaust outlet is arranged in one end of furnace body wheel 3, and the tar gas of generation is pipelined to feed inlet 12 and enters burning Pond.
The maize straw matrix activated carbon prepared as stated above is used for household water filter filter element filtering after processing Material, good filtration effect.
The above embodiments are merely illustrative of the technical solutions of the present invention, rather than its limitations;Essence of the invention is not being departed from Spirit and principle within made by all any modification, equivalent and improvement etc., should be included in protection scope of the present invention it It is interior.

Claims (7)

1. a kind of stalk prepares the continuous carbonization furnace of activated carbon, it is characterised in that:The device is by heating system and cycle furnace body two Part forms, and heating system is made of fuel tank (1) and fuel (2) two parts, and cycle furnace body passes through company by 4 furnace body wheels (3) Bar (5), main shaft (4) and wheel shaft (6) connection composition;In the process of running, fuel (2) burning directly heats furnace body wheel (3), Bian Jia Hot side rotating furnace body wheel (3);After the completion of first furnace body wheel (3) is heated, live spindle (4) heats next furnace body wheel (3), when heating third furnace body wheel (3), the outer cover of first furnace body wheel (3) is opened, the straw base that charing is completed is taken out and lives Property charcoal, be packed into new stalk, so recycle, continuously prepare stalk matrix activated carbon.
2. furnace body wheel (3) as described in claim 1 is made of heating shell (7), stalk (8) and positioning plate (9), shell is heated For steel, thickness is 10~20mm, and the outer diameter of furnace body wheel (3) is 0.8~1.6m;The thickness of stalk is 100~300mm, stalk For maize straw, Wheat Straw or rice straw, detached using the skin and the stalks of rice, wheat, etc. of stalk when maize straw, the straw skin of separation can be direct It being added in furnace body wheel (3), the stalk stalks of rice, wheat, etc. of separation is added after need to being rolled using gravity, and laying depth is 300~500mm when rolling, It is that 150~300kPa is directly added into when using Wheat Straw or rice straw to roll intensity;Positioning plate (9) uses steel mesh, mesh Diameter or the length of side are 5~8mm, and positioning plate (9) is 5.5~10.6kPa to the pressure of stalk.
3. the furnace body wheel (3) as described in claim 1 and claim 2 switchs to 2.2~3.6 circle per minute certainly, pass through auxiliary shaft (11) wheel shaft (6) is driven to rotate, the heating time of each furnace body wheel (3) is 16~22min, and each furnace body wheel (3) heating is completed Afterwards, main shaft (4) revolves round the sun 45 degree, and main shaft (4) is driven by spindle rod (14) to be rotated.
4. entire furnace body as described in claim 1 is closed using furnace body shell (10), in furnace body wheel (3) position positioned at top Horizontal discharge port is set, for the discharging of finished activated charcoal and the charging of new stalk.
5. heating temperature is 300~350 DEG C when being packed into straw and Wheat Straw in furnace body wheel (3) as claimed in claim 3, it is packed into Heating temperature when maize straw is 380~420 DEG C.
6. top setting gas outlet (13) of furnace body shell (10) as claimed in claim 4, gas outlet (13) are unidirectional gas Floss hole, oxygen are fed by feed inlet (12).
7. exhaust outlet is arranged in one end of the furnace body wheel (3) as described in claim 1 and claim 5, the tar gas of generation is logical Piping is transported to feed inlet (12) and enters burning.
CN201710660088.3A 2017-08-04 2017-08-04 Continuous carbonization furnace for preparing activated carbon from straws Active CN108569696B (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109897647A (en) * 2019-04-02 2019-06-18 浙江科技学院 A kind of energy-saving biological charcoal prepares stove
CN113461009A (en) * 2021-08-05 2021-10-01 江苏森森炭业科技有限公司 High-efficient carbomorphism device of bio-based preparation active carbon

Citations (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003201482A (en) * 2001-12-28 2003-07-18 Mitsuwa:Kk Chaff-carbonizing device
JP2003226513A (en) * 2002-02-05 2003-08-12 Japan Science & Technology Corp Continuous carbonization system
CN101134899A (en) * 2006-08-28 2008-03-05 李延韬 Biomass energy converter
EP1903292A2 (en) * 2006-09-19 2008-03-26 Blücher GmbH Rotary furnace for manufacturing active carbon using modified rotary pipe geometry
WO2009089356A1 (en) * 2008-01-08 2009-07-16 Carbonxt Group Limited System and method for making low volatile carbonaceous matter with supercritical co2
CN101644448A (en) * 2008-08-10 2010-02-10 沈桀 Intelligent straw gasification furnace
CN101693842A (en) * 2009-10-15 2010-04-14 武汉凯迪科技发展研究院有限公司 Gas lock transportation technology and device thereof for biomass high-pressure retort charcoal product
CN201567236U (en) * 2009-11-25 2010-09-01 商丘三利新能源有限公司 Continuous type charring device
CN103521304A (en) * 2013-09-29 2014-01-22 都江堰申都中药有限公司 Continuous discharge traditional Chinese medicine grinder
US20160039118A1 (en) * 2013-03-28 2016-02-11 Elg Carbon Fibre International Gmbh Pyrolysis system and method of recovering carbon fibres from carbon-fibre-containing plastics
WO2017011669A1 (en) * 2015-07-14 2017-01-19 Enginuity Worldwide, LLC Process for producing bio-products from biomass using rotary compression unit
CN206104032U (en) * 2016-10-09 2017-04-19 天津国安盟固利新材料科技股份有限公司 Novel grinding of lithium ion batteries cathode materials double sintering device
CN206257914U (en) * 2016-12-13 2017-06-16 湛江市茗禾茶业有限公司 A kind of automatic discharge apparatus of tealeaves

Patent Citations (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003201482A (en) * 2001-12-28 2003-07-18 Mitsuwa:Kk Chaff-carbonizing device
JP2003226513A (en) * 2002-02-05 2003-08-12 Japan Science & Technology Corp Continuous carbonization system
CN101134899A (en) * 2006-08-28 2008-03-05 李延韬 Biomass energy converter
EP1903292A2 (en) * 2006-09-19 2008-03-26 Blücher GmbH Rotary furnace for manufacturing active carbon using modified rotary pipe geometry
WO2009089356A1 (en) * 2008-01-08 2009-07-16 Carbonxt Group Limited System and method for making low volatile carbonaceous matter with supercritical co2
CN101644448A (en) * 2008-08-10 2010-02-10 沈桀 Intelligent straw gasification furnace
CN101693842A (en) * 2009-10-15 2010-04-14 武汉凯迪科技发展研究院有限公司 Gas lock transportation technology and device thereof for biomass high-pressure retort charcoal product
CN201567236U (en) * 2009-11-25 2010-09-01 商丘三利新能源有限公司 Continuous type charring device
US20160039118A1 (en) * 2013-03-28 2016-02-11 Elg Carbon Fibre International Gmbh Pyrolysis system and method of recovering carbon fibres from carbon-fibre-containing plastics
CN103521304A (en) * 2013-09-29 2014-01-22 都江堰申都中药有限公司 Continuous discharge traditional Chinese medicine grinder
WO2017011669A1 (en) * 2015-07-14 2017-01-19 Enginuity Worldwide, LLC Process for producing bio-products from biomass using rotary compression unit
CN206104032U (en) * 2016-10-09 2017-04-19 天津国安盟固利新材料科技股份有限公司 Novel grinding of lithium ion batteries cathode materials double sintering device
CN206257914U (en) * 2016-12-13 2017-06-16 湛江市茗禾茶业有限公司 A kind of automatic discharge apparatus of tealeaves

Non-Patent Citations (4)

* Cited by examiner, † Cited by third party
Title
DESOGUS, F, ET AL: "Experimental study on the axial mass transport of minced biomass(rape straw) into a pyrolysis rotating reactor working in the slipping regime", 《CHEMICAL ENGINEERING SCIENCE》 *
R.L卡尔等,: "《活性炭水处理技术》", 30 September 1983, 黑龙江科学技术出版社 *
何健等: "连续化秸秆炭化炉的设计", 《农业科技与装备》 *
王宁等: "蓄热式辐射管旋转床在垃圾热解项目中的应用", 《工业炉》 *

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109897647A (en) * 2019-04-02 2019-06-18 浙江科技学院 A kind of energy-saving biological charcoal prepares stove
CN113461009A (en) * 2021-08-05 2021-10-01 江苏森森炭业科技有限公司 High-efficient carbomorphism device of bio-based preparation active carbon

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