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WO2011090260A2 - Dispositif pour la fabrication continue de charbon actif - Google Patents

Dispositif pour la fabrication continue de charbon actif Download PDF

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Publication number
WO2011090260A2
WO2011090260A2 PCT/KR2010/007667 KR2010007667W WO2011090260A2 WO 2011090260 A2 WO2011090260 A2 WO 2011090260A2 KR 2010007667 W KR2010007667 W KR 2010007667W WO 2011090260 A2 WO2011090260 A2 WO 2011090260A2
Authority
WO
WIPO (PCT)
Prior art keywords
activated carbon
kiln
combustion heat
raw material
carbide
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.)
Ceased
Application number
PCT/KR2010/007667
Other languages
English (en)
Korean (ko)
Other versions
WO2011090260A3 (fr
Inventor
김신철
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.)
Shinkwangchemindco Ltd
Original Assignee
Shinkwangchemindco 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 Shinkwangchemindco Ltd filed Critical Shinkwangchemindco Ltd
Priority to CN2010800619420A priority Critical patent/CN102844270A/zh
Publication of WO2011090260A2 publication Critical patent/WO2011090260A2/fr
Publication of WO2011090260A3 publication Critical patent/WO2011090260A3/fr
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27—FURNACES; KILNS; OVENS; RETORTS
    • F27B—FURNACES, KILNS, OVENS OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B9/00—Furnaces through which the charge is moved mechanically, e.g. of tunnel type; Similar furnaces in which the charge moves by gravity
    • F27B9/02—Furnaces through which the charge is moved mechanically, e.g. of tunnel type; Similar furnaces in which the charge moves by gravity of multiple-track type; of multiple-chamber type; Combinations of furnaces
    • F27B9/021—Furnaces through which the charge is moved mechanically, e.g. of tunnel type; Similar furnaces in which the charge moves by gravity of multiple-track type; of multiple-chamber type; Combinations of furnaces having two or more parallel tracks
    • F27B9/022—With two tracks moving in opposite directions
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B32/00—Carbon; Compounds thereof
    • C01B32/30—Active carbon
    • C01B32/312—Preparation
    • C01B32/336—Preparation characterised by gaseous activating agents
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B32/00—Carbon; Compounds thereof
    • C01B32/30—Active carbon
    • C01B32/39—Apparatus for the preparation thereof
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27—FURNACES; KILNS; OVENS; RETORTS
    • F27B—FURNACES, KILNS, OVENS OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B19/00—Combinations of different kinds of furnaces that are not all covered by any single one of main groups F27B1/00 - F27B17/00
    • F27B19/02—Combinations of different kinds of furnaces that are not all covered by any single one of main groups F27B1/00 - F27B17/00 combined in one structure
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27—FURNACES; KILNS; OVENS; RETORTS
    • F27B—FURNACES, KILNS, OVENS OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B9/00—Furnaces through which the charge is moved mechanically, e.g. of tunnel type; Similar furnaces in which the charge moves by gravity
    • F27B9/02—Furnaces through which the charge is moved mechanically, e.g. of tunnel type; Similar furnaces in which the charge moves by gravity of multiple-track type; of multiple-chamber type; Combinations of furnaces
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27—FURNACES; KILNS; OVENS; RETORTS
    • F27B—FURNACES, KILNS, OVENS OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B9/00—Furnaces through which the charge is moved mechanically, e.g. of tunnel type; Similar furnaces in which the charge moves by gravity
    • F27B9/02—Furnaces through which the charge is moved mechanically, e.g. of tunnel type; Similar furnaces in which the charge moves by gravity of multiple-track type; of multiple-chamber type; Combinations of furnaces
    • F27B9/021—Furnaces through which the charge is moved mechanically, e.g. of tunnel type; Similar furnaces in which the charge moves by gravity of multiple-track type; of multiple-chamber type; Combinations of furnaces having two or more parallel tracks
    • F27B9/022—With two tracks moving in opposite directions
    • F27B9/023—With two tracks moving in opposite directions with a U turn at one end
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27—FURNACES; KILNS; OVENS; RETORTS
    • F27B—FURNACES, KILNS, OVENS OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B9/00—Furnaces through which the charge is moved mechanically, e.g. of tunnel type; Similar furnaces in which the charge moves by gravity
    • F27B9/02—Furnaces through which the charge is moved mechanically, e.g. of tunnel type; Similar furnaces in which the charge moves by gravity of multiple-track type; of multiple-chamber type; Combinations of furnaces
    • F27B9/021—Furnaces through which the charge is moved mechanically, e.g. of tunnel type; Similar furnaces in which the charge moves by gravity of multiple-track type; of multiple-chamber type; Combinations of furnaces having two or more parallel tracks
    • F27B9/022—With two tracks moving in opposite directions
    • F27B9/023—With two tracks moving in opposite directions with a U turn at one end
    • F27B9/024—With two tracks moving in opposite directions with a U turn at one end with superimposed tracks
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27—FURNACES; KILNS; OVENS; RETORTS
    • F27B—FURNACES, KILNS, OVENS OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B9/00—Furnaces through which the charge is moved mechanically, e.g. of tunnel type; Similar furnaces in which the charge moves by gravity
    • F27B9/12—Furnaces through which the charge is moved mechanically, e.g. of tunnel type; Similar furnaces in which the charge moves by gravity with special arrangements for preheating or cooling the charge
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27—FURNACES; KILNS; OVENS; RETORTS
    • F27B—FURNACES, KILNS, OVENS OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B9/00—Furnaces through which the charge is moved mechanically, e.g. of tunnel type; Similar furnaces in which the charge moves by gravity
    • F27B9/30—Details, accessories or equipment specially adapted for furnaces of these types
    • F27B9/3005—Details, accessories or equipment specially adapted for furnaces of these types arrangements for circulating gases
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27—FURNACES; KILNS; OVENS; RETORTS
    • F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
    • F27D13/00—Apparatus for preheating charges; Arrangements for preheating charges
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27—FURNACES; KILNS; OVENS; RETORTS
    • F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
    • F27D17/00—Arrangements for using waste heat; Arrangements for using, or disposing of, waste gases
    • F27D17/10—Arrangements for using waste heat
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27—FURNACES; KILNS; OVENS; RETORTS
    • F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
    • F27D17/00—Arrangements for using waste heat; Arrangements for using, or disposing of, waste gases
    • F27D17/30—Arrangements for extraction or collection of waste gases; Hoods therefor
    • 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
    • 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
    • Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines

Definitions

  • the present invention relates to a continuous activated carbon production apparatus, and more particularly, a heat supply structure and a thermal circulation structure of a carbonization kiln and a gas activation kelon, which constitute a continuous kiln apparatus widely used as an activated carbon production apparatus.
  • the present invention relates to a continuous activated carbon production apparatus capable of producing high quality activated carbon by stabilizing the internal temperature of the continuous kiln apparatus in the shortest time with the least fuel gas.
  • the organic material which is the raw material of activated carbon
  • gas activation method which is the most commonly used gas
  • the organic material which is the raw material of activated carbon
  • the volatile tissues contained in the organic material are burned and the carbon crystals are formed into carbides.
  • Carbonization process to produce charcoal
  • the charcoal to which a gas catalyst such as steam gas (water vapor) is added may be classified into an activation process of reheating the carbonized carbon in the range of 800 to 1100 ° C. to generate fine porous adsorbed carbon.
  • Most of the activated carbon using the gas activation method as described above is a general kiln device having a known structure [combustion gas supply unit, raw material inlet, carbonization kiln, and activation kiln to generate activated carbon by gas activation by adding a gas catalyst. Furnace, consisting of a gas outlet, etc.].
  • activated carbon having good adsorption should have a larger surface area per unit area by forming more voids on the outer surface of the carbide without destroying the structure of the carbon crystals.
  • the interior of the first kiln furnace for carbonization and the second kiln furnace for gas activation, which constitute the kiln apparatus, must be maintained at a constant temperature. Sufficient preheating process will necessarily be required.
  • the length of the furnace is constant so that a large amount of activated carbon can be simultaneously heated due to the characteristics of the carbonization kiln furnace and the gas activation kiln furnace, in which the internal temperature must be maintained at a high temperature. It is generally composed of more than scale.
  • the inlet of the combustion gas capable of heating the internal temperature thereof is formed in only one of the bars.
  • the activated carbon is manufactured from rapidly heated carbide by supplying a large amount of fuel gas to the furnace without the preheating process.
  • the voids formed in the carbide produced in a state in which the internal temperature of the furnace was uneven were formed unstable, which caused a problem of degrading the quality of activated carbon.
  • the kiln for carbonization which constitutes the carbonization apparatus which extracts carbide which becomes a raw material of activated carbon
  • each kiln device using a single type of furnace cools carbides extracted from one furnace, some of them are used as ignition charcoal, and others are raw materials of activated carbon. It is supplied to (iii) and made into activated carbon through reheating,
  • the first object of the present invention for solving the above problems is to provide a structure in which the combustion heat supplied to the first kiln for carbonization and the second kiln for gas activation is simultaneously supplied from both ends of each kiln furnace in the shortest time. It is to implement a continuous activated carbon production apparatus that can improve productivity and produce high quality activated carbon by reducing the preheating process to keep the internal temperature of each kiln constant.
  • Another object of the present invention is to provide a structure in which the heat of combustion supplied to the first kiln for carbonization and the second kiln for gas activation circulates inside each kiln, thereby minimizing the consumption of combustion gas. It is to implement a continuous activated carbon production apparatus that can reduce fuel costs.
  • Still another object of the present invention is to provide a continuous activated carbon production apparatus capable of minimizing the scattering of exhaust gases discharged to the outside by providing an exhaust gas aggregation structure in the waste heat recovery unit.
  • the first combustion heat inlet 230 is provided with the combustion heat having a temperature range of 600 ⁇ 800 °C, respectively,
  • a separate transport pipe 240 and a carbide discharge port 250 are respectively provided,
  • the second combustion heat inlet 330 is formed to penetrate the transfer pipe 240 and provide combustion heat having a temperature range of 800 to 1100 ° C., respectively.
  • Carbide inlets 340 and activated carbon outlets 350 penetrating through the carbide outlets 250 are disposed at positions adjacent to the ventilation hole 320 and the second combustion heat inlet 330, respectively.
  • the second kiln furnace for gas activation to form a porous activated carbon 380 is formed in the inner space portion 360 of the second frame 310 to form a separate transport means 370 for transporting the carbide 280 ( 300);
  • An exhaust gas collection pipe 420 penetrating the ventilation hole 320 is formed at the center of the side of the body 410, the inside of which is sealed.
  • the reflux tube 430 one end of which penetrates the first combustion heat inlet 230, protrudes from the upper portion
  • the exhaust gas agglomeration tube 440 is installed at a lower portion of the body 410 by passing through the bottom surface, and a waste heat recovery part 400 in which a separate refrigerant 450 is filled in the outer circumferential surface of the exhaust gas agglomeration tube 440.
  • the present invention as described above has the advantage of improving the productivity by shortening the preheating process time by the improvement of the heat supply structure
  • FIG. 2 is a view illustrating an activated carbon generation route sequentially illustrating an activated carbon generation process of the present invention
  • FIG. 3 is a combustion gas supply path diagram showing a combustion gas supply form of the present invention.
  • 1 is an assembly of a raw material hopper 100, a carbonization first kiln 200, a gas-activated second kiln 300 and the waste heat recovery unit 400 constituting the continuous activated carbon production apparatus of the present invention Is the overall degree of coupling showing the state,
  • FIG. 2 is an activated carbon production path diagram sequentially illustrating a process of generating activated carbon of the present invention
  • FIG. 3 is a combustion gas supply path diagram illustrating a supply mode of the combustion gas of the present invention.
  • the raw material hopper 100 is stored organic raw material 110 corresponding to the raw material of the activated carbon, and
  • the second kiln 300 for gas activation to add a water gas catalyst to the carbide 280 to re-heat at a temperature range of 800 ⁇ 1100 °C to produce a porous activated carbon 380,
  • It is composed of a combination of the waste heat recovery unit 400 for discharging the exhaust gas generated in the carbonization first kiln 200 and the gas activation second kiln 300.
  • the individual structures of the raw material hopper 100, the carbonization first kiln 200 and the gas activating second kiln 300 are the individual structures used in the known kiln apparatus for producing activated carbon. I will say no,
  • the coupling structure of the present invention as shown in Figure 1, and the opposite end of the carbonization first kiln furnace 200, the first combustion heat inlet 230 is formed at one end,
  • the opposite end of the second kiln furnace 300 for gas activation provided with the second combustion heat inlet 330 is penetrated by the transfer pipe 240,
  • the carbide discharge port 250 formed at a position adjacent to the first combustion heat inlet 230 of the first kiln furnace 200 for carbonization is the second combustion heat inlet 330 of the second kiln furnace 300 for gas activation.
  • Penetrating the carbide inlet 340 formed in the opposite position to the exhaust gas collection pipe 420 of the waste heat recovery unit 400 is the second combustion heat inlet of the second kiln furnace 300 for gas activation. It is coupled with the ventilation hole 320 is formed in a position opposite to 330,
  • Reflux tube 430 formed on the upper portion of the body 410 constituting the waste heat recovery unit 400 is
  • the bottom surface of the body 410 has a structure in which the exhaust gas agglomeration tube 440 filled with the refrigerant 450 as an outer circumferential surface thereof penetrates the bottom surface of the body 410.
  • the combustion heat supplied from the first combustion heat inlet 230 of the first kiln furnace 200 for carbonization by the coupling structure of the present invention heats the internal space 260 of the first frame 210 and simultaneously discharges a carbide.
  • the internal space 360 of the second frame 310 constituting the second kiln 300 for gas activation is heated through the 250 and the carbide inlet 340,
  • the combustion heat supplied from the second combustion heat inlet 330 of the second kiln furnace 300 for gas activation heats the internal space 360 of the second framework 310 and is transferred through the transfer pipe 240. 1 by heating the inner space 260 of the frame 210,
  • Combustion heat and second combustion heat inlet 330 are supplied from the first combustion heat inlet 230 to the internal space 260 of the first frame 210 and the internal space 360 of the second frame 310. As the heat of combustion supplied from
  • the first kiln furnace 200 for carbonization and the second kiln furnace 300 for gas activation may improve productivity of activated carbon by shortening a preheating process stably maintaining a desired temperature in the shortest time.
  • the exhaust gas generated in the process of burning the impurities contained in the organic raw material 110 is formed through the carbide discharge port 250 and the transfer pipe 240 formed at both ends of the first frame 210, and the second frame body. Inflow into the exhaust gas collection pipe 420 constituting the internal space portion 360 and the waste heat recovery unit 400 of the 310 is discharged to the outside through the exhaust gas aggregation pipe 440.
  • the exhaust gas contains a large amount of high temperature organic volatile to maintain a very high temperature
  • High temperature organic volatiles containing the exhaust gas can be recycled to the heat of combustion
  • the organic volatile matter remaining in the exhaust gas introduced into the exhaust gas collection pipe 420 may also be recycled into the combustion heat of the first combustion heat inlet 230 through the reflux pipe 430.
  • the high temperature exhaust gas which is in a gas state, is filled in the outer circumferential surface of the exhaust gas condensing tube 440.
  • the internal temperature of the inner space portion 260 of the first frame 210 constituting the carbonization first kiln 200 is in the temperature range of 600 ⁇ 800 °C supplied from the first combustion heat inlet 230
  • the heat of combustion and the heat of combustion in the temperature range of 800 to 1100 ° C. supplied from the second combustion heat inlet 330 are simultaneously supplied, thereby shortening the preheating process in the shortest time.
  • the organic material raw material 110 transferred along the transfer means 270 provided in the inner space 260 of the first mold body 210 to maintain a desired temperature range uniformly is heated at a desired constant temperature.
  • the quality of the carbide 280 is to be improved.

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Environmental & Geological Engineering (AREA)
  • Inorganic Chemistry (AREA)
  • Carbon And Carbon Compounds (AREA)

Abstract

La présente invention concerne un dispositif pour la fabrication continue de charbon actif et, plus particulièrement, un dispositif pour la fabrication continue de charbon actif qui est capable de fabriquer un charbon actif de grande qualité en améliorant les structures d'alimentation en chaleur et les structures de circulation de la chaleur d'un four pour carbonisation et d'un four pour activation de gaz, le four étant constitué d'un dispositif de four continu couramment utilisé en tant que dispositif pour la fabrication de charbon actif, afin de stabiliser la température interne du dispositif de four continu en la durée la plus courte et avec une quantité minimale de combustible gazeux.
PCT/KR2010/007667 2010-01-22 2010-11-02 Dispositif pour la fabrication continue de charbon actif Ceased WO2011090260A2 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2010800619420A CN102844270A (zh) 2010-01-22 2010-11-02 用于连续生产活性炭的设备

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
KR1020100005789A KR101070636B1 (ko) 2010-01-22 2010-01-22 연속식 활성탄 제조장치
KR10-2010-0005789 2010-01-22

Publications (2)

Publication Number Publication Date
WO2011090260A2 true WO2011090260A2 (fr) 2011-07-28
WO2011090260A3 WO2011090260A3 (fr) 2011-11-03

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Family Applications (1)

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PCT/KR2010/007667 Ceased WO2011090260A2 (fr) 2010-01-22 2010-11-02 Dispositif pour la fabrication continue de charbon actif

Country Status (3)

Country Link
KR (1) KR101070636B1 (fr)
CN (1) CN102844270A (fr)
WO (1) WO2011090260A2 (fr)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103130220A (zh) * 2013-03-27 2013-06-05 徐州天正活性炭厂 内热式变径活性炭生产转炉
WO2014206154A1 (fr) * 2013-06-27 2014-12-31 密西西比国际水务有限公司 Procédé et appareil pour l'utilisation de la chaleur résiduelle de gaz de carneau à haute température
CN106698428A (zh) * 2017-02-28 2017-05-24 福建省木源炭科技有限公司 一种生产活性炭的设备及利用该设备生产活性炭的方法
CN112551527A (zh) * 2020-12-26 2021-03-26 河南省大潮炭能科技有限公司 一种超级电容器用活性炭的制备装置及其制作方法
CN113247896A (zh) * 2021-04-15 2021-08-13 中国铝业股份有限公司 活性炭活化装置

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2013082342A2 (fr) * 2011-11-30 2013-06-06 Corning Incorporated Appareil et procédé d'activation de charbon à l'aide d'un four périodique à chambres multiples
RU2638390C1 (ru) * 2016-09-30 2017-12-13 Общество с ограниченной ответственностью "Сорбенты Кузбасса" Колпаковая установка высокотемпературной термохимической активации углей

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JP3184910B2 (ja) * 1993-05-18 2001-07-09 株式会社ジェ・シィ・エー 廃タイヤを原料とする活性炭の製造装置
JP4267968B2 (ja) 2003-05-15 2009-05-27 三菱重工環境エンジニアリング株式会社 バイオマス処理法
JP2005103437A (ja) 2003-09-30 2005-04-21 Meidensha Corp 有機性含水物の加工方法とその施設
KR100503490B1 (ko) 2005-03-26 2005-07-22 김창준 슬러지나 음식물 또는 생활쓰레기 등의 유기물 및 폐기물 건조 탄화 처리시스템
JP2007284543A (ja) * 2006-04-14 2007-11-01 Okawa Transteel Corp 炭化処理方法と炭化処理装置
JP2010013329A (ja) 2008-07-04 2010-01-21 Haruo Shiraishi 高分子廃棄物からの活性炭製造システム

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103130220A (zh) * 2013-03-27 2013-06-05 徐州天正活性炭厂 内热式变径活性炭生产转炉
WO2014206154A1 (fr) * 2013-06-27 2014-12-31 密西西比国际水务有限公司 Procédé et appareil pour l'utilisation de la chaleur résiduelle de gaz de carneau à haute température
CN106698428A (zh) * 2017-02-28 2017-05-24 福建省木源炭科技有限公司 一种生产活性炭的设备及利用该设备生产活性炭的方法
CN112551527A (zh) * 2020-12-26 2021-03-26 河南省大潮炭能科技有限公司 一种超级电容器用活性炭的制备装置及其制作方法
CN112551527B (zh) * 2020-12-26 2023-06-23 河南省大潮炭能科技有限公司 一种超级电容器用活性炭的制备装置及其制作方法
CN113247896A (zh) * 2021-04-15 2021-08-13 中国铝业股份有限公司 活性炭活化装置

Also Published As

Publication number Publication date
KR20100018008A (ko) 2010-02-16
WO2011090260A3 (fr) 2011-11-03
KR101070636B1 (ko) 2011-10-07
CN102844270A (zh) 2012-12-26

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