JPS58140311A - Manufacture of molded activated carbon using wood as starting material - Google Patents

Manufacture of molded activated carbon using wood as starting material

Info

Publication number
JPS58140311A
JPS58140311A JP57019721A JP1972182A JPS58140311A JP S58140311 A JPS58140311 A JP S58140311A JP 57019721 A JP57019721 A JP 57019721A JP 1972182 A JP1972182 A JP 1972182A JP S58140311 A JPS58140311 A JP S58140311A
Authority
JP
Japan
Prior art keywords
wood
raw material
pellets
activated carbon
crushed
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.)
Granted
Application number
JP57019721A
Other languages
Japanese (ja)
Other versions
JPS611365B2 (en
Inventor
Hidekazu Fujimori
藤森 英一
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.)
Japan Steel Works Ltd
Original Assignee
Japan Steel Works 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 Japan Steel Works Ltd filed Critical Japan Steel Works Ltd
Priority to JP57019721A priority Critical patent/JPS58140311A/en
Publication of JPS58140311A publication Critical patent/JPS58140311A/en
Publication of JPS611365B2 publication Critical patent/JPS611365B2/ja
Granted legal-status Critical Current

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Abstract

PURPOSE:To obtain woody molded activated carbon of high quality without using a binder by crushing wood as a starting material, extrusion-molding the crushed wood after adjusting the water content, carbonizing the moldings by heating, and carrying out activation in a specified atmosphere. CONSTITUTION:Woody waste, etc. are crushed and classified. This crushed starting material having a prescribed grain size is dried to adjust the water content to about 12-18wt%, and the dried material is extrusion-molded at high temp. and pressure with a continuous compression molding machine or the like. The moldings are cut to form woody pellets, and the pellets are carbonized by heating at about 400-700 deg.C. The carbonized pellets are activated in a steam atmosphere at about 800-1,000 deg.C in a rotary kiln or the like to grow the porous structure of the pellets. By this method woody molded activated carbon having many pores and high adsorbing power is obtd.

Description

【発明の詳細な説明】 本発明は、木材を原料とする成形活性炭の製造方法に関
するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing shaped activated carbon using wood as a raw material.

ガス処理、液体処理等に使用される。p、形活性炭を製
造する従来の方法では、粉砕した原料に粘結剤すなわち
バインダ(タール、ピッチ、網布等)を添加し、練合成
形、炭化、賦活、酸洗、乾燥、選別の工程によって製造
していた。
Used for gas processing, liquid processing, etc. In the conventional method for producing p-type activated carbon, a caking agent or binder (tar, pitch, mesh cloth, etc.) is added to the pulverized raw material, and the steps of kneading, carbonization, activation, pickling, drying, and sorting are carried out. It was manufactured by.

しかしながら、上記のような従来の木材を原料とする成
形活性炭の製造方法にあっては、バインダを原料に添加
していたため、粒状の原料と液状のバインダとを混合す
る際に原料中の空気を脱気して密度を大きくする必要が
あったが、真空装置を備えたスクリュニーダ等を使用し
ても十分な脱気を行なうことができなかった。また、バ
インダは揮発性物質を主成分としており、炭化の際に既
発成分が成形物内に比較的大きな空孔を作り、このため
成形物の強度及び密度が低下するという問題点があった
。更に、バインダの種類によっては炭化時にM員酸化物
等の有害ガスを発生するという問題点があった。
However, in the conventional method for producing shaped activated carbon using wood as the raw material, binder is added to the raw material, so when mixing the granular raw material and liquid binder, air in the raw material is removed. It was necessary to increase the density by degassing, but sufficient degassing could not be achieved even by using a screw kneader or the like equipped with a vacuum device. In addition, the binder is mainly composed of volatile substances, and during carbonization, the emitted components create relatively large pores within the molded product, which causes a problem in that the strength and density of the molded product decreases. . Furthermore, depending on the type of binder, there is a problem in that harmful gases such as M-member oxides are generated during carbonization.

本発明は、従来の木材を原料とする成形活性炭の製造方
法における=E記ような問題点に着目してなされたもの
であり、バインダを使用することなく成形活性炭を製造
″することができるようにすることにより、上記問題点
を解消することを目的としている。
The present invention has been made by focusing on the problems described in E in the conventional method for producing shaped activated carbon using wood as a raw material, and has made it possible to produce shaped activated carbon without using a binder. The aim is to solve the above problems by doing so.

以下、本発明をその実施例を示す添付図面に基づいて説
明する。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described below with reference to the accompanying drawings showing embodiments thereof.

まず、木質系廃棄物である原材料をチッパ等の粗破砕機
によって1次破砕し、最大長500 mmmトド最大径
100mm以下の木片とし、これを原料とする。なお、
〈ぎ、かすがい等の鉄片を含む原材料の場合には、1次
破砕後、磁選機によって鉄片を除去する。
First, the raw material, which is wood waste, is first crushed using a coarse crusher such as a chipper to produce wood pieces with a maximum length of 500 mm and a maximum diameter of 100 mm, which are used as the raw material. In addition,
In the case of raw materials containing iron pieces, such as shavings and scraps, the iron pieces are removed by a magnetic separator after the primary crushing.

次いで、原料を衝撃式破砕機によって2次破砕し、鯰大
長30mm以下、最大径5mm以下の細片又は粉粒の破
砕原料にする。なお、破砕原料に石片等の異物が混入し
ている場合には、風力選別により異物を除去する。風力
選別は、トラップを備えた輸送管内を風力によって破砕
原料を移動させ、比重の大きい異物を・トラップ内に捕
集することにより行なう。
Next, the raw material is subjected to secondary crushing using an impact crusher to obtain crushed raw material in the form of small pieces or powder having a catfish size of 30 mm or less and a maximum diameter of 5 mm or less. Note that if the crushed raw material contains foreign matter such as stone chips, the foreign matter is removed by air sorting. Wind sorting is performed by moving the crushed raw material by wind power through a transport pipe equipped with a trap, and collecting foreign matter with a large specific gravity in the trap.

次いで、破砕原料は水分調節される。水分調整において
は、破砕原料中の水分が12〜18重量%となるように
ロータリキルン式乾燥機で乾燥させる。なお、水分調整
の前の状態では、生木を原材料にした場合の水分は通常
45〜5511!:量%であり、製材過程の廃材の水分
は20〜30重琶%であり、また建築廃材の水分は10
〜20重蓮%である。従って、建築廃材の場合はほとん
ど乾燥の必要がない。
The crushed raw material is then moisture-adjusted. In moisture adjustment, the crushed raw material is dried in a rotary kiln dryer so that the moisture content becomes 12 to 18% by weight. In addition, before moisture adjustment, the moisture content when raw wood is used as raw material is usually 45-5511! :% by weight, the moisture content of waste wood from the lumber process is 20 to 30%, and the moisture content of construction waste wood is 10%.
~20 Juren%. Therefore, in the case of construction waste materials, there is almost no need for drying.

水分調整後、破砕原料はふるいにかけて選別され、含ま
れていた粗粒片は再び2次破砕に送り返される。送り返
された粗粒片は再び2次破砕されるが、今回は水分調整
されて乾燥しているため、所定寸法まで確実に破砕され
る。
After adjusting the moisture content, the crushed raw material is sieved and sorted, and the coarse particles contained therein are sent back to secondary crushing. The returned coarse particles are crushed again for a second time, but this time the moisture content has been adjusted and the pieces have been dried, so they are reliably crushed to a predetermined size.

選別工程を通過した好適な大きさの破砕原料は貯留容器
内に収容され、定量供給機によって連続圧縮成形機に一
定量供給される。連続圧縮成形機は、モータによって回
転される円筒状のダイスと、ダイス内径部に接するよう
に配置される複数のロールと、破砕原料を各ロール間に
均等に分配するスプレッダとを有している。ダイス内に
投入された破砕原料は、ダイス内径部とロールとの間に
かみ込まれ、ダイスに放射状に設けたダイス穴から外周
へ連続的に押出される。ダ、イス穴の直径は5〜7mm
であり、このダイス穴から押出された円柱状の成形品は
、ダイス外周に近接して設けられたカッタによって適当
な長さに切断される。
The crushed raw material of a suitable size that has passed through the sorting process is stored in a storage container, and is supplied in a fixed amount to a continuous compression molding machine by a quantitative feeder. A continuous compression molding machine has a cylindrical die rotated by a motor, a plurality of rolls placed in contact with the inner diameter of the die, and a spreader that evenly distributes the crushed raw material between the rolls. . The crushed raw material introduced into the die is caught between the inner diameter portion of the die and the roll, and is continuously extruded toward the outer periphery through die holes provided radially in the die. The diameter of the chair hole is 5-7mm.
The cylindrical molded product extruded from the die hole is cut into an appropriate length by a cutter provided close to the outer periphery of the die.

ダイスとロールとの間で圧縮されダイス穴を通過する際
に、破砕原料の温欧は150〜200℃に達し、圧力は
400〜8000kg/cm’に達する。このため破砕
原料は6r塑化され、原料中に含まれるリグニン、樹脂
等の作用によって自己粘結する。こうして粘結された成
形品は1.4g/cm3程度の高密度に圧縮された状態
となる。また、1−記のような高温高圧下で圧縮成形す
ると、原料がダイス穴を通過するときワックス等の樹脂
成分が表面ににじみ出て、成形品の表面に光沢膜がで5
る。光沢膜ができない程度の低い温度・圧力で成形した
場合には、成形品の結合が弱く1表面にひび割れを生じ
、最絆製品である活性炭の品質が低ドする。上記成形の
過程で原料中の水分は3〜5重植%だけ減少する。成形
品を切断して作った木質ペレットは、次の炭化工程に移
行する前に空冷され、これによって更に水分が減少し、
強度が増大する。
When compressed between a die and a roll and passed through a die hole, the temperature of the crushed raw material reaches 150 to 200°C and the pressure reaches 400 to 8000 kg/cm'. For this reason, the crushed raw material is plasticized by 6R and self-caking due to the action of lignin, resin, etc. contained in the raw material. The molded product thus caked is compressed to a high density of approximately 1.4 g/cm 3 . In addition, when compression molding is performed under high temperature and high pressure as described in 1-, when the raw material passes through the die hole, resin components such as wax ooze out onto the surface, creating a glossy film on the surface of the molded product.
Ru. If molding is performed at low temperatures and pressures that do not produce a glossy film, the bonding of the molded product will be weak and cracks will occur on one surface, reducing the quality of the activated carbon that is the most bonded product. During the above-mentioned molding process, the moisture content in the raw material is reduced by 3 to 5 percent. Wood pellets made by cutting the molded product are air-cooled before moving on to the next carbonization process, which further reduces moisture content.
Strength increases.

空冷された木質ペレットは炭化工程に送られる。炭化工
程では、木質ペレットは、酸素の存在しない又はほとん
ど存在しない炉中において400〜700℃に加熱され
る。これによって木質ペレットは炭化して体積が40〜
50%に収縮し木炭ペレットとなる。なお、炭化時間は
、細かく切断された木炭ペレットの炭化であるので、非
常に短くてすむ。また、木質ペレットに対する木炭ペレ
ットの収率は30〜45%(重り比)であった。これは
、木質ペレット中の水分及び揮発分が失われ、また木質
ペレットの一部が熱分解するからである。炭化ペレット
は、炭化の際に揮発性物質が失われた部分及び揮発性物
質が通過した部分が空隙となった多孔性の構造となって
いる。
The air-cooled wood pellets are sent to the carbonization process. In the carbonization process, wood pellets are heated to 400-700°C in a furnace with little or no oxygen. As a result, the wood pellets are carbonized and the volume increases to 40~
It shrinks to 50% and becomes a charcoal pellet. Note that the carbonization time is very short because finely cut charcoal pellets are carbonized. Moreover, the yield of charcoal pellets to wood pellets was 30 to 45% (weight ratio). This is because moisture and volatile content in the wood pellets are lost, and some of the wood pellets are thermally decomposed. The carbonized pellet has a porous structure with voids formed in areas where volatile substances are lost during carbonization and areas through which volatile substances have passed.

炭化が経った炭化ペレットは、外熱式のロータる。賦活
時間は、10〜30分で吹き込む水蒸気のiは0.5〜
2.5kg(水蒸気) /kg i”木炭ペレット)が
適当であった。この賦活工程によって、炭化ペレットの
多孔構造が更に発達し、小さな空孔から比較的大きな空
孔までの極めて多数の空孔を有する吸着性に富む活性炭
が得られる。
The carbonized pellets that have undergone carbonization are transferred to an external heating rotor. The activation time is 10 to 30 minutes, and the i of the steam blown in is 0.5 to 30 minutes.
2.5 kg (steam)/kg i” charcoal pellet) was suitable. Through this activation process, the porous structure of the carbonized pellet was further developed, and an extremely large number of pores ranging from small pores to relatively large pores were formed. Activated carbon with high adsorption properties can be obtained.

賦活後の活性炭は、不活性雰囲気中で冷却され、次いで
、選別されて粉末状の活性炭が取り除かれ、最終製品と
される(なお、このとき除去される粉末は粉末活性炭と
して使用される)。
The activated carbon is cooled in an inert atmosphere, and then sorted to remove powdered activated carbon to form a final product (the powder removed at this time is used as powdered activated carbon).

なお、炭化工程及び賦活工程において発生するH2及び
COを主成分とするガスは回収し、炭化及び賦活のため
の燃料ガスとして使用する。
Note that the gas mainly composed of H2 and CO generated in the carbonization process and the activation process is recovered and used as a fuel gas for carbonization and activation.

1−記のように、本発明では、原料を炭化させる前に、
木質原料の高温・高圧下における可塑化及び自己粘結性
を利用して木質ペレットを成形し、これを炭化・賦活す
ることにより吸着性に富んだ活性炭を得るようにした。
As described in 1-, in the present invention, before carbonizing the raw material,
Wood pellets are formed using the plasticization and self-caking properties of wood raw materials under high temperature and high pressure, and activated carbon with high adsorption properties is obtained by carbonizing and activating the wood pellets.

従って、従来は成形時に必要であったバインダを使用す
る必要がない。
Therefore, there is no need to use a binder, which was conventionally required during molding.

このため、従来のように脱気不十分及び揮発分の揮発に
よる強度及び密度の低下という不具合、及び有毒ガスの
発生という問題は解消される。このため、十分な機械的
強度及び密度を有する良質な成形活性炭を得ることがで
きる。また、炭化前に成形しであるため、乾燥、成形工
程において原料に着火するおそれが全くなくなる。
Therefore, the conventional problems of insufficient degassing and a decrease in strength and density due to volatilization of volatile matter, and the generation of toxic gases, are eliminated. Therefore, high quality shaped activated carbon having sufficient mechanical strength and density can be obtained. Furthermore, since the material is shaped before carbonization, there is no risk of the raw material igniting during the drying and shaping process.

なお、木材原料としては、製材時の加工廃材、間伐材、
建築廃材等があるが、これらに樹皮を加えても、50%
(乾燥重量%)以下であれば、本発明方法によって木質
ベレットを成形する際に性状が悪化するということはな
く、良質の成形活性炭を得ることができた。
In addition, wood raw materials include processed waste wood from sawmilling, thinned wood,
There are construction waste materials, etc., but even if you add bark to these materials, 50%
(dry weight %) or less, the properties of the wood pellet did not deteriorate when the wood pellet was formed by the method of the present invention, and a high-quality formed activated carbon could be obtained.

以上説明してきたように、本発明によると、原料である
木材を破砕して所定粒度の破砕原料とし、破砕原料を乾
燥させて水分を調整し、水分調整後の破砕原料を高温・
高圧で押出成形し切断して木質ペレットとし、次いで木
質ペレットを加熱し炭化させて炭化ペレットとし、炭化
ペレットを高温水蒸気雰囲気中で賦活して活性炭とする
ので、良質な木質成形活性炭を簡単な製造工程により製
造することができるという効果が得られる。
As explained above, according to the present invention, wood as a raw material is crushed to obtain crushed raw material with a predetermined particle size, the crushed raw material is dried to adjust the moisture content, and the crushed raw material after moisture adjustment is heated at high temperature.
Wood pellets are made by extrusion molding and cutting under high pressure, then the wood pellets are heated and carbonized to make carbonized pellets, and the carbonized pellets are activated in a high-temperature steam atmosphere to make activated carbon, making it easy to produce high-quality wood shaped activated carbon. The advantage is that it can be manufactured through multiple steps.

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

図は本発明による製造工程を示すブロック図である。 特許出願人  株式会社日本製鋼所 代理人  弁理士 宮内利行 The figure is a block diagram showing the manufacturing process according to the present invention. Patent applicant: Japan Steel Works, Ltd. Agent: Patent attorney: Toshiyuki Miyauchi

Claims (1)

【特許請求の範囲】 1、原料である木材を破砕して所定粒度の破砕原料とし
、破砕原料を乾燥させて水分を調整し、水分調整後の破
砕原料を高温−高圧で押出成形し切断して木質ペレット
とし、次いで木質ペレットを加熱し炭化させて炭化ペレ
ットとし、炭化ペレットを高温水蒸気雰囲気中で賦活し
て活性炭とする、木材を原料とする成形活性炭の製造方
法。 2、原料である木材は、50%(乾燥重量%)以下の樹
皮を含む特許請求の範囲第1項記載の木材を原料とする
成形活性炭の製造方法。
[Scope of Claims] 1. The raw material wood is crushed to obtain a crushed raw material with a predetermined particle size, the crushed raw material is dried to adjust the moisture content, and the crushed raw material after moisture adjustment is extruded at high temperature and high pressure and cut. A method for producing shaped activated carbon using wood as a raw material, in which the wood pellets are made into wood pellets, the wood pellets are then heated and carbonized to make carbonized pellets, and the carbonized pellets are activated in a high-temperature steam atmosphere to make activated carbon. 2. A method for producing shaped activated carbon using wood as a raw material according to claim 1, wherein the raw material wood contains 50% (dry weight %) or less of bark.
JP57019721A 1982-02-12 1982-02-12 Manufacture of molded activated carbon using wood as starting material Granted JPS58140311A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57019721A JPS58140311A (en) 1982-02-12 1982-02-12 Manufacture of molded activated carbon using wood as starting material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57019721A JPS58140311A (en) 1982-02-12 1982-02-12 Manufacture of molded activated carbon using wood as starting material

Publications (2)

Publication Number Publication Date
JPS58140311A true JPS58140311A (en) 1983-08-20
JPS611365B2 JPS611365B2 (en) 1986-01-16

Family

ID=12007160

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57019721A Granted JPS58140311A (en) 1982-02-12 1982-02-12 Manufacture of molded activated carbon using wood as starting material

Country Status (1)

Country Link
JP (1) JPS58140311A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004315242A (en) * 2003-04-10 2004-11-11 Tokyo Gas Co Ltd Activated carbon
GB2476819A (en) * 2010-01-11 2011-07-13 Univ Surrey Method for preparing activated charcoal

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004315242A (en) * 2003-04-10 2004-11-11 Tokyo Gas Co Ltd Activated carbon
GB2476819A (en) * 2010-01-11 2011-07-13 Univ Surrey Method for preparing activated charcoal
GB2476819B (en) * 2010-01-11 2014-05-07 Univ Surrey Activated charcoal

Also Published As

Publication number Publication date
JPS611365B2 (en) 1986-01-16

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