JPH01288346A - Method for supplying material to mill - Google Patents
Method for supplying material to millInfo
- Publication number
- JPH01288346A JPH01288346A JP11707188A JP11707188A JPH01288346A JP H01288346 A JPH01288346 A JP H01288346A JP 11707188 A JP11707188 A JP 11707188A JP 11707188 A JP11707188 A JP 11707188A JP H01288346 A JPH01288346 A JP H01288346A
- Authority
- JP
- Japan
- Prior art keywords
- weight
- mill
- supplied
- return
- crushing
- 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
Links
- 239000000463 material Substances 0.000 title claims abstract description 48
- 238000000034 method Methods 0.000 title claims description 14
- 238000006467 substitution reaction Methods 0.000 abstract 2
- 239000004568 cement Substances 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 238000007599 discharging Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000005303 weighing Methods 0.000 description 1
Landscapes
- Disintegrating Or Milling (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は、ミルへ材料を供給するに際し、新規供給材料
に破砕分級後の戻し分を加えて供給するようにしたミル
への材料供給方法の改良に関する。[Detailed Description of the Invention] [Industrial Application Field] The present invention provides a method for supplying material to a mill in which, when supplying material to a mill, a material returned after crushing and classification is added to the newly supplied material. Regarding the improvement of
[従来の技術]
従来のこの種の破砕システムとして、ミルの適性フィー
ド(給鉱)をコントロールする下記のシステムがある。[Prior Art] As a conventional crushing system of this type, there is the following system for controlling appropriate feed of a mill.
(1)ミルの粉砕音の音量を計測し、この音量が適度に
なるようにフィードコントロールする方法。(1) A method of measuring the volume of the mill's grinding noise and controlling the feed so that the volume is moderate.
(2)ミルに供給される被粉砕物の供給重量そのものが
一定となるようにフィードコントロールする方法。(2) A method of controlling the feed so that the weight of the material to be crushed that is supplied to the mill remains constant.
(3)ミルの所要動力が予め設定された値に合致(追従
)するようにフィードコントロールする方法。(3) A method of controlling the feed so that the required power of the mill matches (follows) a preset value.
これらの方法では、変数系のPIDコントローラ、又は
これの組み合わせにてコントローラを形成したものを採
用している。These methods employ a variable-based PID controller or a controller formed by a combination of these controllers.
例えば、第2図に示すように、チューブミル1、分級R
2、輸送路3等により構成され、セメントを製造する閉
回路系の粉砕システムにおいては、上記(2)の方法を
採用しているが、チューブミル1に供給される新規供給
材料Fと破砕分級後の戻し分Rとを加えた重量Tを一定
に制御している。For example, as shown in Fig. 2, tube mill 1, classification R
2. In the closed-circuit crushing system for producing cement, which is composed of transportation routes 3, etc., the method (2) above is adopted, but the new feed material F supplied to the tube mill 1 and the crushing classification The weight T including the later returned amount R is controlled to be constant.
T=F+R=一定・・・・・・・・・・・・・・・・・
・・・・・・・・・・・・・(1)[発明が解決しよう
とする課題]
しかし、上記例示の従来技術の現状では、チュ−ブミル
1の粉砕エネルギの消費、つまり、既に一旦破砕が行わ
れた分級機2からの戻し分Rと、新にフィードする新規
供給材料Fとでは、同じ重量であっても戻し分Rの方が
破砕し易く、従って、全重量Tが一定であっても、戻し
分Rの多少によっては、所要の粉砕エネルギに差が生じ
ることとなっていた。T=F+R=constant・・・・・・・・・・・・・・・
(1) [Problems to be Solved by the Invention] However, in the current state of the prior art illustrated above, the consumption of the crushing energy of the tube mill 1, that is, the Even if the weight of the returned material R from the classifier 2 that has been crushed and the newly fed material F is the same, the returned material R is easier to crush, so the total weight T is constant. Even if there is, there will be a difference in the required crushing energy depending on the amount of return R.
このため、単なる供給全重量T一定の制御では、戻し分
Rの破砕し易さが考慮されていないために、ミルにおけ
る動力消費の適正化が図られていないと共に、粉砕効率
の低下になっている。また、これが原因で、精粉(セメ
ント)の粒径分布にバラツキが出る(セメント品質を低
下する)。For this reason, simply controlling the total supply weight T to be constant does not take into account the ease of crushing the returned portion R, which does not allow for optimization of power consumption in the mill and results in a decrease in crushing efficiency. There is. This also causes variations in the particle size distribution of fine powder (cement) (reducing cement quality).
本発明は、このような従来技術の問題点を解決するため
に創案されたもので、粉砕系のトータルの所要エネルギ
(動力消費)が適正化され、製品の品質が向上する新規
なミルへの材料供給方法を提供することを目的とする。The present invention was devised to solve the problems of the conventional technology, and is a novel mill that optimizes the total energy required (power consumption) of the grinding system and improves product quality. The purpose is to provide a material supply method.
[課題を解決するための手段]
上記目的を達成するために本発明のミルへの材料供給方
法は、新規供給材料に破砕分級後の戻し分を加えて、こ
れらの重量和を一定にしてミルに供給するようにしたミ
ルへの材料供給方法において、上記破砕分級後の戻し分
の重量を新規供給材料重量に置換当量させて供給するよ
うにしたものである。[Means for Solving the Problems] In order to achieve the above object, the method of supplying material to a mill of the present invention adds the returned material after crushing and classification to the newly supplied material, and feeds the mill with the sum of the weights constant. In this method, the weight of the returned material after the crushing and classification is replaced with the weight of the new feed material, and then fed.
[作用コ
上記構成により、新規供給材料重量に置換当量させて供
給される戻し分の重量と、新たに供給されてくる新規供
給材料重量とを1・−タルした重量を、ミルの室内を通
過させる一定のフィード量としてコントロールすれば、
上記戻し分及び新規供給材料の粉砕に要するエネルギが
上記ミルの室内の粉砕消費動力に見合い、効率的な粉砕
が行われる。[Operation] With the above configuration, the weight obtained by adding the weight of the returned material, which is replaced by the weight of the new feed material, and the weight of the new feed material, which is newly fed, passes through the mill chamber. If you control it as a constant feed amount,
The energy required for grinding the returned material and the newly supplied material is commensurate with the grinding power consumed in the chamber of the mill, and efficient grinding is carried out.
[実施例] 以下本発明の実施例を図面に基づいて詳述する。[Example] Embodiments of the present invention will be described in detail below based on the drawings.
なお、従来のものと共通する構成要素については同一符
号を使用するものとする。Note that the same reference numerals are used for components common to the conventional one.
第1図は本発明のミルへの材料供給方法の回路図である
。FIG. 1 is a circuit diagram of a method of supplying material to a mill according to the present invention.
図示するように、この実施例の回路は、搬入された新規
供給材料Fを計量する材料計器4と、その材料計器4か
ら放出される新規供給材料ドをチューブミル1に搬送す
る搬送通路5と、そのチューブミル1で破砕された材料
を分級機2に供給する供給通路6と、その分級機2から
製品を排出する排出通路7と、その分級1fi2から再
破砕を要する戻し分Rを上記搬送通路5に計量しつつ戻
す戻し通路8とで構成されている。As shown in the figure, the circuit of this embodiment includes a material meter 4 for weighing the new feed material F brought in, and a conveying path 5 for conveying the new feed material F discharged from the material meter 4 to the tube mill 1. , a supply passage 6 for supplying the material crushed by the tube mill 1 to the classifier 2, a discharge passage 7 for discharging the product from the classifier 2, and the above-mentioned transportation of the returned material R that needs to be crushed again from the classification 1fi2. and a return passage 8 that returns the amount to the passage 5 while being measured.
上記戻し通路8の途中に設けられる計器9は、分級R2
からの戻し分Rを計量する。そしてこの戻し分Rをチュ
ーブミル1への新規供給材料Fに置換当Ji(コントー
ルゲインにという)させ、この当量された戻し分Rと新
規供給材料Fとの和が一定になるようコントロールする
ようになっている。この置換当量並びに当量後の重量一
定のフィードコントロールは図示されないコントローラ
で行われ、コンベア10の搬送速度等を調節して達成さ
れる。The instrument 9 provided in the middle of the return passage 8 is classified as R2.
Weigh the amount R returned from the Then, this returned amount R is replaced with the new feed material F to the tube mill 1 (referred to as control gain), and the sum of the returned amount R and the new feed material F is controlled so as to be constant. It has become. This replacement equivalent and feed control to keep the weight constant after the equivalent are performed by a controller (not shown) and are achieved by adjusting the conveyance speed of the conveyor 10 and the like.
ここに、上記コントロールゲインには、被破砕物の破砕
性(破砕抵抗)、チューブミル1の特性(性能)、分級
機2の特性(性能)により定まる定数である。Here, the control gain is a constant determined by the crushability (crushing resistance) of the object to be crushed, the characteristics (performance) of the tube mill 1, and the characteristics (performance) of the classifier 2.
理論的には、U= (k<1>1−に
のように示される。この場合、Uは分級機に供給される
供給量に対する戻し分の割合である。Theoretically, it is expressed as U = (k<1>1-. In this case, U is the ratio of the returned amount to the supplied amount supplied to the classifier.
しかし、この理論値は実際の利用が非常に困難であるこ
とから、本発明では、
’ro =F+Ro =F十kR=一定・・・・・・・
・・(2)(k<1)
の形式でコントロールするものとする。However, since it is very difficult to use this theoretical value in practice, in the present invention, 'ro = F + Ro = F + kR = constant...
... (2) (k<1) shall be controlled in the form.
コントロールゲインには最近のチューブミル1では0.
2〜0.6の範囲にある。したがって、この破砕システ
ムに使用される装置の運転開始時に、現場の実機により
、実験的に求めて、それを使用することになる。The control gain is 0.0 in the recent tube mill 1.
It is in the range of 2 to 0.6. Therefore, when starting the operation of the equipment used in this crushing system, it is determined experimentally using the actual equipment on site and used.
次に使用例を説明する。Next, a usage example will be explained.
一定フイード量T0が1,000kgとされている場台
において、実機のコントロールゲインkが0.6であっ
たとする。ここに、計器9が400 kgの戻し分を計
量した場合には、新規供給材料Fの重量は760 kg
が計量されて、戻し分と共にミルlに供給されることに
なり、消費動力の適正化が達成され、また破砕効率等の
向上が達成されることになる。Assume that the control gain k of the actual machine is 0.6 in a case where the constant feed amount T0 is 1,000 kg. Here, if the meter 9 weighs the returned amount of 400 kg, the weight of the new feed material F is 760 kg.
is weighed and supplied to the mill 1 together with the returned amount, thereby optimizing power consumption and improving crushing efficiency.
[発明の効果]
以上要するに、本発明によれば、破砕分級後の戻し分の
重量を新規供給材料重量に置換当量させて供給するよう
にしたから、破砕系のトータルの所要エネルギすなわち
、動力消費が適正化されると共に、破砕効率と製品の品
質の向上を図ることができる。[Effects of the Invention] In summary, according to the present invention, since the weight of the returned material after crushing and classification is replaced with the weight of the new feed material and supplied, the total energy required for the crushing system, that is, the power consumption is reduced. This makes it possible to optimize crushing efficiency and improve product quality.
第1図は本発明が採用される破砕システムの破砕系統説
明図、第2図は従来の供給方法を説明する破砕系統図で
ある。
図中、1はミル、2は分級機、Fは新規供給材料、Rは
戻し分である。
第2図FIG. 1 is an explanatory diagram of a crushing system of a crushing system to which the present invention is adopted, and FIG. 2 is a crushing system diagram illustrating a conventional supply method. In the figure, 1 is the mill, 2 is the classifier, F is the new feed material, and R is the returned material. Figure 2
Claims (1)
らの重量和を一定にしてミルに供給するようにしたミル
への材料供給方法において、上記破砕分級後の戻し分の
重量を新規供給材料重量に置換当量させて供給するよう
にしたミルへの材料供給方法。1. In a material supply method to a mill in which the returned material after crushing and classification is added to the newly supplied material and the sum of these weights is kept constant and supplied to the mill, the weight of the returned material after crushing and classification is A method of feeding materials to a mill in which the weight of the feed material is replaced by equivalent weight.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11707188A JPH01288346A (en) | 1988-05-16 | 1988-05-16 | Method for supplying material to mill |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11707188A JPH01288346A (en) | 1988-05-16 | 1988-05-16 | Method for supplying material to mill |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH01288346A true JPH01288346A (en) | 1989-11-20 |
Family
ID=14702696
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP11707188A Pending JPH01288346A (en) | 1988-05-16 | 1988-05-16 | Method for supplying material to mill |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH01288346A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104607301A (en) * | 2014-12-24 | 2015-05-13 | 昆明理工大学 | Method for determining best grinding feed size |
-
1988
- 1988-05-16 JP JP11707188A patent/JPH01288346A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104607301A (en) * | 2014-12-24 | 2015-05-13 | 昆明理工大学 | Method for determining best grinding feed size |
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