JPH10244176A - Operation of roller mill - Google Patents

Operation of roller mill

Info

Publication number
JPH10244176A
JPH10244176A JP5036197A JP5036197A JPH10244176A JP H10244176 A JPH10244176 A JP H10244176A JP 5036197 A JP5036197 A JP 5036197A JP 5036197 A JP5036197 A JP 5036197A JP H10244176 A JPH10244176 A JP H10244176A
Authority
JP
Japan
Prior art keywords
roller mill
crushed
residue
roller
organic waste
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.)
Pending
Application number
JP5036197A
Other languages
Japanese (ja)
Inventor
Kenichi Arima
謙一 有馬
Shinji Matsumoto
慎治 松本
Yutaka Iida
豊 飯田
Shuichi Sakota
秀一 迫田
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries 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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP5036197A priority Critical patent/JPH10244176A/en
Publication of JPH10244176A publication Critical patent/JPH10244176A/en
Pending legal-status Critical Current

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  • Crushing And Grinding (AREA)
  • Disintegrating Or Milling (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a method of operation of a roller with which organic wastes are safely crushed after they are heat treated. SOLUTION: A motor 1 rotates a vertical shaft 2, and a material to be pulverized 28 is fed between a table 3 and a roller 5 and is classified by a separator 6 as a crushed material 29 before feeding to a boiler 9. Organic waste 21 is thrown in a rotary kiln 12 having a jacket 11, and oil 22 and combustion air 23 are fed to the jacket 11, and the organic waste 21 is heated at 200∼500 deg.C in an oxygen shortage state to thermally decompose it into volatile gas 24 and a residue 25. The gas 24 is fed to the boiler, and the residue 25 is fed to a mill through a feeding pipe 4 together with coal 26, if necessary and is crushed. The residue 25 consists essentially of carbon and is fragile and is easily crushed and is also thermally stable and is not ignited.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、都市ゴミ、RDF
(Refuse Derive Fuel;都市ごみを固形燃料化したも
の)、廃プラスチック等を粉砕し、従来の石炭焚火力発
電所で混焼するために用いられ、粉砕物を単独あるいは
石炭と混合粉砕するためのローラミルの運転方法に関す
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to urban refuse, RDF
(Refuse Derive Fuel; solid waste fuel from municipal solid waste), waste plastics, etc. are crushed and used for co-firing in a conventional coal-fired power plant. Roller mill for crushing the crushed material alone or mixed with coal Related to the driving method.

【0002】[0002]

【従来の技術】図3は従来のローラミルの一般的な構成
図である。図において、モータ1により駆動される垂直
軸2により回転するテーブル3上には、上部の供給管4
より被粉砕物8、例えば、石炭が投入され、同テーブル
3上を押圧、転動する複数個のローラ5によりテーブル
3上の被粉砕物8が粉砕される。テーブル3とローラ5
間で粉砕された被粉砕物8はテーブル3の下部から供給
されて周囲より吹上る熱空気7により乾燥、搬送され、
セパレータ6を通過することにより分級され、所定の粒
度の被粉砕物はボイラ9へ搬送され、粗粒は再度テーブ
ル3上に落下し、再粉砕される。
2. Description of the Related Art FIG. 3 is a general configuration diagram of a conventional roller mill. In the figure, an upper supply pipe 4 is provided on a table 3 rotated by a vertical shaft 2 driven by a motor 1.
The crushed object 8, for example, coal is charged, and the crushed object 8 on the table 3 is crushed by a plurality of rollers 5 that press and roll on the table 3. Table 3 and roller 5
The pulverized material 8 pulverized in between is dried and conveyed by hot air 7 supplied from the lower part of the table 3 and blowing up from the surroundings.
The material to be crushed having a predetermined particle size is conveyed to the boiler 9 by passing through the separator 6, and the coarse particles fall again on the table 3 and are crushed again.

【0003】上記に説明した従来の一般的なローラミル
では石炭や鉱石以外で軟らかく、粉砕されにくい有機系
廃棄物の粉砕は不可能であった。なお、ローラミル以外
による粉砕では、プラスチック等に対して液体窒素を用
いた冷凍粉砕が行なわれているが、特殊な粉砕方法であ
り、コストが高く、かつ大規模な粉砕には向かないのが
現状である。
The conventional general roller mill described above cannot pulverize organic wastes which are soft and hard to pulverize except for coal and ore. In addition, in the case of pulverization by means other than a roller mill, frozen pulverization using liquid nitrogen is performed on plastics and the like, but it is a special pulverization method, which is expensive and not suitable for large-scale pulverization. It is.

【0004】[0004]

【発明が解決しようとする課題】前述の従来のローラミ
ルで有機系廃棄物を粉砕しようとすると次のような問題
があった。
However, there are the following problems when pulverizing organic waste with the above-mentioned conventional roller mill.

【0005】(1)ローラミルの粉砕メカニズムは圧
縮、せん断であるが、プラスチックのような軟らかく延
性のある材料では偏平化されるだけであり、せん断がな
されないためローラミルから排出されず、内部に蓄積
し、最終的にはミルの運転が不能となる。
(1) The crushing mechanism of the roller mill is compression and shearing. However, soft and ductile materials such as plastics are only flattened, and are not discharged from the roller mill because they are not sheared, and are accumulated inside. Eventually, the operation of the mill becomes impossible.

【0006】(2)特に、石炭と混合して粉砕する場
合、200℃程度の熱空気が使用されるが、有機系廃棄
物の発火温度が低い場合にはミル内で発火し、火炎が発
生する恐れがある。
(2) In particular, when mixed with coal and pulverized, hot air of about 200 ° C. is used. However, when the ignition temperature of organic waste is low, it is ignited in a mill and a flame is generated. Might be.

【0007】本発明は、上記の(1),(2)の問題を
解決するために、有機系廃棄物の粉砕を可能とし、かつ
ミル内部で着火することがなく石炭等と混合もでき、安
全な運転を可能とするローラミルの運転方法を提供する
ことを課題としている。
According to the present invention, in order to solve the above problems (1) and (2), it is possible to pulverize organic waste and mix with coal and the like without igniting inside the mill. An object of the present invention is to provide a roller mill operation method that enables safe operation.

【0008】[0008]

【課題を解決するための手段】そのため、本発明は、モ
ータにより鉛直な垂直軸まわりに回転するテーブルと、
同テーブル上を押圧しつつ転動する複数個のローラとを
備え、同ローラと同テーブルとの間で被粉砕物を粉砕す
るローラミルの運転方法において、前記被粉砕物として
粉砕されにくい軟らかい有機系廃棄物を予め酸素不足雰
囲気で200〜500℃の温度範囲で加熱処理し、その
後ローラミル内の前記テーブル上に投入し、粉砕するこ
とを特徴とするローラミルの運転方法を提供する。
SUMMARY OF THE INVENTION Accordingly, the present invention provides a table rotated by a motor about a vertical axis.
A plurality of rollers that roll while pressing on the same table, and a method of operating a roller mill that crushes an object to be crushed between the roller and the table, wherein a soft organic material that is hard to be crushed as the object to be crushed. A method for operating a roller mill, comprising: subjecting a waste to heat treatment in advance in an oxygen-deficient atmosphere in a temperature range of 200 to 500 ° C., and thereafter throwing the waste on the table in a roller mill and pulverizing the waste.

【0009】本発明のローラミルの運転方法では、有機
系廃棄物、例えばプラスチック等を酸素のない雰囲気で
加熱することにより、次の(1)又は(2)式で示すよ
うな熱分解が起る。
In the method for operating a roller mill of the present invention, by heating an organic waste such as a plastic in an oxygen-free atmosphere, thermal decomposition as shown in the following equation (1) or (2) occurs. .

【0010】[0010]

【化1】 Embedded image

【0011】上記の(1),(2)式におけるCα’H
α’は低分子炭化水素であり、CO,H2 O等と共に気
体、即ち揮発性ガスとなって有機系廃棄物から放出さ
れ、有機系廃棄物は炭素Cを主成分とする残渣となる。
炭素を主成分とする残渣はローラミルにおいて脆くて容
易に粉砕されると共に、熱的にも安定で発火することも
ない。
Cα′H in the above equations (1) and (2)
α ′ is a low molecular hydrocarbon, which is released from the organic waste as a gas, that is, a volatile gas together with CO, H 2 O, etc., and the organic waste becomes a residue mainly composed of carbon C.
The residue mainly composed of carbon is brittle and easily pulverized in a roller mill, and is thermally stable and does not ignite.

【0012】上記のローラミルの運転方法を図1に示す
本発明のローラミルの基本構成図により説明すると、有
機系廃棄物Aは、例えば、加熱装置Bに投入され、ここ
で酸素不足雰囲気で加熱され、前述のように揮発性ガス
と残渣に熱分解される。揮発性ガスは、例えば、そのま
まボイラ等へ送り、燃焼に利用可能であり、残渣は炭素
を主成分として容易に粉砕されるのでローラミルDに投
入され、被粉砕物D−4となってテーブルD−3上に投
入される。投入された残渣、即ち被粉砕物D−4はモー
タD−1と垂直軸D−2によって回転するテーブルD−
3とローラD−5との間で粉砕され、下方からの熱風に
よりボイラに供給される。この際、残渣は、必要に応じ
て石炭Cと混合してローラミルDへ投入することもでき
る。
The operation method of the above roller mill will be described with reference to the basic configuration diagram of the roller mill of the present invention shown in FIG. 1. The organic waste A is put into, for example, a heating device B, where it is heated in an oxygen-deficient atmosphere. Is thermally decomposed into volatile gases and residues as described above. The volatile gas is sent, for example, to a boiler or the like as it is, and can be used for combustion. Since the residue is easily pulverized with carbon as a main component, it is put into a roller mill D, and becomes a material D-4 to be pulverized. -3. The loaded residue, that is, the material to be ground D-4 is rotated by a motor D-1 and a vertical axis D-2.
Crushed between the roller 3 and the roller D-5, and supplied to the boiler by hot air from below. At this time, the residue can be mixed with coal C and fed to roller mill D as needed.

【0013】[0013]

【発明の実施の形態】以下、本発明の実施の形態につい
て図面に基づいて具体的に説明する。図1は本発明の基
本構成を示す図であり、前述の手段の欄で説明したもの
であり、説明は省略する。図2は本発明の実施の一形態
に係るローラミルの運転方法を実施する装置の構成図で
あり、前述の図1に示す本発明の基本構成を具体化した
ものである。以下、本発明の実施の一形態について図2
により説明する。
Embodiments of the present invention will be specifically described below with reference to the drawings. FIG. 1 is a diagram showing a basic configuration of the present invention, which has been described in the section of the above-mentioned means, and a description thereof will be omitted. FIG. 2 is a configuration diagram of an apparatus for performing the roller mill operation method according to one embodiment of the present invention, and embodies the basic configuration of the present invention shown in FIG. 1 described above. FIG. 2 shows an embodiment of the present invention.
This will be described below.

【0014】図2において、ローラミル10はモータ1
により、駆動される垂直軸2まわりに回転するテーブル
3と、被粉砕物28を供給する供給管4、テーブル3上
を押圧しつつ、転動する複数個のローラ5、上部のセパ
レータ6を備えている。
In FIG. 2, a roller mill 10 is a motor 1
A table 3 that rotates around the driven vertical axis 2, a supply pipe 4 that supplies the material to be ground 28, a plurality of rollers 5 that roll while pressing on the table 3, and an upper separator 6. ing.

【0015】更に、ローラミル10からの粉砕物が送ら
れ、燃焼に供するボイラ9、有機系廃棄物21を加熱
し、揮発性ガス24と残渣25に分解するジャケット1
1を有するロータリキルン12を備えている。
Further, the pulverized material from the roller mill 10 is sent to the boiler 9 for combustion, the organic waste 21 is heated, and the jacket 1 is decomposed into volatile gas 24 and residue 25.
1 is provided with a rotary kiln 12.

【0016】上記の装置構成において、その運転方法を
説明する。まず、供給管4より投入された被粉砕物28
はテーブル3とローラ5との間に押圧され、粉砕されて
粉砕された被粉砕物29となり、テーブル3の下部から
供給されてテーブル3の周囲から吹き上がる熱空気27
により乾燥、搬送され、上部のセパレータ6を通過し、
分級されてボイラ9へ供給される。セパレータ6で分級
されたもののうち、粗粒は再びテーブル3上に落下し、
再粉砕される。
An operation method of the above-described apparatus configuration will be described. First, the crushed material 28 supplied from the supply pipe 4
Is pressed between the table 3 and the roller 5 to be pulverized into a pulverized object 29, which is supplied from a lower portion of the table 3 and blows up from the periphery of the table 3.
Is dried and conveyed, passes through the upper separator 6,
Classified and supplied to the boiler 9. Among the materials classified by the separator 6, coarse particles fall again on the table 3,
Re-crushed.

【0017】本実施の形態の運転方法においては、有機
系廃棄物21、例えば、プラスチック等はジャケット1
1を有するロータリキルン12に投入され、内部で20
0℃〜500℃の温度範囲で30分以上加熱されるが、
本例では300℃で約1時間加熱する。
In the operation method according to the present embodiment, the organic waste 21, for example, plastic,
1 into a rotary kiln 12 and internally 20
It is heated for 30 minutes or more in the temperature range of 0 ° C to 500 ° C,
In this example, heating is performed at 300 ° C. for about 1 hour.

【0018】即ち、ジャケット11には油22と燃焼用
空気23が供給され、油22と燃焼用空気23を燃焼さ
せ、有機系廃棄物21を加熱する。有機系廃棄物21は
内部で酸素不足状態で加熱され、熱分解して低分子炭化
水素を主成分とする揮発性ガス24と炭素を主成分とす
る残渣25とに分離する。
That is, oil 22 and combustion air 23 are supplied to the jacket 11, and the oil 22 and combustion air 23 are burned to heat the organic waste 21. The organic waste 21 is heated in an oxygen-deficient state inside and is thermally decomposed to separate into a volatile gas 24 mainly composed of low molecular hydrocarbons and a residue 25 mainly composed of carbon.

【0019】発生した揮発性ガス24はCO,H2 Oな
どと共にボイラ9に供給され、燃焼に供され、残渣25
は炭素を主成分として必要に応じて石炭26と共に供給
管4からローラミル10に投入され、ローラミル10に
より前述の如く微粉砕された後、ボイラ9へ供給され
る。
The generated volatile gas 24 is supplied to the boiler 9 together with CO, H 2 O, etc., and is subjected to combustion, and the residue 25
Is fed into the roller mill 10 from the supply pipe 4 together with the coal 26 as necessary, and is supplied to the boiler 9 after being finely pulverized by the roller mill 10 as described above.

【0020】上記説明の実施の形態によるローラミルの
運転方法によれば、有機系廃棄物21をロータリキルン
12で酸素不足雰囲気で加熱し、熱分解により揮発性ガ
ス24と残渣25に分解し、揮発性ガス24はそのまま
ボイラ9へ、残渣25は炭素を主成分として脆くて容易
にローラミル10で粉砕され、熱的にも安定で300℃
程度で発火することもなく安全にローラミル10で粉砕
することができる。
According to the operation method of the roller mill according to the above-described embodiment, the organic waste 21 is heated in the oxygen-deficient atmosphere by the rotary kiln 12 and decomposed into volatile gas 24 and residue 25 by thermal decomposition. The neutral gas 24 is directly sent to the boiler 9, and the residue 25 is easily crushed by the roller mill 10 because it is brittle, mainly composed of carbon, and is thermally stable and 300 ° C.
It is possible to safely pulverize with the roller mill 10 without causing any ignition.

【0021】[0021]

【発明の効果】以上、具体的に説明したように、本発明
のローラミルの運転方法は、モータにより鉛直な垂直軸
まわりに回転するテーブルと、同テーブル上を押圧しつ
つ転動する複数個のローラとを備え、同ローラと同テー
ブルとの間で被粉砕物を粉砕するローラミルの運転方法
において、前記被粉砕物として粉砕されにくい軟らかい
有機系廃棄物を予め酸素不足雰囲気で200〜500℃
の温度範囲で加熱処理し、その後ローラミル内の前記テ
ーブル上に投入し、粉砕することを特徴としているの
で、有機系廃棄物は熱分解により揮発性ガスと残渣に分
離され、揮発性ガスはそのままボイラ等へ供給されるこ
とができ、残渣は炭素を主成分として脆くて容易に粉砕
することができる。よって、ローラミルにおいてこの残
渣を容易に粉砕し、ボイラ等に供給でき、この残渣は
又、熱的にも安定で発火する恐れもないので有機系廃棄
物をローラミルで安全に粉砕することが可能となった。
As described above, the method for operating the roller mill according to the present invention comprises a table rotating around a vertical axis by a motor, and a plurality of rollers rolling while pressing on the table. A roller mill operating method for crushing an object to be crushed between the roller and the table, comprising: a soft organic waste which is hard to be crushed as the object to be crushed;
Heat treatment in the temperature range of, and then thrown on the table in the roller mill and pulverized, so that organic waste is separated into volatile gas and residue by thermal decomposition, and the volatile gas remains as it is. The residue can be supplied to a boiler or the like, and the residue is brittle with carbon as a main component and can be easily pulverized. Therefore, this residue can be easily pulverized in a roller mill and supplied to a boiler or the like, and since this residue is also thermally stable and has no risk of ignition, it is possible to safely pulverize organic waste with a roller mill. became.

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

【図1】本発明のローラミルの運転方法を適用する装置
の構成図である。
FIG. 1 is a configuration diagram of an apparatus to which a method for operating a roller mill according to the present invention is applied.

【図2】本発明の実施の一形態に係るローラミルの運転
方法を適用する装置の構成図である。
FIG. 2 is a configuration diagram of an apparatus to which a method for operating a roller mill according to an embodiment of the present invention is applied.

【図3】従来のローラミルの構成図である。FIG. 3 is a configuration diagram of a conventional roller mill.

【符号の説明】[Explanation of symbols]

1 モータ 2 垂直軸 3 テーブル 4 供給管 5 ローラ 6 セパレータ 9 ボイラ 10 ローラミル 11 ジャケット 12 ロータリキルン 21 有機系廃棄物 22 油 23 燃焼用空気 24 揮発性ガス 25 残渣 26 石炭 27 熱空気 28 被粉砕物 DESCRIPTION OF SYMBOLS 1 Motor 2 Vertical axis 3 Table 4 Supply pipe 5 Roller 6 Separator 9 Boiler 10 Roller mill 11 Jacket 12 Rotary kiln 21 Organic waste 22 Oil 23 Combustion air 24 Volatile gas 25 Residue 26 Coal 27 Hot air 28 Pulverized material

───────────────────────────────────────────────────── フロントページの続き (72)発明者 迫田 秀一 長崎市飽の浦町1番1号 三菱重工業株式 会社長崎造船所内 ──────────────────────────────────────────────────続 き Continuing from the front page (72) Inventor Shuichi Sakota 1-1, Akunouramachi, Nagasaki City Inside Nagasaki Shipyard, Mitsubishi Heavy Industries, Ltd.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 モータにより鉛直な垂直軸まわりに回転
するテーブルと、同テーブル上を押圧しつつ転動する複
数個のローラとを備え、同ローラと同テーブルとの間で
被粉砕物を粉砕するローラミルの運転方法において、前
記被粉砕物として粉砕されにくい軟らかい有機系廃棄物
を予め酸素不足雰囲気で200〜500℃の温度範囲で
加熱処理し、その後ローラミル内の前記テーブル上に投
入し、粉砕することを特徴とするローラミルの運転方
法。
1. A table which rotates around a vertical axis by a motor, and a plurality of rollers which roll while pressing on the table, and crush the object to be crushed between the rollers and the table. In the operation method of the roller mill, the soft organic waste that is hard to be pulverized as the object to be pulverized is heat-treated in advance in an oxygen-deficient atmosphere at a temperature in the range of 200 to 500 ° C., and then put on the table in the roller mill and pulverized. A method for operating a roller mill.
JP5036197A 1997-03-05 1997-03-05 Operation of roller mill Pending JPH10244176A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5036197A JPH10244176A (en) 1997-03-05 1997-03-05 Operation of roller mill

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5036197A JPH10244176A (en) 1997-03-05 1997-03-05 Operation of roller mill

Publications (1)

Publication Number Publication Date
JPH10244176A true JPH10244176A (en) 1998-09-14

Family

ID=12856762

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5036197A Pending JPH10244176A (en) 1997-03-05 1997-03-05 Operation of roller mill

Country Status (1)

Country Link
JP (1) JPH10244176A (en)

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JP2007091892A (en) * 2005-09-29 2007-04-12 Ube Machinery Corporation Ltd Manufacturing system of boiler fuel from ligneous biomass
CN102512077A (en) * 2011-12-24 2012-06-27 向安奎 Electric heating lapping machine
WO2014168004A1 (en) * 2013-04-10 2014-10-16 三菱重工環境・化学エンジニアリング株式会社 Biomass pyrolysis apparatus, and power generation system

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JP2007091894A (en) * 2005-09-29 2007-04-12 Ube Machinery Corporation Ltd Production system for woody biomass fuel
JP2007091891A (en) * 2005-09-29 2007-04-12 Ube Machinery Corporation Ltd Manufacturing system of boiler fuel
JP2007091893A (en) * 2005-09-29 2007-04-12 Ube Machinery Corporation Ltd Feeding system of ligneous biomass fuel
JP2007091889A (en) * 2005-09-29 2007-04-12 Ube Machinery Corporation Ltd Manufacturing system of biomass fuel
JP2007091888A (en) * 2005-09-29 2007-04-12 Ube Machinery Corporation Ltd Method for crushing woody biomass
JP2007091892A (en) * 2005-09-29 2007-04-12 Ube Machinery Corporation Ltd Manufacturing system of boiler fuel from ligneous biomass
CN102512077A (en) * 2011-12-24 2012-06-27 向安奎 Electric heating lapping machine
WO2014168004A1 (en) * 2013-04-10 2014-10-16 三菱重工環境・化学エンジニアリング株式会社 Biomass pyrolysis apparatus, and power generation system
JP2014205730A (en) * 2013-04-10 2014-10-30 三菱重工環境・化学エンジニアリング株式会社 Biomass thermal decomposition device and power generating system
CN105026836A (en) * 2013-04-10 2015-11-04 三菱重工环境·化学工程株式会社 Biomass pyrolysis apparatus, and power generation system
AU2014251842B2 (en) * 2013-04-10 2017-02-09 Mitsubishi Heavy Industries Environmental & Chemical Engineering Co., Ltd. Biomass pyrolysis apparatus, and power generation system
US10184082B2 (en) 2013-04-10 2019-01-22 Mitsubishi Heavy Industries Environmental & Chemical Engineering Co., Ltd. Biomass pyrolysis apparatus, and power generation system

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