JPH0361729B2 - - Google Patents

Info

Publication number
JPH0361729B2
JPH0361729B2 JP8168784A JP8168784A JPH0361729B2 JP H0361729 B2 JPH0361729 B2 JP H0361729B2 JP 8168784 A JP8168784 A JP 8168784A JP 8168784 A JP8168784 A JP 8168784A JP H0361729 B2 JPH0361729 B2 JP H0361729B2
Authority
JP
Japan
Prior art keywords
charcoal
briquettes
powder
binder
moisture
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.)
Expired
Application number
JP8168784A
Other languages
Japanese (ja)
Other versions
JPS60228622A (en
Inventor
Masaharu Matsui
Seizaburo Takai
Isamu Uchida
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.)
JFE Engineering Corp
Original Assignee
Nippon Kokan 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 Nippon Kokan Ltd filed Critical Nippon Kokan Ltd
Priority to JP8168784A priority Critical patent/JPS60228622A/en
Priority to BR8501942A priority patent/BR8501942A/en
Publication of JPS60228622A publication Critical patent/JPS60228622A/en
Publication of JPH0361729B2 publication Critical patent/JPH0361729B2/ja
Granted legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L5/00Solid fuels
    • C10L5/02Solid fuels such as briquettes consisting mainly of carbonaceous materials of mineral or non-mineral origin
    • C10L5/06Methods of shaping, e.g. pelletizing or briquetting
    • C10L5/10Methods of shaping, e.g. pelletizing or briquetting with the aid of binders, e.g. pretreated binders
    • C10L5/12Methods of shaping, e.g. pelletizing or briquetting with the aid of binders, e.g. pretreated binders with inorganic binders
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L5/00Solid fuels
    • C10L5/02Solid fuels such as briquettes consisting mainly of carbonaceous materials of mineral or non-mineral origin
    • C10L5/34Other details of the shaped fuels, e.g. briquettes
    • C10L5/36Shape
    • C10L5/366Powders
    • 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Geology (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Manufacture And Refinement Of Metals (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

〔発明の技術分野〕 本発明は木炭粉のブリケツト製造法に関するも
のである。 〔従来技術〕 現在木炭粉は木炭の使用先で篩別けしその篩下
粉として、或は輸送過程に於て発生されるが、そ
の大部分は排棄され有効利用されてない。一般に
発生微粉量は輸送過程で15〜20%、輸送後使用先
で3%程度発生すると云われ、そのごく一部を除
き殆んどが排棄されている。 また木炭中の水撫は、釜出し時4%程度である
が輸送が保管中に水分を吸収し通常7〜9%最高
30%にも達する場合がある。 水分が15%以下であれば、製鉄高炉に混用しも
影響が少なくそのまゝ利用できるが、それ以上に
なると、蒸発した水分の放出速度より蒸気発生速
度が大となり、炉内で木炭が粉化するため炉況の
不調原因となる。従つて水分の管理が重要である
が、粉塵爆発防止のため、極力開放された状態で
運搬や保管を行なうため、水分の吸収は不可避な
問題である。 木炭微粉のブリケツト化については、従来木炭
が家庭内で燃料として利用されていた当時は、木
炭粉をすり潰し、ニカワ、糖密液等の粘結剤を加
へ手作業にて団塊とし、自然乾燥にて硬化させ暖
房用炭団(タドン)として使用されていた。然し
ながら生産性も低く到底工業用として利用出来る
ものではなかつた。 一方暖房用燃料として木炭粉ではなく無煙炭を
主原料として、粘土、ベントナイト、ニカワ、糖
密液、パルプ廃液等を粘結剤として混合し、ロー
ル式プレス成型機で成型する豆炭や、スタンプ式
の穴明煉炭等が知られている。 この場合原料が石炭系であり、吸水性が少く、
比重が木炭より重く、また木炭の様に繊維質が無
いため、その組織が緻密であるので成型が可能で
あつた。然しながら木炭粉を前述のような方法で
処理した場合、最高30%に及び水分を有し、かつ
軟かく、木炭の木質部の繊維質が炭化して、炭化
部分が多数存在するので、在来の石炭ブリケツト
の粘結剤である中ピツチやアスフアルト系、瀝青
系のものでは、木炭の各粒子を被覆するには、展
延性が悪く、また吸水に富んでいるため、その表
面の湿性も悪く成型性が劣り、強圧により破壊さ
れ、ブリケツト化は困難である。従つてフレツト
ミルのロールにてすり潰すことにより、その木炭
の組牲を破壊することが必要となる。 木炭粉をブリケツト化するためには次の各工程
を必要とする。即ち (1) 木炭の粗雑な機構を破壊するための強力な機
械的粉砕工程 (2) 木炭粒子表面に均等に、比重、特性の異なる
粘結剤を混合展延させる工程 (3) 使用粘結剤に応じて必要な加熱工程 (4) 使用粘結剤に応じて水を添加または除く工程 (5) 強力な圧縮成型工程 (6) 仕上り品の硬度向上と水分調整工程 以上の6工程を必須とされ、従つて従来の無煙
炭ブリケツト化設備では、木炭粉のブリケツト化
は出来なかつた。 次に粘結剤をその木炭微粒子表面に薄く展延さ
せるには、前述の如くその表面の湿性が必要であ
るが、吸水性の無い木炭の場合、重量比5〜6%
の水分を必要とするが、木炭質の場合は内部に吸
収し、しかも表面に必要な湿性を保持しなければ
粘結剤の経済的な展延は望めない。この調整が石
炭のブリケツトの方法ではできない。 〔発明の目的〕 本発明は、従来廃棄され利用されていない木炭
の微粉を適当な大きさのブリケツトとし、しかも
水分を15%に保持することに依り、木炭高炉や電
気炉に使用可能な木炭粉ブリケツトの製造法を提
供するにある。 〔発明の概要〕 本発明は、上記目的を達成するために、特許
980334号に開示された「強固なるコークス用成型
炭の製造法及びこれに用いる装置」の高速撹拌羽
根を有する混合装置」(以下K.Bミクサーという)
を利用し、従来の木炭粉よりブリケツトを製造す
るに必要な工程を出来るだけ簡素化し、前記(1)〜
(4)工程を1工程にて処理し、圧縮成型、水分調整
するものである。即ち本発明の要旨は 木炭粉単体または木炭粉と鉄鉱石粉との混合物
を原料とし、該原料に粘結剤を加えてブリケツト
を製造する工程において、高速撹拌羽根を有する
混合機で、原料の粉砕、粘結剤の添加、混合、加
熱処理の一連の工程を一工程にて処理し、次いで
圧縮成型、水分調整を行なうことを特徴とする木
炭粉ブリケツト製造法にある。 〔発明の構成〕 次に本発明を第1図に示す本発明の工程図に基
いて説明する。普通10mm以下の篩下粉または極小
微粉を一括して原料供給ホツパ1に装入し、これ
により、高速撹拌KBミクサー2に導入し、高速
回転する上下羽根で木炭は粉砕される。この際木
炭々質によつて、微粉砕される粒度が異なるため
この回転数は変速機4にて任意に変更できる。高
速撹拌KBミクサー2内の滞留時間は2〜5分で
充分である。次に必要な粘結剤例えば、カルボキ
シ・メチルセルロウスCMC、ポリビニル・アル
コールその他合成樹脂、澱粉、リグニン、無機質
のベントナイト、セメント、水ガラス、ピツチ、
タール、ホタール等の内単体もしくは2〜4種の
混合粘結剤ホツパー5より供給する。また水分を
必要とする場合水槽6より高速撹拌KBミクサー
2内に同時に添加する。木炭粒子構成や特性によ
り前記(1)、粉砕工程(2)、粘結剤との混合展延工程
(3)加熱工程を同時に行なうことも出来る。 一方木炭の吸水率が多い時には高速撹拌KBミ
クサー2の外筒7に熱源供給装置(蒸気、熱媒
油、排熱等)8より熱を供給し間接加熱にて水分
を排気筒9より放出させる。 本発明方法によれば水分は前記粉砕工程と同時
に同一高速撹拌KBミクサー2内で加水すること
により容易に調整できる。また粘結剤の展延後余
分の水分は成型時の障害となるので、充分展延さ
せた後、高速撹拌KBミクサー2の外筒7からの
熱により水分を排出させる。勿論水分の多少は使
用する粘結剤の特性に関係があるので、予じめ木
炭質の水分と粘結剤の必要とする水分を測定して
おくことが必要である。 この水分調整もKBミクサー2の高速撹拌
(260r/m)による同一容器内での撹拌状況で行
なわれるので、有効熱伝導面積も広く効果良く実
施できる。 次に下部より排出された処理原料は一旦ホツパ
ー10に貯えられ、圧縮成型機10、ロール式成
型機11またはデスク式成型機12に装入され
る。ロール式成型機11には第2図に示す如く、
圧縮時に出る過多な水分を除去し易い水切溝13
があり、デスク式成型機12には第3図に示す如
くそのモールド円周に脱水溝14が設けられてい
る。いずれも圧縮効率が良好である。 圧縮成型されたブリケツトはその時使用した粘
結剤の特性により熱風乾燥炉15を通過させ、仕
上り品の水分と硬度を調整する。熱風乾燥炉15
を通過後製品ホツパー16に一時貯えられるかま
たは直接木炭高炉17に装入される。木炭高炉の
代りに電気炉でもよい。 〔発明の実施例〕 次に本発明の実施例について述べる。 実施例 1 原木炭を国内の軟炭のナラ炭を基準炭として、
基準炭と、原木炭の8mm篩下粉を成型したブリケ
ツトA、各粘結剤の組合せを変え製造したブリケ
ツトBを前述の工程に基いて製造した。 粘結剤の配合並に物理性を第1表に示す。
[Technical Field of the Invention] The present invention relates to a method for producing charcoal powder briquettes. [Prior Art] Currently, charcoal powder is generated as an unsieved powder after sifting the charcoal at the place where it is used, or during the transportation process, but most of it is discarded and not used effectively. Generally, it is said that 15 to 20% of the fine powder is generated during the transportation process, and about 3% at the destination after transportation, and most of it, except for a small portion, is discarded. In addition, the water content in charcoal is about 4% when taken out of the pot, but it usually reaches a maximum of 7 to 9% because it absorbs moisture during transportation and storage.
It can reach up to 30%. If the moisture content is less than 15%, it can be used in a steelmaking blast furnace with little effect and can be used as is, but if it exceeds that, the rate of steam generation will be faster than the rate of release of evaporated moisture, and the charcoal will become powder in the furnace. This causes the furnace to malfunction. Therefore, moisture management is important, but moisture absorption is an unavoidable problem because the products are transported and stored in an open state as much as possible to prevent dust explosions. Regarding the production of briquettes from fine charcoal powder, in the past, when charcoal was used as fuel at home, the charcoal powder was ground, then a binder such as glue or molasses liquid was added to form briquettes by hand, and then air-dried. It was hardened and used as a heating charcoal block (tadong). However, productivity was low and it could not be used for industrial purposes. On the other hand, as a heating fuel, anthracite is used as the main raw material instead of charcoal powder, and clay, bentonite, glue, molasses liquid, pulp waste liquid, etc. are mixed as a binder, and the mixture is molded with a roll press molding machine. Anamei briquettes are known. In this case, the raw material is coal-based, has low water absorption,
Since it has a higher specific gravity than charcoal and is not fibrous like charcoal, it has a dense structure that allows it to be molded. However, when charcoal powder is treated using the method described above, it has a moisture content of up to 30% and is soft. Medium pitch, asphalt-based, and bituminous binders for coal briquettes have poor spreadability to coat each charcoal particle, and since they absorb a lot of water, the surface has poor moisture retention and is difficult to mold. It has poor properties, breaks down under strong pressure, and is difficult to make into briquettes. Therefore, it is necessary to break the texture of the charcoal by grinding it with the rolls of a fret mill. The following steps are required to make charcoal powder into briquettes. Namely, (1) a powerful mechanical crushing process to destroy the rough structure of the charcoal; (2) a process of mixing and spreading caking agents with different specific gravity and properties evenly on the surface of the charcoal particles; and (3) the caking used. Heating process required depending on the agent (4) Adding or removing water depending on the binder used (5) Powerful compression molding process (6) Improving the hardness of the finished product and adjusting moisture The above six steps are essential Therefore, it was not possible to briquette charcoal powder using conventional anthracite briquetting equipment. Next, in order to thinly spread the binder on the surface of the fine charcoal particles, the surface needs to be moist as described above, but in the case of charcoal that does not have water absorption, the weight ratio is 5 to 6%.
However, in the case of charcoal, economic expansion of the binder cannot be expected unless it is absorbed into the interior and maintains the necessary moisture on the surface. This adjustment cannot be made using the coal briquetting method. [Object of the Invention] The present invention produces charcoal that can be used in charcoal blast furnaces and electric furnaces by turning fine charcoal powder, which has conventionally been discarded and unused, into briquettes of an appropriate size and keeping the moisture content at 15%. To provide a method for manufacturing powder briquettes. [Summary of the invention] In order to achieve the above object, the present invention
``Mixing device with high-speed stirring blades'' (hereinafter referred to as KB mixer) of ``Method for producing strong briquette coal for coke and apparatus used therein'' disclosed in No. 980334
By using the above-mentioned (1) to simplify the process necessary to produce briquettes from conventional charcoal powder as much as possible,
(4) Processing is performed in one step, compression molding and moisture adjustment. That is, the gist of the present invention is to use charcoal powder alone or a mixture of charcoal powder and iron ore powder as a raw material, and in the process of manufacturing briquettes by adding a binder to the raw material, the raw material is pulverized using a mixer having high-speed stirring blades. A method for producing charcoal powder briquettes is characterized in that a series of steps of adding a binder, mixing, and heat treatment are performed in one step, followed by compression molding and moisture adjustment. [Structure of the Invention] Next, the present invention will be explained based on the process chart of the present invention shown in FIG. Subsieved powder or extremely fine powder, usually 10 mm or less in size, is charged in bulk into the raw material supply hopper 1, and then introduced into the high-speed stirring KB mixer 2, where the charcoal is pulverized by the upper and lower blades rotating at high speed. At this time, since the particle size to be finely pulverized differs depending on the charcoal substance, this rotational speed can be arbitrarily changed by the transmission 4. A residence time of 2 to 5 minutes in the high-speed stirring KB mixer 2 is sufficient. Next, the necessary binders include carboxy methylcellulose CMC, polyvinyl alcohol and other synthetic resins, starch, lignin, inorganic bentonite, cement, water glass, pitch,
A single binder or a mixed binder of 2 to 4 of tar, firefly, etc. is supplied from the hopper 5. If water is required, it is simultaneously added from the water tank 6 into the high-speed stirring KB mixer 2. Depending on the charcoal particle structure and characteristics, the above (1), the crushing process (2), and the mixing and spreading process with a caking agent
(3) The heating process can also be performed simultaneously. On the other hand, when the water absorption rate of charcoal is high, heat is supplied from the heat source supply device (steam, thermal oil, waste heat, etc.) 8 to the outer cylinder 7 of the high-speed stirring KB mixer 2, and moisture is released from the exhaust pipe 9 by indirect heating. . According to the method of the present invention, water content can be easily adjusted by adding water in the same high-speed stirring KB mixer 2 at the same time as the grinding process. Further, excess moisture after spreading the binder becomes an obstacle during molding, so after sufficient spreading, the moisture is discharged by heat from the outer cylinder 7 of the high-speed stirring KB mixer 2. Of course, the amount of moisture is related to the characteristics of the binder used, so it is necessary to measure the moisture content of the charcoal and the moisture required by the binder in advance. This moisture adjustment is also carried out in the same container with high-speed stirring (260 r/m) by the KB mixer 2, so that the effective heat transfer area can be widened and carried out effectively. Next, the processed raw material discharged from the lower part is temporarily stored in a hopper 10 and charged into a compression molding machine 10, a roll molding machine 11, or a desk molding machine 12. As shown in FIG. 2, the roll forming machine 11 includes:
Drainage groove 13 that makes it easy to remove excess moisture released during compression
As shown in FIG. 3, the desk type molding machine 12 is provided with a dewatering groove 14 around the mold circumference. Both have good compression efficiency. The compression molded briquettes are passed through a hot air drying oven 15 to adjust the moisture and hardness of the finished product, depending on the properties of the binder used at that time. Hot air drying oven 15
After passing through, the product is temporarily stored in a hopper 16 or directly charged into a charcoal blast furnace 17. An electric furnace may be used instead of a charcoal blast furnace. [Embodiments of the Invention] Next, embodiments of the present invention will be described. Example 1 Raw charcoal was made using domestic soft oak charcoal as the reference charcoal.
Briquettes A were prepared by molding standard charcoal and raw charcoal powder under a sieve of 8 mm, and briquettes B were prepared by changing the combination of each binder, based on the above-mentioned process. The formulation and physical properties of the binder are shown in Table 1.

【表】 第1表に示す如く、ブリケツトABとの基準の
木炭と比較して大差が無いので、高炉に装入でき
るものであり、また水分は基準と比較してブリケ
ツトABは少なく、水分による高炉内の挙動は優
れているものである。 実施例 2 原料の木炭粉に鉄鉱石微粉を同時に混合してブ
リケツトを製造した例について述べる。 実施例1と同様な工程にて、次の第2表に示す
如く配合にてブリケツトC,D,Eを製造し、そ
の結果の物理性をも第2表に示す。
[Table] As shown in Table 1, there is no big difference between briquette AB and the standard charcoal, so it can be charged into the blast furnace, and the moisture content of briquette AB is less compared to the standard, so it is not caused by moisture. The behavior inside the blast furnace is excellent. Example 2 An example will be described in which briquettes were manufactured by simultaneously mixing raw charcoal powder and iron ore fine powder. Briquettes C, D, and E were manufactured using the same process as in Example 1 and the formulations shown in Table 2 below, and the physical properties of the results are also shown in Table 2.

【表】【table】

【表】 第2表に示す如く、木炭粉に鉄鉱石を混合して
も本製造法によるとブリケツト化し得て、その強
度も比重の重い鉄鉱石粉が混合されるので良好な
成績を示した。 尚木炭粉と鉄鉱石粉との混合割合は1:1が最
高である。また石灰にて鉄鉱石粉を置換えること
も可能である。 木炭高炉の特徴は、木炭の物理的強度の弱さか
ら、高炉が上げられず低い点にある。一方木炭は
コークスに比して反応性が高いため、炉高を上げ
る必要がないので大型化は難しいと云われてい
る。従つて通常木炭高炉の有効内容積は40〜300
m3生産量50〜500T/D程度であるため、本発明
による木炭粉ブリケツトは充分使用可能である。
但し使用高炉容積により、前記ブリケツトの熱間
圧潰が尚必要とする場合は、粘結剤を熱可塑性の
アクリル系樹脂または熱硬化性の粘結剤を単体ま
たは他の粘結剤と組合せることにより更に向上す
ることができる。 〔発明の効果〕 叙上の如く本発明による木炭粉製造法によれば
従来の石炭ブリケツト製造工程ではできなかつた
木炭粉のブリケツト化を、高速撹拌羽根を有する
混合機の利用と粘結剤を選択使用することによ
り、工程を短縮して簡単にかつ経済的に製造を可
能とした甚だ有効な方法であり、木炭粉の有効利
用と、木炭高炉または電気炉等における使用を可
能とした有用な発明である。
[Table] As shown in Table 2, even if iron ore is mixed with charcoal powder, it can be made into briquettes according to this production method, and the strength of the briquettes is also good because the iron ore powder, which has a heavy specific gravity, is mixed. The best mixing ratio of charcoal powder and iron ore powder is 1:1. It is also possible to replace iron ore powder with lime. A characteristic of charcoal blast furnaces is that the blast furnace cannot be raised due to the weak physical strength of charcoal. On the other hand, charcoal has higher reactivity than coke, so it is said that it is difficult to increase the size of the furnace because there is no need to raise the furnace height. Therefore, the effective internal volume of a normal charcoal blast furnace is 40 to 300
The charcoal powder briquette according to the present invention can be used satisfactorily since the production amount is about 50 to 500 T/D.
However, if hot crushing of the briquettes is still required depending on the volume of the blast furnace used, the binder may be a thermoplastic acrylic resin or a thermosetting binder alone or in combination with other binders. This can be further improved. [Effects of the Invention] As described above, according to the charcoal powder production method of the present invention, charcoal powder can be made into briquettes, which could not be achieved with the conventional coal briquette production process, by using a mixer with high-speed stirring blades and using a binder. This is an extremely effective method that shortens the process and enables easy and economical production by selectively using charcoal powder. It is an invention.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は本発明製造方法を示す工程図、第2図
はロール式成型機の脱水溝を示す模式図、第3図
はデスク式成型機の脱水溝を示すモールドの模式
図である。 図において、1…木炭粉ホツパー、2…高速撹
拌混合機、3…撹拌羽根、5…粘結剤ホツパー、
7…外筒、8…熱源供給装置、9…排気筒、10
…圧縮成型機、11…ロール式成型機、12…デ
スク式成型機、13…水切溝、14…脱水溝、1
5…熱風乾燥炉、17…高炉又は電気炉。
FIG. 1 is a process diagram showing the manufacturing method of the present invention, FIG. 2 is a schematic diagram showing a dewatering groove of a roll-type molding machine, and FIG. 3 is a schematic diagram of a mold showing a dewatering groove of a desk-type molding machine. In the figure, 1... Charcoal powder hopper, 2... High speed stirring mixer, 3... Stirring blade, 5... Binder hopper,
7...Outer cylinder, 8...Heat source supply device, 9...Exhaust pipe, 10
...Compression molding machine, 11...Roll type molding machine, 12...Desk type molding machine, 13...Draining groove, 14...Dewatering groove, 1
5... Hot air drying oven, 17... Blast furnace or electric furnace.

Claims (1)

【特許請求の範囲】[Claims] 1 木炭粉単体または木炭粉と鉄鉱石粉との混合
物を原料とし、該原料に粘結剤を加えてブリケツ
トを製造する工程において、高速撹拌羽根を有す
る混合機で、原料の粉砕、粘結剤の添加、混合、
加熱処理の一連の工程を一工程にて処理し、次い
で圧縮成型、水分調整を行なうことを特徴とする
木炭粉ブリケツト製造法。
1. In the process of manufacturing briquettes using charcoal powder alone or a mixture of charcoal powder and iron ore powder as a raw material and adding a binder to the raw material, a mixer with high-speed stirring blades is used to crush the raw material and remove the binder. addition, mixing,
A method for producing charcoal powder briquettes characterized by performing a series of heat treatment steps in one step, followed by compression molding and moisture adjustment.
JP8168784A 1984-04-25 1984-04-25 Charcoal powder briquette manufacturing method Granted JPS60228622A (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP8168784A JPS60228622A (en) 1984-04-25 1984-04-25 Charcoal powder briquette manufacturing method
BR8501942A BR8501942A (en) 1984-04-25 1985-04-24 PROCESS OF MANUFACTURING COAL BRIQUETS

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8168784A JPS60228622A (en) 1984-04-25 1984-04-25 Charcoal powder briquette manufacturing method

Publications (2)

Publication Number Publication Date
JPS60228622A JPS60228622A (en) 1985-11-13
JPH0361729B2 true JPH0361729B2 (en) 1991-09-20

Family

ID=13753264

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8168784A Granted JPS60228622A (en) 1984-04-25 1984-04-25 Charcoal powder briquette manufacturing method

Country Status (2)

Country Link
JP (1) JPS60228622A (en)
BR (1) BR8501942A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2023523173A (en) * 2020-04-24 2023-06-02 ポール ヴルス エス.エイ. Raw material supply method to sintering plant

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0635622B2 (en) * 1989-04-12 1994-05-11 日本磁力選鉱株式会社 Steelmaking raw material manufacturing method
KR20040019425A (en) * 2002-08-26 2004-03-06 민병창 Compound iron and mineral material including mineral rock and fragment iron as an essential element and method of manufacturing it
FR2882368A1 (en) * 2005-02-21 2006-08-25 Andreas Anest ECOLOGICAL CHARCOAL GUARANTEED WITHOUT WOOD
JP5880941B2 (en) * 2012-01-31 2016-03-09 Jfeスチール株式会社 Method for producing reduced iron
KR101728824B1 (en) * 2014-12-23 2017-04-20 주식회사 포스코 Method for manufacturing coal briquettes, and the device

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2023523173A (en) * 2020-04-24 2023-06-02 ポール ヴルス エス.エイ. Raw material supply method to sintering plant

Also Published As

Publication number Publication date
BR8501942A (en) 1985-12-24
JPS60228622A (en) 1985-11-13

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