JPH0418938A - Operating method for vertical type roller mill - Google Patents

Operating method for vertical type roller mill

Info

Publication number
JPH0418938A
JPH0418938A JP11972690A JP11972690A JPH0418938A JP H0418938 A JPH0418938 A JP H0418938A JP 11972690 A JP11972690 A JP 11972690A JP 11972690 A JP11972690 A JP 11972690A JP H0418938 A JPH0418938 A JP H0418938A
Authority
JP
Japan
Prior art keywords
stone
ejected
mill
raw material
amount
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
JP11972690A
Other languages
Japanese (ja)
Other versions
JPH074549B2 (en
Inventor
Takuya Takayama
卓也 高山
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.)
Ube Corp
Original Assignee
Ube 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 Ube Industries Ltd filed Critical Ube Industries Ltd
Priority to JP11972690A priority Critical patent/JPH074549B2/en
Publication of JPH0418938A publication Critical patent/JPH0418938A/en
Publication of JPH074549B2 publication Critical patent/JPH074549B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Crushing And Grinding (AREA)

Abstract

PURPOSE:To minimize deterioration of grinding capacity by adding water to ejected stone at the specified rate to perform humidity conditioning while ejected stone is discharged from a mill and joined to a freshly supplied raw material and properly controlling the circulating amount of ejected stone in accordance with the change in grindability of a raw material to be ground. CONSTITUTION:In the vertical type roller mills 4, 5 having an external circulation system of ejected stone, while ejected stone 7 is discharged from the mills and joined to a freshly supplied raw material 1, this ejected stone 7 is measured by a weighing equipment 15. Thereafter water is added to ejected stone in an amount of 1-5% by weight based on ejected stone 7 with a water adding device 17 and humidity conditioning is performed. As a result, the circulating amount of ejected stone is properly controlled in accordance with the change in grindability of the raw material and deterioration of grinding capacity of the mills. Thereby deterioration of grinding capacity can be minimized.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、回転する粉砕テーブルと粉砕ローラとの協動
によりセメント原料、高炉スラグ、石炭化学品などを粉
砕する排石外部循環方式を採用した竪型ローラミルの運
転方法に関するものである。
[Detailed Description of the Invention] [Industrial Application Field] The present invention employs an external rock circulation system for pulverizing cement raw materials, blast furnace slag, coal chemicals, etc. through cooperation between a rotating pulverizing table and pulverizing rollers. The present invention relates to a method of operating a vertical roller mill.

[従来の技術] 第3図は、粉砕テーブル4および粉砕ローラ5を備えた
排石外部循環方式を採用した従来の竪型ローラミルの概
略図で、セメント原料や石炭の粉砕用ミルとして、広く
用いられている。
[Prior Art] Figure 3 is a schematic diagram of a conventional vertical roller mill that employs an external rock circulation system and is equipped with a crushing table 4 and crushing rollers 5, and is widely used as a mill for crushing raw materials for cement and coal. It is being

ミルに供給される原?!41は、被粉砕物供給管2を通
じて、円筒あるいは円錐台状のミルケーシング下部に設
置された減速機を介在した駆動モータ3によって回転す
る円盤状の粉砕テーブル4の中央部に投入され、遠心力
により粉砕テーブル4と、この粉砕テーブル4上面外周
部を円周方向に等分する箇所に油圧式やバネ式の粉砕ロ
ーラ圧接装置(図示せず)によって圧接されて従動回転
する複数個の粉砕ローラ5との間に噛み込まれ粉砕され
る。粉砕された粉砕物は粉砕テーブル4の外周部下方か
らミル内に吹き込まれる熱ガス流6によって乾燥および
分級作用を受け、粒径の粗い粗粒子と比較的細かな粒子
とに分けられる。粗粒子は熱ガス流6に逆らって乾燥し
ながら落下し排石7としてミルから排出された後、輸送
装置14により運ばれ、供給原料1と一緒になって再度
被粉砕物として粉砕テーブル4上に投入される。
Raw material supplied to the mill? ! The material to be crushed 41 is fed through the supply pipe 2 to the center of a disk-shaped crushing table 4 that is rotated by a drive motor 3 with a reducer installed at the bottom of a cylindrical or truncated conical mill casing. A crushing table 4 and a plurality of crushing rollers that are pressed into contact with a hydraulic or spring-type crushing roller pressure device (not shown) and driven to rotate at positions that equally divide the outer circumference of the upper surface of the crushing table 4 in the circumferential direction. 5 and is crushed. The pulverized material is dried and classified by a hot gas flow 6 blown into the mill from below the outer periphery of the pulverizing table 4, and is separated into coarse particles with a coarse particle size and relatively fine particles. The coarse particles fall while drying against the hot gas flow 6 and are discharged from the mill as waste stones 7. After that, they are transported by a transport device 14, and together with the feed material 1, they are placed on the grinding table 4 again as a material to be ground. will be put into the

一方、比較的細かな粒子はガス流と共に粉砕テーブル4
上方に位置し垂直軸回りに回転する分組機8へと運ばれ
、ここで2回めの分級作用を受ける。分級機8を通過し
た微粒子は下流に設置されたバッグフィルタ9で製品l
Oとして補集され、分級機8を通過できずに分離された
粒子は、ミル下部へと落下し、粉砕されるべく再び粉砕
テーブル4上に導かれる。
On the other hand, relatively fine particles are removed from the grinding table 4 along with the gas flow.
It is transported to a sorting machine 8 located above and rotating around a vertical axis, where it undergoes a second sorting action. The fine particles that have passed through the classifier 8 are processed into a bag filter 9 installed downstream to produce a product.
Particles that are collected as O and separated without passing through the classifier 8 fall to the lower part of the mill and are guided onto the grinding table 4 again to be crushed.

ここで、排石外部循環方式について若干補足するが、こ
れは、前述の粉砕テーブル4の周囲がら落下する粉砕物
をテーブル周囲から吹上げる熱ガス流6によって再度粉
砕テーブル4上に戻す代わりに一旦、ミル外へ排出させ
た後、機械式の輸送装置14によってミル上方へ運搬し
て粉砕テーブル4上へ再度投入し、これによって、ミル
を通過するガス量を減少させ排気ファン24の動力を低
減しようとするものである。
Here, I would like to add a little bit about the external stone circulation system, which is that instead of returning the pulverized materials that fall from around the pulverizing table 4 onto the pulverizing table 4 again using the hot gas flow 6 blown up from around the table, , after being discharged outside the mill, it is transported to the upper part of the mill by a mechanical transport device 14 and placed on the grinding table 4 again, thereby reducing the amount of gas passing through the mill and reducing the power of the exhaust fan 24. This is what I am trying to do.

[発明が解決しようとする課題] 従来の排石外部循環方式を採用した竪型ローラミルには
、次のような問題点がある。
[Problems to be Solved by the Invention] Vertical roller mills that employ the conventional external rock circulation system have the following problems.

すなわち、排石外部循環方式の竪型ローラミルの場合、
ミルに供給される原料の被粉砕性が悪くなったり、ミル
の長時間の運転によって粉砕デープル4や粉砕ローラ5
の摩耗が進行して粉砕能力が低下すると、被粉砕物の粉
砕が行われにくくなって、排石7の循環量が増大しミル
の運転が困難となる場合がある。
In other words, in the case of a vertical roller mill with external rock circulation system,
The grindability of the raw material supplied to the mill may deteriorate, or the grinding lap 4 or the grinding roller 5 may become damaged due to long-term operation of the mill.
As wear progresses and the crushing capacity decreases, it becomes difficult to crush the material to be crushed, and the amount of circulating waste stones 7 increases, making it difficult to operate the mill.

また、特に乾燥した粉状の排石が増大すると竪型ローラ
ミルは大きな振動を発生してミルの運転を不可能にする
場合もある。
In addition, when the amount of dry powdery waste stone increases, the vertical roller mill may generate large vibrations that may make the mill unable to operate.

この場合、原料の供給量を少くする方向で運転調整を行
うことになるが、そういった運転方法では、所要量の製
品を得るまでの時間が長くなるといった時間の損失、ま
た、電力の損失等を招きコストアップの原因となる。
In this case, operational adjustments will be made to reduce the amount of raw material supplied, but such an operating method will result in time losses such as longer time required to obtain the required amount of product, as well as power losses. This causes an increase in the cost of invitation.

本発明の目的は、原料の被粉砕性の変化やミルの粉砕能
力の低下に対して、排石の循環量を適度にコントロール
し、粉砕能力の低下を極力抑λる方法を提供することに
ある。
The purpose of the present invention is to provide a method for appropriately controlling the circulation amount of waste stone and suppressing the decrease in the crushing capacity as much as possible in response to changes in the pulverizability of raw materials and decreases in the crushing capacity of the mill. be.

[課題を解決するための手1’U] 前記のような問題点を解決するために、排石がミル外部
を輸送装置を通って循環する間に、計量された排石の重
量に対して1%以上5%以下の範囲で水を加λτ調湿し
、輸送の途中で混合され。
[Measures for solving the problem 1'U] In order to solve the above-mentioned problems, while the waste rock circulates outside the mill through the transport device, the weight of the waste rock that is weighed is Water is humidified and adjusted to a range of 1% to 5%, and mixed during transportation.

新しい供給原料と一緒に被粉砕物として粉砕テーブル上
に投入するものである。
It is placed on the grinding table as a material to be ground together with new raw materials.

し作用] 前記のように排石は、既に粉砕テーブルと粉砕ローラに
よって1回以上粉砕作用を受けているものの、製品とし
てミル系外へ取出すことのできないような粉砕されにく
いものを含んでおり、また、サイズ的にも小さくなって
いるので、ミルに再度投入された場合に、粉砕テーブル
上に落ちずに熱ガス流に乗って田土がることもあるため
、再度粉砕テーブルと粉砕ローラの間に噛み込まれにく
い状態にある。
As mentioned above, the waste rock contains hard-to-pulverize materials that cannot be taken out of the mill system as a product, although they have already been subjected to the crushing action at least once by the crushing table and the crushing rollers. In addition, since the size is smaller, if the rice is fed into the mill again, it may not fall onto the grinding table and may get carried away by the hot gas flow, so it is difficult to prevent it from falling between the grinding table and the grinding rollers again. It is in a state where it is difficult to get caught.

そこで、排石に湿分を与λることによって、粉砕テーブ
ル上に再度供給された場合にも、確実に粉砕テーブルと
粉砕ローラの間に噛み込まれるようになり長期に亙って
竪型ローラミルの粉砕能力を変えることなく効率的な運
転が可能となる。
Therefore, by adding moisture to the waste stones, even if they are fed onto the grinding table again, they will be reliably caught between the grinding table and the grinding rollers, and this has led to the use of vertical roller mills for a long time. Efficient operation is possible without changing the crushing capacity of the machine.

なお、排石に加える水の量に1〜5%と幅があるのは、
水の量が1%より少い場合は、排石が粉砕テーブルと粉
砕ローラの間へ噛み込まれにくく、本発明によるところ
の効果が少くなり、また、5%を越えると乾燥費が重ん
で、コストアップの要因となるためミルに供給する原料
の性状や排石の性状によって水の量を変化させ、ミルの
所要動力や製品の乾燥度合のコントロールを行いやすく
するために設けた範囲である。
Furthermore, the amount of water added to the waste rock varies from 1 to 5%.
If the amount of water is less than 1%, it is difficult for the waste stones to be caught between the crushing table and the crushing rollers, and the effect of the present invention will be reduced, and if it exceeds 5%, the drying cost will increase. This range was created to make it easier to control the power required for the mill and the degree of dryness of the product by changing the amount of water depending on the properties of the raw materials supplied to the mill and the properties of the waste rock, which can increase costs. .

[実施例] 第1図は、本発明の実施例を示す概略図である。[Example] FIG. 1 is a schematic diagram showing an embodiment of the present invention.

ミルに供給される原料1は、被粉砕物供給室2を通じて
、円筒あるいは円錐台状のミルケーシング下部に設置さ
れた減速機を介在した駆動モータ3によって回転する円
盤状の粉砕テーブル4の中央部に投入され、遠心力によ
り粉砕テーブル4と、この粉砕テーブル4上面外周部を
円周方向に等分する箇所に油圧式やバネ式の粉砕ローラ
圧接装置(図示せず)によって圧接されて従動回転する
複数個の粉砕ローラ5との間に噛み込まれ粉砕される。
The raw material 1 to be supplied to the mill is passed through a material supply chamber 2 to the center of a disk-shaped grinding table 4 which is rotated by a drive motor 3 with a speed reducer installed at the bottom of a cylindrical or truncated conical mill casing. It is pressed against the grinding table 4 by centrifugal force and a hydraulic or spring-type grinding roller pressing device (not shown) that equally divides the outer periphery of the top surface of this grinding table 4 in the circumferential direction, resulting in driven rotation. It is caught between the plurality of crushing rollers 5 and crushed.

粉砕された粉砕物は粉砕テーブル4の外周部下方からミ
ル内に吹き込まれる熱ガス流6によって乾燥および分級
作用を受け、粒径の粗い粗粒子と比較的細かな粒子とに
分けられ、比較的細かな粒子はガス流と共に粉砕テーブ
ル4上方に位置し垂直軸回りに回転する分級機8へと運
ばれ、ここで2回めの分級作用を受ける。分級機8を通
過した微粒子は下流に設置された排気ファン24に吸引
されたバッグフィルタ9で製品10として捕集され、分
級機8を通過できずに分離された粒子はミル下部へと落
下し、粉砕されるべく再び粉砕テーブル4上に導かれる
The pulverized material is dried and classified by a hot gas flow 6 blown into the mill from below the outer periphery of the pulverizing table 4, and is separated into coarse particles with a coarse particle size and relatively fine particles. The fine particles are carried along with the gas flow to a classifier 8 located above the crushing table 4 and rotating around a vertical axis, where they are subjected to a second classification action. The fine particles that have passed through the classifier 8 are collected as products 10 by the bag filter 9, which is sucked into the exhaust fan 24 installed downstream, and the particles that cannot pass through the classifier 8 and are separated fall to the bottom of the mill. , and is guided onto the grinding table 4 again to be ground.

方、粗粒子は熱ガス流6に逆らって乾燥しながら落下し
排石7としてミルから排出され、排石用の計量装置15
で計量された後、所定の量の水が水添加装置17によっ
て添加され、排石輸送装置14を経由して、供給原料1
と共に粉砕テーブル上に投入される。
On the other hand, the coarse particles fall while drying against the hot gas flow 6 and are discharged from the mill as waste stones 7, and are transferred to a weighing device 15 for waste stones.
After being metered in, a predetermined amount of water is added by a water addition device 17 and sent to the feedstock 1 via a waste rock transport device 14.
It is also placed on the crushing table.

なおこの場合、排石計量装置15と水添加装置17の位
置関係は前後してもかまわないが、水添加装置17の位
置は、排石が供給原料と合流する以前に、排石がほぼ均
質に湿ることのできる位置に設定することが望ましい。
In this case, the positional relationship between the waste rock measuring device 15 and the water addition device 17 may be different, but the position of the water addition device 17 is such that the waste rock is almost homogeneous before the waste rock is combined with the feed material. It is desirable to set it in a position where it can get wet.

また、水の添加量については、原料供給量、排石の量お
よびミルの所要電力、製品の乾燥状態を考廖し、排石の
重態に対して1〜5%の範囲で加えられることが望まし
5い。
In addition, the amount of water added should be in the range of 1 to 5% based on the critical condition of the waste rock, taking into consideration the amount of raw materials supplied, the amount of waste rock, the power required for the mill, and the drying condition of the product. Desirable 5.

第2図は、本発明の他の実施例を示す概略図である。FIG. 2 is a schematic diagram showing another embodiment of the invention.

作用等については、第1図と同様であるので説明を省略
するが、本発明を実施するに当り、さらに効果を高める
ため、水添加量を自動的に設定するためのシステムとし
たものである。
The operation etc. are the same as those shown in Fig. 1, so the explanation is omitted, but in order to further enhance the effect when carrying out the present invention, this system is designed to automatically set the amount of water added. .

原料供給装置12には、原料計量装置13が、水添加装
置17には、水添加量制御装置18が設置されている。
A raw material measuring device 13 is installed in the raw material supply device 12, and a water addition amount control device 18 is installed in the water addition device 17.

原料計量装置13の供給量の信号は、フィルタ19を通
り、不必要な周波数成分が除去され、コントローラ23
に送られる。
The supply amount signal from the raw material measuring device 13 passes through a filter 19, unnecessary frequency components are removed, and the signal is sent to the controller 23.
sent to.

同様に、排石計量装置15の排石量の信号、駆動モータ
電力計16の電力の信号、水添加量制御装置18からの
水添加量の信号も、それぞれフィルタ20〜22を通り
、コントローラ23へ送られる。
Similarly, the signal of the amount of waste rock from the waste rock measuring device 15, the power signal of the drive motor wattmeter 16, and the signal of the amount of water added from the water addition amount control device 18 also pass through filters 20 to 22, and are sent to the controller 23. sent to.

これらの信号をもとに、あらかじめ定められた計算式に
より、水の添加量が計算され、この計算値にしたがって
水添加量制御装置18が水添加Iを自動的に制御する。
Based on these signals, the amount of water added is calculated using a predetermined calculation formula, and the water addition amount control device 18 automatically controls water addition I according to this calculated value.

[発明の効果] 以−ト述べたように、本発明には排石外部循環方式を採
用した竪型ローラミルにおいて次のような著しい効果が
ある。
[Effects of the Invention] As described above, the present invention has the following remarkable effects in a vertical roller mill that employs the external rock circulation system.

(1)ミル内に供給される原料が非常に堅く粉砕されに
くいような原料であっても、排石循環量を増加させるこ
となく粉砕を行うことが可能となる。
(1) Even if the raw material supplied into the mill is very hard and difficult to crush, it can be crushed without increasing the amount of waste stone circulating.

(2)ミルの長時間の運転によって、粉砕テーブルや粉
砕ローラが摩耗し、粉砕能力が低下している場合におい
ても、排石循環量を適度にコントロールして、粉砕能力
の低下を極力小さくすることが可能となる。
(2) Even if the grinding table and grinding rollers are worn out due to long-term operation of the mill and the grinding capacity is reduced, the amount of waste stone circulation is appropriately controlled to minimize the decline in the grinding capacity. becomes possible.

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

第1〜2図は、本発明の実施例を示す概略図であり、 第3図は従来の排石外部循環方式を採用した竪型ローラ
ミルの概略図である。 1・・供給厚相、    2・・被粉砕物供給管、3・
・・駆動モータ、   4・・・粉砕テーブル、5・粉
砕ローラ、   6・・熱ガス流、7・・排石、   
  8・・・分級機、9・ バッグフィルタ、lO・・
・製品、11・−・水、      12・・・原料供
給装置、13・・・原斜計1装置、 14・・・排石輸
送装置、15・・排石計量装置、 16・・・駆動モー
タ電力計、17・・・水添加装置、  18・・・水添
加量制御装置、19〜22・・・フィルタ、 23・・
・コントローラ、24・・排気ファン。 特許出願人  宇部興産株式会社 第 図
1 and 2 are schematic diagrams showing an embodiment of the present invention, and FIG. 3 is a schematic diagram of a vertical roller mill employing a conventional external rock circulation system. 1. Supply thick phase, 2. Materials to be crushed supply pipe, 3.
...Drive motor, 4.Crushing table, 5.Crushing roller, 6.Hot gas flow, 7.Discharge stone,
8... Classifier, 9. Bag filter, lO...
・Product, 11...Water, 12...Raw material supply device, 13...Original inclination meter 1 device, 14...Exhaust rock transport device, 15...Exhaust rock weighing device, 16...Drive motor Power meter, 17...Water addition device, 18...Water addition amount control device, 19-22...Filter, 23...
・Controller, 24...Exhaust fan. Patent applicant Ube Industries Co., Ltd.

Claims (1)

【特許請求の範囲】[Claims] 排石外部循環方式を有する竪型ローラミルにおいて、排
石がミルから出て新しく供給される原料と一緒になるま
での間に排石との重量比で1%以上5%以下の割合で排
石に水を加えて調湿を行うことを特徴とする竪型ローラ
ミルの運転方法。
In a vertical roller mill that has an external stone circulation system, between the time the waste stone leaves the mill and is combined with newly supplied raw materials, the weight ratio of the waste stone to the waste stone is 1% or more and 5% or less. A method of operating a vertical roller mill characterized by adding water to control humidity.
JP11972690A 1990-05-11 1990-05-11 How to operate a vertical roller mill Expired - Lifetime JPH074549B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11972690A JPH074549B2 (en) 1990-05-11 1990-05-11 How to operate a vertical roller mill

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11972690A JPH074549B2 (en) 1990-05-11 1990-05-11 How to operate a vertical roller mill

Publications (2)

Publication Number Publication Date
JPH0418938A true JPH0418938A (en) 1992-01-23
JPH074549B2 JPH074549B2 (en) 1995-01-25

Family

ID=14768605

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11972690A Expired - Lifetime JPH074549B2 (en) 1990-05-11 1990-05-11 How to operate a vertical roller mill

Country Status (1)

Country Link
JP (1) JPH074549B2 (en)

Also Published As

Publication number Publication date
JPH074549B2 (en) 1995-01-25

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