CN103484138B - Manufacturing process and equipment of bamboo charcoal - Google Patents

Manufacturing process and equipment of bamboo charcoal Download PDF

Info

Publication number
CN103484138B
CN103484138B CN201310438495.1A CN201310438495A CN103484138B CN 103484138 B CN103484138 B CN 103484138B CN 201310438495 A CN201310438495 A CN 201310438495A CN 103484138 B CN103484138 B CN 103484138B
Authority
CN
China
Prior art keywords
drying
combustor
bamboo
bamboo charcoal
gas
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.)
Active
Application number
CN201310438495.1A
Other languages
Chinese (zh)
Other versions
CN103484138A (en
Inventor
康德朗
吉健斌
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shang Ding Environmental Technology (Jiangsu) Co., Ltd.
Original Assignee
Is Dinglu Industry Science And Technology (yangzhou) Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Is Dinglu Industry Science And Technology (yangzhou) Co Ltd filed Critical Is Dinglu Industry Science And Technology (yangzhou) Co Ltd
Priority to CN201310438495.1A priority Critical patent/CN103484138B/en
Publication of CN103484138A publication Critical patent/CN103484138A/en
Application granted granted Critical
Publication of CN103484138B publication Critical patent/CN103484138B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • 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
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/10Biofuels, e.g. bio-diesel
    • 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
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel

Abstract

The invention provides a manufacturing process and manufacturing equipment of bamboo charcoal. The manufacturing process comprises the following steps: cutting into sections: cutting bamboo into sections; drying: feeding the cut bamboo into a drying machine, drying, conveying tail gas generated in the drying process to a postcombustion chamber, and feeding high-temperature flue gas to the drying machine by the postcombustion chamber for drying the bamboo which is fed newly; performing dry distillation: placing the bamboo which is dried by a rotary kiln and the drying machine into a multi-section furnace, performing dry distillation, feeding combustible gas into the multi-section furnace to provide combustion-supporting gas for dry distillation, and feeding tail gas generated in the dry distillation process into a combustor or the postcombustion chamber to generate high-temperature flue gas; cooling: quickly feeding the bamboo subjected to dry distillation into an aqueous medium quenching tank and cooling; redrying: feeding the bamboo which is cooled by the aqueous medium quenching tank into the drying machine and drying to prepare the bamboo charcoal. The manufacturing process and the manufacturing equipment of the bamboo charcoal can continuously manufacture bamboo charcoal products, save energy and are favorable for environmental protection.

Description

Bamboo charcoal manufacturing process and its manufacturing equipment
Technical field
The present invention relates to a kind of bamboo charcoal manufacturing process and its manufacturing equipment, and in particular to one kind continuously manufactures senior bamboo charcoal and produces The manufacturing process and its manufacturing equipment of product.
Background technology
Bamboo charcoal is to adopt Phyllostachys pubescens Mazei ex H.de Lebaie for raw material, under the conditions of 400 DEG C of temperatures above completely cuts off carbonization product made by air dry distilling. With the difference of firing temperature, the quality of bamboo charcoal and purposes difference are very big, and on the whole, the final firing temperature of retort process is got over Height, the density of bamboo charcoal product, mechanical hardness, porosity and surface area are also bigger, when firing temperature is more than 1050 DEG C, can adopt The senior bamboo charcoal with far infrared, anion and conducting function is made with bamboo wood, " Linesless charcoal " is commonly called as, is then commonly referred to as in Japan " standby Long charcoal "(" Binchotan " has almost gone completely into the synonym of senior bamboo charcoal product at present).
Traditional bamboo charcoal is produced using earth kiln device, and bamboo matter Binchotan then needs to fill using the earth kiln of particular design Put, special charcoal kiln will be loaded after the Phyllostachys pubescens Mazei ex H.de Lebaie cutting newly cut, through carbonization, high temperature refinery, red charcoal kiln discharge, then lid is flooded with dry sandy soil Method is stopped working, the senior Binchotan product needed for being eventually fabricated.Wherein high temperature refinery process procedure is to need most control technology and behaviour Make the period of experience.
Take the existing long history of earth kiln device bamboo charcoal, but the production technology method has intrinsic, Wu Fatong The defect crossed local improving and get rid of:
(1)Production process is seriously polluted, and flammable vapor product cannot realize effectively utilizes.Carbonization and refining process, Substantial amounts of ash-laden gas can be discharged in carbonization process especially, although the bamboo vinegar in flue gas and wood tar can be big by condensation Part removes, but incoagulability vapor phase contaminants(Hydrocarbon containing small molecule, carbon monoxide, methane and hydrogen etc. it is flammable into Point)Then effectively cannot eliminate, also cannot effectively reuse(Reason is the rate of release extremely unstable of these gaseous products, it is impossible to Carry out effectively storing and conveying).
(2)Production efficiency is extremely low.Earth kiln technique can only take interval, by batch production mode manufacturing bamboo charcoal product, Often complete stove bamboo charcoal firing and need to take 15 to 30 days, maximum earth kiln is also only capable of producing 30 tons or so of bamboo charcoal every time, puts down Production efficiency is only 1~2 ton day.
(3)Unstable product quality.The bamboo charcoal of traditional earth kiln method production, its quality are completely controlled by furnace operation personnel's Technical experience, impact of the anthropic factor to product quality are very big.
The content of the invention
The present invention is made improvements for the problem that above-mentioned prior art is present, i.e., the technical problem to be solved in the present invention is to carry For a kind of bamboo charcoal manufacturing process and its manufacturing equipment, this bamboo charcoal manufacturing process and its manufacturing equipment can continuously manufacture bamboo charcoal product Product, energy saving are conducive to environmental conservation.
In order to solve above-mentioned technical problem, the invention provides following technical scheme:
A kind of bamboo charcoal manufacturing process,
Comprise the steps:
S1. cutting, by bamboo wood cutting;
S2. it is dried, the bamboo wood for cutting is sent into into drying machine and is dried, the tail gas produced in dry run is transported to afterburner, High-temperature flue gas are sent into drying machine by afterburner again to be used to be dried the new bamboo wood sent into;
S3. dry distilling, carries out dry distilling by being put in multi-stage oven through the dried bamboo wood of rotary kiln drying machine, by fuel gas Sending into multi-stage oven and combustion-supporting gas being provided for dry distilling, the tail gas produced in retort process sends into combustor or afterburner to produce height Warm flue gas;
S4. cool down, cool down being rapidly feeding in aqueous medium chilling groove through the bamboo wood of dry distilling;
S5. cooled bamboo wood in aqueous medium chilling groove is sent into drying machine and is dried, and bamboo is obtained by after drying Charcoal.
A kind of bamboo charcoal manufacturing equipment for realizing above-mentioned bamboo charcoal manufacturing process, including control device and respectively with the control Drying device, multi-stage oven, chilling groove, combustor, aeration tower and water-storing device that device is electrically connected;The drying device includes One drying device and the second drying device;The multi-stage oven includes burning zone, cooling section, combustor, air inlet, charging aperture and goes out Material mouth, each section of the burning zone are all connected with combustor, and the charging aperture is connected with first drying device, it is described go out Material mouth is connected with the chilling groove;The combustor is connected with the drying device, multi-stage oven, aeration tower respectively;It is described Second drying device is connected with the chilling groove;The water-storing device is connected with the chilling groove, aeration tower respectively.
The combustor includes the first combustor and the second combustor, first combustor and the multi-stage oven, first Drying device, the second drying device are connected;Second combustor is connected with first drying device, aeration tower.
The water-storing device includes cesspool and depositing reservoir, is provided with water purification cartridge between the cesspool and the depositing reservoir Put.
First drying device is to be dried converter.
Second drying device is mesh dryer.
It is an advantage of the current invention that being capable of achieving " cleanly production " of bamboo charcoal product, the gas phase pollution produced in production process Thing is introduced directly into emission control systems(It is made up of afterburner I, afterburner II, aeration tower, air-introduced machine etc.)It is able to ensure that whole life Producing line realizes cleanly production target;After pre- char zone and fining cell the are discharged, tail gas containing combustible gas component is introduced I thorough burning disposal of combustor, the dried of the high-temperature flue gas of generation drying and water-containing products as raw material bamboo wood; The high heating value process tail gas that char zone produces are directly used as into the heat source gas of fining cell, and assemble supersonic combustion machine, make height Calorific value process tail gas are able to fully burn and be prevented effectively from burning machine nozzle generation " carbon distribution " phenomenon so that the thermal efficiency and the energy are comprehensive Close utilization rate to be significantly improved;
Traditional earth kiln production technology could obtain about 15% as the bamboo wood that must consume q.s does thermal source(Account for raw material The ratio of butt quality of bamboo timber)Senior bamboo charcoal product, the process of the present invention is by making full use of returning for each production process Heat energy is received, the pyrogenicity consumption of bamboo material is greatly reduced(Parts of bamboo raw material is used as into the thermal source of production process, to tie up The operation temperature for holding earth kiln is required), the yield of senior bamboo charcoal product can be greatly improved to 40%(Account for raw material butt quality of bamboo timber Ratio);
The present invention makes full use of each layer burner hearth process operation temperatures of multistage furnace apparatus to be accurately controlled, the intensification of solid material Speed such as can preferably regulate and control at the Inherent advantage, according to the heat absorption of bamboo wood pyrolysis, heat release, three key steps of absorbing heat again, by tailored version Multistage furnace apparatus are divided into three different functional areas, pre- carbonization respectively as bamboo wood, carbonization and fining cell, and continuously produce Senior bamboo charcoal product(Binchotan), maintain bamboo charcoal to produce with traditional, to fully rely on firing skilled industrial worker practical operation experience The empirical approach of quality performance is compared, and the present invention can make the quality stability of product be able to significantly improve and maintain.
Description of the drawings
Accompanying drawing is used for providing a further understanding of the present invention, and constitutes a part for description, the reality with the present invention Applying example is used for explaining the present invention together, is not construed as limiting the invention.In the accompanying drawings:
Fig. 1 is a kind of flow chart of bamboo charcoal manufacturing process of the invention;
Fig. 2 is a kind of bamboo charcoal manufacturing equipment structural representation of the invention;
Fig. 3 is multi-stage oven structural representation in Fig. 2.
Specific embodiment
As Figure 1-3, the present invention discloses a kind of bamboo charcoal manufacturing process, comprises the steps:
S1. cutting, by bamboo wood cutting;
S2. it is dried, the bamboo wood for cutting is sent into into drying machine and is dried, the tail gas produced in dry run is transported to afterburner, High-temperature flue gas are sent into drying machine by afterburner again to be used to be dried the new bamboo wood sent into;
S3. dry distilling, carries out dry distilling by being put in multi-stage oven through the dried bamboo wood of rotary kiln drying machine, by fuel gas Sending into multi-stage oven and combustion-supporting gas being provided for dry distilling, the tail gas produced in retort process sends into combustor or afterburner to produce height Warm flue gas;
S4. cool down, cool down being rapidly feeding in aqueous medium chilling groove through the bamboo wood of dry distilling;
S5. cooled bamboo wood in aqueous medium chilling groove is sent into drying machine and is dried, and bamboo is obtained by after drying Charcoal.
Retort process includes pre- carbonization, carbonization, refine.The operation temperature of pre- carbonization is 150 ° -280 °.The operation temperature of carbonization Spend for 350 ° -700 °.The operation temperature of refine is 800 ° -1100 °.
A kind of bamboo charcoal manufacturing equipment for realizing above-mentioned bamboo charcoal manufacturing process, including control device and respectively with control device The drying device of electrical connection, multi-stage oven, chilling groove, combustor, aeration tower and water-storing device;Drying device includes that the first drying is filled Put and the second drying device;Multi-stage oven includes burning zone, cooling section, combustor, air inlet, charging aperture and discharging opening, burning zone Each section be all connected with combustor, charging aperture is connected with the first drying device, and discharging opening is connected with chilling groove;Combustor point It is not connected with drying device, multi-stage oven, aeration tower;Second drying device is connected with chilling groove;Water-storing device respectively with urgency Cold trap, aeration tower are connected.
Combustor includes the first combustor and the second combustor, the first combustor and multi-stage oven, the first drying device, second Drying device is connected;Second combustor is connected with the first drying device, aeration tower.
Water-storing device includes cesspool and depositing reservoir, is provided with purifier between the cesspool and the depositing reservoir.
In the present embodiment, the first drying device is to be dried converter.Second drying device is mesh dryer.Carbonizing apparatus Using with diameter greater than 5 meters, siege sum up to 12 layers of multi-stage oven.
The burner hearth of multi-stage oven is divided into three functional areas, exercises pre- carbonization respectively(Also known as " pre-distillation " or " pre- to be pyrolyzed "), charcoal Change(Also known as " dry distilling " or " pyrolysis "), refine(Also known as " high-temperature retorting " or " high temperature pyrolysis "), refrigerating function.
Pre- char zone is made up of two-stage furnace thorax, and it is 150 to 280 DEG C that operation temperature is interval;
Char zone is made up of four sections of burner hearths, and it is 350 to 700 DEG C that operation temperature is interval;
Fining cell is made up of four sections of burner hearths, and it is 800 to 1100 DEG C that operation temperature is interval;
Two-stage furnace thorax is finally set as cooling section, makes refine bamboo charcoal product that less than 700 DEG C are naturally cooling in burner hearth.
The bamboo charcoal product drawn off from multi-stage oven is directly processed using the quenching of aqueous medium chilling groove, makes hard bamboo matter standby Long charcoal product.
Contain more pyroligneous acid composition in the tail gas that pre- carbonization process is produced, combustion heat value is relatively low;Fining cell is arranged The tail gas for going out contains more imflammable gas such as hydrogen, carbon monoxide and small molecule hydrocarbon components, combustion heat value It is relatively low.
The thorough burning disposal of the first combustor, the high-temperature flue gas of generation are introduced after pre- carbonization tail gas and refine tail gas are merged For raw material bamboo wood(Cutting is processed)Be dried converter thermal medium gas, produce in dry run containing it is wet, containing a small amount of flammable Composition(Predominantly carbon monoxide and small molecule Hydrocarbon and a small amount of pyroligneous acid etc.)Tail gas introduce the second combustor After individually burning, discharge Jing after aeration tower dust removal process;
It is also used as from chilling groove drawing off the drying medium gas of bamboo matter Binchotan product, using mesh-belt drier Finished product Binchotan is dried, generation is discharged Jing after aeration tower dust removal process containing wet tail gas.
The tail gas that carbonization process is generated contains a large amount of combustible components, such as hydrogen, carbon monoxide, small molecule hydro carbons(Methane, second Alkene, ethane, propane etc.), wood tar, pyroligneous acid(It is micro)Deng, calorific value up to more than 4500kcal/Nm3, design is directly used as essence The pyrogenicity gas of refining functional areas.To prevent the larger molecular organicses such as wood tar and pyroligneous acid from producing " carbon distribution " in combustion And blocking combustor fuel nozzle, the present invention has selected the special type combustor with ultrasonic atomization function as carbonization tail gas Special burner(Make the combustion gas containing organic oil mist and the mixture of combustion air form plasmoid, improve burning Efficiency), it is improved the efficiency of combustion and heat utilization rate of carbonization tail gas.
To sum up, the present invention make full use of each layer burner hearth process operation temperatures of multistage furnace apparatus to be accurately controlled, solid material Heating rate the Inherent advantage such as can preferably regulate and control, according to the heat absorption of bamboo wood pyrolysis, heat release, three key steps of absorbing heat again, will Tailored version multistage furnace apparatus are divided into three different functional areas, pre- carbonization respectively as bamboo wood, carbonization and fining cell, and continuously Produce senior bamboo charcoal product(Binchotan), maintain with traditional, to fully rely on firing skilled industrial worker practical operation experience The empirical approach of bamboo charcoal product quality performance is compared, and the present invention can make the quality stability of product be able to significantly improve and tie up Hold.
The preferred embodiments of the present invention are the foregoing is only, the present invention is not limited to, although with reference to aforementioned reality Apply example to be described in detail the present invention, for a person skilled in the art, which still can be to aforementioned each enforcement Technical scheme described in example is modified, or carries out equivalent to which part technical characteristic.All essences in the present invention Within god and principle, any modification, equivalent substitution and improvements made etc. should be included within the scope of the present invention.

Claims (3)

1. a kind of bamboo charcoal manufacturing equipment, it is characterised in that:Including control device
And drying device, multi-stage oven, chilling groove, combustor, aeration tower and the water-retention for electrically connecting with the control device respectively Device;
The drying device includes the first drying device and the second drying device;First drying device is rotary kiln drying Machine;
The multi-stage oven includes burning zone, cooling section, combustor, air inlet, charging aperture and discharging opening, the burning zone it is each Section is all connected with combustor, and the charging aperture is connected with first drying device, and the discharging opening is connected with the chilling groove It is logical;
Second drying device is connected with the chilling groove;
The water-storing device is connected with the chilling groove, aeration tower respectively;
The combustor includes the first combustor and the second combustor, and first combustor is dried with the multi-stage oven, first Device, the second drying device are connected;Second combustor is connected with first drying device, aeration tower;
Wherein, the burner hearth of multi-stage oven is divided into three different functional areas, the pre- carbonization, carbonization and fining cell respectively as bamboo wood; Combustion-supporting gas is provided for dry distilling by fuel gas feeding multi-stage oven;The high heating value process tail gas that char zone produces are directly used as into essence The heat source gas in refining area, and assemble supersonic combustion machine;The first combustor is introduced after pre- carbonization tail gas and refine tail gas are merged Thorough burning disposal, the high-temperature flue gas of generation be used for cutting process raw material bamboo wood drying and being dried of water-containing products at Reason;After the tail gas produced in raw material bamboo wood dry run introduces the independent burning of the second combustor, Jing aeration tower dust removal process heel row Put.
2. bamboo charcoal manufacturing equipment according to claim 1, it is characterised in that:The water-storing device includes cesspool and clarification Pond, is provided with purifier between the cesspool and the depositing reservoir.
3. bamboo charcoal manufacturing equipment according to claim 1, it is characterised in that:Second drying device is mesh belt dry Machine.
CN201310438495.1A 2013-09-24 2013-09-24 Manufacturing process and equipment of bamboo charcoal Active CN103484138B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201310438495.1A CN103484138B (en) 2013-09-24 2013-09-24 Manufacturing process and equipment of bamboo charcoal

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201310438495.1A CN103484138B (en) 2013-09-24 2013-09-24 Manufacturing process and equipment of bamboo charcoal

Publications (2)

Publication Number Publication Date
CN103484138A CN103484138A (en) 2014-01-01
CN103484138B true CN103484138B (en) 2017-04-12

Family

ID=49824749

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201310438495.1A Active CN103484138B (en) 2013-09-24 2013-09-24 Manufacturing process and equipment of bamboo charcoal

Country Status (1)

Country Link
CN (1) CN103484138B (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103851633A (en) * 2014-02-20 2014-06-11 煤炭科学研究总院 Tail gas purification and waste-heat utilization method for multi-hearth furnace
CN104312600A (en) * 2014-10-14 2015-01-28 北京北宇机械设备有限公司 Sludge pyrolysis and gasification treatment process and sludge pyrolysis and gasification treatment system
CN105713698B (en) * 2016-05-04 2019-04-05 广州市威士环保科技有限公司 A kind of method of afforestation Castoff material energizing
CN106287736A (en) * 2016-09-21 2017-01-04 尚鼎炉业科技(扬州)有限公司 A kind of solid waste processes technique and processing system
CN108910875A (en) * 2018-07-19 2018-11-30 紫云自治县紫香源农林科技有限责任公司 A kind of production method of bamboo bamboo charcoal

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002235088A (en) * 2001-02-09 2002-08-23 Akebono Toba Equipment and method for producing charcoal and bamboo charcoal
CN1458225A (en) * 2003-04-13 2003-11-26 胡福昌 Method for continuous dry distillation and carbonization for wood and bamboo
JP2006111770A (en) * 2004-10-15 2006-04-27 Suzuki Kogyosho:Kk Apparatus for producing bamboo charcoal or charcoal and method for producing the same
CN101885487A (en) * 2010-07-26 2010-11-17 东南大学 Device and method for continuously preparing active carbon by biomass in bulk
CN101921604A (en) * 2010-08-30 2010-12-22 浙江建中竹业科技有限公司 Dry distillation charring method for bamboos
CN102206498A (en) * 2011-05-03 2011-10-05 浙江省林业科学研究院 Method for firing high-density bamboo charcoal by using medium-small diameter bamboos
CN102643657A (en) * 2012-04-28 2012-08-22 郑州大学生化工程中心 Continuous biomass carbonization process
CN202530040U (en) * 2012-04-28 2012-11-14 郑州凯乐生物能有限公司 Continuous biomass dry-distillation carbonization apparatus

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002235088A (en) * 2001-02-09 2002-08-23 Akebono Toba Equipment and method for producing charcoal and bamboo charcoal
CN1458225A (en) * 2003-04-13 2003-11-26 胡福昌 Method for continuous dry distillation and carbonization for wood and bamboo
JP2006111770A (en) * 2004-10-15 2006-04-27 Suzuki Kogyosho:Kk Apparatus for producing bamboo charcoal or charcoal and method for producing the same
CN101885487A (en) * 2010-07-26 2010-11-17 东南大学 Device and method for continuously preparing active carbon by biomass in bulk
CN101921604A (en) * 2010-08-30 2010-12-22 浙江建中竹业科技有限公司 Dry distillation charring method for bamboos
CN102206498A (en) * 2011-05-03 2011-10-05 浙江省林业科学研究院 Method for firing high-density bamboo charcoal by using medium-small diameter bamboos
CN102643657A (en) * 2012-04-28 2012-08-22 郑州大学生化工程中心 Continuous biomass carbonization process
CN202530040U (en) * 2012-04-28 2012-11-14 郑州凯乐生物能有限公司 Continuous biomass dry-distillation carbonization apparatus

Also Published As

Publication number Publication date
CN103484138A (en) 2014-01-01

Similar Documents

Publication Publication Date Title
CN103484138B (en) Manufacturing process and equipment of bamboo charcoal
CN101514291B (en) Method for dry quenching by internal heat and low temperature carbonization of coal
CN1256405C (en) Method for continuous dry distillation and carbonization for wood and bamboo
CN104560072B (en) Thermal decomposition of organic wastes system and method for pyrolysis
CN101880540A (en) Low-coalification degree pulverized coal pyrolysis method and product prepared through the same
CN101955181B (en) Method for preparing active carbon by using carbon byproduct of fast pyrolysis of larchwood
CN103627415A (en) Biomass pyrolysis carbonization system equipment
CN104560071A (en) Pyrolysis system and pyrolyzing method
CN102250633A (en) Method for improving quality of brown coal with externally heated rotary furnace
CN105062521A (en) Rotary-type continuous pyrolyzing straw carbonizing furnace
CN104748125A (en) Pyrolysis volatile matter combustion system
CN102492443A (en) External-heating type integrated biomass pyrolysis equipment
CN102634358A (en) Efficient selectable pyrolysis system and using method thereof
CN102964884B (en) Hot cracking method process for preparing carbon black by using co-production of tail gas
CN105018121A (en) Gas, tar and activated carton co-production system
CN204897829U (en) Cogeneration system of coal gas, tar and active carbon
CN103936001A (en) Horizontal thermal regeneration furnace for waste powdered activated carbon
CN103435028B (en) Method and device for producing semi coke
CN102807216B (en) Method for preparing activated carbon with high specific surface area utilizing wood tar
CN202717749U (en) Biomass pyrogenic decomposition carbonization system device
CN203411452U (en) Sludge carbonization and carbon recovery device for oil refinery
CN204939394U (en) Rotary type continuous pyrolysis stalk coke oven
CN204529746U (en) A kind of cotton stalk dry distillation charring system
CN106520157A (en) Gasifying type dry-distilling pyrolysis charring method
CN201520746U (en) External-combustion internal-heating-type coal dry distillation furnace

Legal Events

Date Code Title Description
PB01 Publication
C06 Publication
SE01 Entry into force of request for substantive examination
C10 Entry into substantive examination
GR01 Patent grant
GR01 Patent grant
CP01 Change in the name or title of a patent holder

Address after: 225100 Yangzhou City, Jiangsu Province, Hanjiang Economic Development Zone Development West Road No. 217

Patentee after: Shang Ding Environmental Technology (Jiangsu) Co., Ltd.

Address before: 225100 Yangzhou City, Jiangsu Province, Hanjiang Economic Development Zone Development West Road No. 217

Patentee before: Is Dinglu industry science and Technology (Yangzhou) Co. Ltd.

CP01 Change in the name or title of a patent holder