JPH078819A - Pulverizing equipment - Google Patents

Pulverizing equipment

Info

Publication number
JPH078819A
JPH078819A JP15559493A JP15559493A JPH078819A JP H078819 A JPH078819 A JP H078819A JP 15559493 A JP15559493 A JP 15559493A JP 15559493 A JP15559493 A JP 15559493A JP H078819 A JPH078819 A JP H078819A
Authority
JP
Japan
Prior art keywords
crushing
raw material
crusher
vertical
roller
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
JP15559493A
Other languages
Japanese (ja)
Other versions
JP2858684B2 (en
Inventor
Tatsuro Ishikawa
辰郎 石川
Hajime Asakawa
肇 浅川
Takashi Sasaki
貴志 佐々木
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 JP5155594A priority Critical patent/JP2858684B2/en
Publication of JPH078819A publication Critical patent/JPH078819A/en
Application granted granted Critical
Publication of JP2858684B2 publication Critical patent/JP2858684B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B02CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
    • B02CCRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
    • B02C21/00Disintegrating plant with or without drying of the material
    • B02C21/002Disintegrating plant with or without drying of the material using a combination of a roller mill and a drum mill

Landscapes

  • Engineering & Computer Science (AREA)
  • Food Science & Technology (AREA)
  • Crushing And Grinding (AREA)
  • Disintegrating Or Milling (AREA)

Abstract

PURPOSE:To provide pulverizing equipment where there is little abnormal vibration and which is equipped with a preliminary pulverizer having relatively high pulverizing capacity in pulverizing equipment for giving two-stage pulverization of the preliminary one and the finish one to a raw material hard to pulverize, mainly such as cement clinker and blast furnace slag CONSTITUTION:A vertical pulverizer 1A used as a preliminary pulverizer has small diameter pulverizing rollers whose average diameter is 0.4-0.8, being the conventional standard value, and has a turntable whose revolution is 1.1-2.0 being the conventional standard value. Pulverizing equipment consists of the vertical pulverizer 1A, raw material supplying equipment 30, 32, 40, 40A, 42, a finish mill 100, a classifier 10 and a conveying path for connecting the above equipment.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明の粉砕設備は,ボールミル
などの仕上ミルの予備粉砕機として竪型粉砕機を使用す
るものであって,主としてセメントクリンカ,高炉スラ
グなど特に硬くて粉砕し難い原料を,異常振動を抑制し
て連続安定的に,かつ,比較的高い粉砕能力で運転する
ことのできる予備粉砕機を備えた粉砕設備に関する。
BACKGROUND OF THE INVENTION The crushing equipment of the present invention uses a vertical crusher as a preliminary crusher for a finishing mill such as a ball mill. Mainly hard materials that are hard to crush, mainly cement clinker and blast furnace slag. The present invention relates to a crushing facility equipped with a preliminary crusher capable of continuously operating stably with a comparatively high crushing ability by suppressing abnormal vibration.

【0002】[0002]

【従来の技術】石灰石や高炉スラグ,セメント原料など
の化学品を細かく粉砕し粉体とする粉砕機の一種とし
て,図4に示すように,回転テーブルと粉砕ローラとを
備えた竪型粉砕機1が広く用いられている。この種の粉
砕機は,円筒状ケーシング15の下部においてモータ2
Aにより減速機2で駆動されて低速回転する円盤状の回
転テーブル3Aと,その上面外周部を円周方向へ等分す
る箇所に油圧などで圧接されて従動回転する複数個の粉
砕ローラ4とを備えている。
2. Description of the Related Art As a kind of crusher for finely crushing chemicals such as limestone, blast furnace slag, and cement raw material into powder, as shown in FIG. 4, a vertical crusher equipped with a rotary table and crushing rollers. 1 is widely used. This type of crusher has a motor 2 at the bottom of the cylindrical casing 15.
A disk-shaped rotary table 3A driven by a speed reducer 2 by A to rotate at a low speed, and a plurality of crushing rollers 4 which are driven to rotate by being pressed by hydraulic pressure or the like at locations equally dividing the outer peripheral portion of the upper surface thereof in the circumferential direction. Is equipped with.

【0003】粉砕ローラ4はケーシング15に軸6によ
って揺動自在に軸支されたアーム5とアーム7を介して
油圧シリンダ9のピストンロッド10に連結されてお
り,油圧シリンダ9を作動させることにより,粉砕ロー
ラ4を回転テーブル3A上に押圧して原料への粉砕圧力
を与えている。3Bは回転テーブル3Aの外周縁に設け
られ原料層厚を調整するダムリング,14は回転テーブ
ル3A周囲のガス吹上用環状空間通路,14Aはガス供
給路,13は羽根13Aにより粉砕された原料を分級す
る回転セパレータ,16はガスと共に製品を取出す排出
口,17は原料投入シュートである。
The crushing roller 4 is connected to a piston rod 10 of a hydraulic cylinder 9 through an arm 5 and an arm 7 which are pivotally supported by a shaft 6 in a casing 15, and by operating the hydraulic cylinder 9, The crushing roller 4 is pressed against the rotary table 3A to apply a crushing pressure to the raw material. 3B is a dam ring provided on the outer periphery of the rotary table 3A for adjusting the raw material layer thickness, 14 is a gas blowing annular space passage around the rotary table 3A, 14A is a gas supply passage, and 13 is a raw material crushed by blades 13A. A rotary separator for classification, 16 is an outlet for taking out a product together with gas, and 17 is a raw material charging chute.

【0004】このような竪型粉砕機において,回転テー
ブルの中央部へ原料投入シュート17で供給された原料
は,回転テーブル3Aの回転によりテーブル半径方向の
遠心力を受けて回転テーブル3A上を滑るときに回転テ
ーブル3Aにより回転方向の力を受け,回転テーブル3
Aとの間で滑って回転テーブル3Aの回転数よりいくら
か遅い回転を行なう。以上2つの力,すなわち,半径方
向と回転方向の力とが合成され,原料は回転テーブル3
A上を渦巻状の軌跡を描いて回転テーブル3Aの外周部
へ移動する。この外周部には,ローラが圧接されて回転
しているので,渦巻線を描いた原料は粉砕ローラ4と回
転テーブル3Aとの間へローラ軸方向とある角度をなす
方向から進入して噛込まれて粉砕される。
In such a vertical crusher, the raw material supplied to the central portion of the rotary table by the raw material chute 17 receives the centrifugal force in the radial direction of the rotary table 3A and slides on the rotary table 3A. Sometimes the rotary table 3A receives a force in the direction of rotation,
It slides with A and makes a rotation somewhat slower than the rotation speed of the rotary table 3A. The above two forces, that is, the radial direction force and the rotational direction force are combined, and the raw material is the rotary table 3.
A spiral locus is drawn on A to move to the outer peripheral portion of the rotary table 3A. Since the roller is pressed against the outer periphery and is rotating, the raw material in which the spiral is drawn enters between the crushing roller 4 and the rotary table 3A from a direction forming an angle with the roller axial direction and is bitten therein. It is crushed and crushed.

【0005】一方,ケーシング15の基部にはダクトに
よって空気,あるいは熱風などのガスが導かれており,
このガスが回転テーブル3Aの外周面とケーシングの内
周面との間の環状空間部14から吹き上がることによ
り,粉砕された微粉体はガスに同伴されてケーシング1
5内を上昇し,上部に位置するセパレータ13の羽根1
3Aにより分級作用を受け,所定粒度の製品はガスと共
に排出口16から排出され次の工程へ送られる。
On the other hand, gas such as air or hot air is guided to the base of the casing 15 by a duct,
This gas is blown up from the annular space portion 14 between the outer peripheral surface of the rotary table 3A and the inner peripheral surface of the casing, so that the pulverized fine powder is entrained in the gas and the casing 1
Blades 1 of the separator 13 located in the upper part
The product having a predetermined particle size is discharged by the 3A from the discharge port 16 together with the gas and sent to the next step.

【0006】近年粉砕原料の製品粒度への要求は年々高
まり,微粉砕あるいは超微粉砕と称されるように,益々
製品粒度の微細化が望まれるようになった。そこで単一
の粉砕機でその要求に応じることは困難になり,このた
め,たとえばボールミル等の仕上ミルに原料を投入する
前に予備粉砕機として分級機を内蔵しない竪型粉砕機を
使用し,竪型粉砕機の粉砕産物を振動篩でふるい分けし
て微粉のみを仕上ミルへ供給する方法が採用されるよう
になった。図5はこの場合のフローシートを示し,原料
ホッパ30の原料はコンスタントフィード・ウェア40
を経て,竪型粉砕機1で粉砕され,産物はバケットエレ
ベータ80を介して振動篩90に導かれてスクリーニン
グされ,微粉のみ仕上ミル(ボールミル)100で粉砕
され,オーバサイズの産物は再び竪型粉砕機1で予備粉
砕されるようになっている。
In recent years, the demand for the product particle size of pulverized raw materials has been increasing year by year, and it has become more and more desired to make the product particle size finer, which is called fine pulverization or ultrafine pulverization. Therefore, it becomes difficult to meet the demand with a single crusher. For this reason, for example, a vertical crusher without a classifier is used as a preliminary crusher before the raw material is put into a finishing mill such as a ball mill. A method has been adopted in which pulverized products of a vertical pulverizer are sieved with a vibrating screen and only fine powder is supplied to a finishing mill. FIG. 5 shows a flow sheet in this case. The raw material of the raw material hopper 30 is a constant feed wear 40.
After that, the product is pulverized by the vertical pulverizer 1, the product is guided to the vibrating screen 90 through the bucket elevator 80 and screened, and only the fine powder is pulverized by the finishing mill (ball mill) 100, and the oversized product is re-vertical. Preliminary crushing is performed by the crusher 1.

【0007】[0007]

【発明が解決しようとする課題】このようなフローシー
トに示す予備粉砕と仕上粉砕の組み合わせによる2段粉
砕で,予備粉砕機として分級機を内蔵しない竪型粉砕機
を使用する粉砕設備では,セメント・クリンカや高炉ス
ラグ等被粉砕性の厳しい原料を単独の仕上ミルのみの粉
砕設備にくらべて高生産性と低い電力原単位で粉砕でき
るという利点があるが,反面予備粉砕機としての竪型粉
砕機は,粉砕ローラへの原料の噛込みが悪くミル異常振
動を頻発して連続安定運転の継続が困難で,異常振動発
生時の緊急避難的な供給量削減や運転停止による生産性
悪化を招くことがあった。
The crushing equipment using a vertical crusher without a classifier as a preliminary crusher by the two-stage crushing by the combination of the preliminary crushing and the finish crushing shown in the flow sheet as described above.・ Compared to crushing equipment with only a finishing mill, crushers and blast furnace slag, which have severe grindability, have the advantage that they can be crushed with higher productivity and lower power consumption, but on the other hand, vertical crushing as a preliminary crusher In the machine, it is difficult to continue continuous stable operation due to frequent occurrence of abnormal mill vibrations due to poor biting of raw material into the crushing rollers, which leads to productivity reduction due to emergency evacuation of supply volume reduction and abnormal operation when abnormal vibration occurs. There was an occasion.

【0008】[0008]

【課題を解決するための手段】以上の課題を解決するた
めに,本発明の粉砕設備においては,竪型粉砕機を予備
粉砕機として使用する粉砕設備であって,該竪型粉砕機
は回転テーブルの外周部上面に複数個の回転自在な粉砕
ローラを配設し,粉砕ローラに所定の粉砕力を与えて回
転テーブル上面と粉砕ローラ周面との間で原料を粉砕す
る竪型粉砕機であって,該粉砕ローラは平均直径が従来
採用されていた粉砕ローラ平均直径の標準値の0.4〜
0.8となる小径ローラとするとともに,回転テーブル
回転数を従来採用されていた標準値の1.1〜2.0倍
に増速した竪型粉砕機とし,該竪型粉砕機へ原料を供給
する原料供給設備と,該竪型粉砕機と,該竪型粉砕機の
粉砕産物を受け入れて粉砕する仕上ミルと,該仕上ミル
の粉砕産物を分級する分級装置と,これら各機器を連結
する輸送系路と,からなる粉砕設備とした。
In order to solve the above problems, in the crushing equipment of the present invention, a vertical crusher is used as a preliminary crusher, and the vertical crusher rotates. A vertical crusher in which a plurality of rotatable crushing rollers are arranged on the upper surface of the outer periphery of the table and a predetermined crushing force is applied to the crushing rollers to crush the raw material between the upper surface of the rotating table and the crushing roller peripheral surface. The crushing roller has an average diameter of 0.4 to 0.4 which is the standard value of the average diameter of the crushing roller which has been conventionally adopted.
A vertical roller with a small diameter roller of 0.8 and a rotary table rotation speed increased to 1.1 to 2.0 times the standard value that was conventionally adopted, and the raw material was fed to the vertical crusher. A raw material supply facility for supplying, a vertical crusher, a finishing mill for receiving and crushing crushed products of the vertical crusher, a classifying device for classifying the crushed products of the finishing mill, and these devices are connected. The crushing equipment consisted of a transportation route.

【0009】[0009]

【作用】本発明の粉砕設備においては,予備粉砕を行な
う竪型粉砕機では粉砕ローラを小径ローラとし,かつ,
回転テーブルを増速した構成としたので,粉砕ローラの
上流の原料噛込角が増加した点およびテーブルスピード
増加に起因する原料引込力の増加の相乗効果によって,
粉砕ローラへ噛込み後の原料の離脱(上流側への逃げ)
が減少して原料層厚の均一安定化による異常振動の減少
と粉砕力の増加が得られる。
In the crushing equipment of the present invention, in the vertical crusher for performing preliminary crushing, the crushing roller is a small diameter roller, and
Since the rotary table is configured to be accelerated, the synergistic effect of the increase of the raw material drawing force due to the increase of the raw material trapping angle upstream of the crushing roller and the increase of the table speed
Release of raw material after biting into the crushing roller (escaping to the upstream side)
It is possible to reduce the abnormal vibration and increase the crushing force due to the uniform stabilization of the raw material layer thickness.

【0010】[0010]

【実施例】以下図面に基づいて本発明の実施例の詳細に
ついて説明する。図1〜図3は本発明の実施例に係り,
図1は粉砕設備のフローシート,図2は竪型粉砕機の全
体縦断面図,図3は従来例と本発明の粉砕ローラへの原
料噛込み状況の比較説明図である。図において,30は
原料ホッパ(クリンカ),32は原料ホッパ(石膏),
40,40A,42はコンスタントフィード・ウェア,
1Aは竪型粉砕機,70はベルトコンベヤ,80はバケ
ットエレベータ,90Aはエアスライド,100は仕上
ミル,100A〜100Eはエアスライド,110はサ
イクロンセパレータ,110Aは押込ファン,120は
集塵装置,130は吸引ファン,140はダンパであ
る。仕上ミル100は通常ボールミルやロッドミルを使
用し,サイクロンセパレータ110を閉回路に連結して
分級後の粗粉を仕上ミル100の入口側へ再度供給す
る。微粉はバッグフィルタや電気集塵機などの集塵装置
120で捕集し,製品となる。
Embodiments of the present invention will be described below in detail with reference to the drawings. 1 to 3 relate to an embodiment of the present invention,
FIG. 1 is a flow sheet of a crushing facility, FIG. 2 is an overall vertical cross-sectional view of a vertical crusher, and FIG. 3 is a comparative explanatory diagram of a raw material biting state into a crushing roller of a conventional example and the present invention. In the figure, 30 is a raw material hopper (clinker), 32 is a raw material hopper (plaster),
40, 40A, 42 are constant feed wear,
1A is a vertical crusher, 70 is a belt conveyor, 80 is a bucket elevator, 90A is an air slide, 100 is a finishing mill, 100A to 100E are air slides, 110 is a cyclone separator, 110A is a pushing fan, 120 is a dust collector, Reference numeral 130 is a suction fan, and 140 is a damper. A ball mill or a rod mill is usually used as the finishing mill 100, and the cyclone separator 110 is connected in a closed circuit to re-feed the classified coarse powder to the inlet side of the finishing mill 100. The fine powder is collected by a dust collector 120 such as a bag filter or an electric dust collector to be a product.

【0011】次に,竪型粉砕機1Aの構造や作動につい
て図2,図3に基づいて説明する。本発明の竪型粉砕機
1Aは,図4に示す従来構造の竪型粉砕機1の頂部に装
備したセパレータ13を取り除いたものであり,図示し
ない電動機および減速機2を介して竪軸回りに回転する
回転テーブル3Aと回転テーブル3Aにア−ム5ならび
に軸6を介してアーム7を経由して揺動し油圧シリンダ
9によって押圧される粉砕ローラ4とを備え,ケーシン
グ15の上部中央の原料投入シュート17より回転テー
ブル3A上へ供給された原料は回転テーブル3Aと粉砕
ローラ4との間で粉砕されて回転テーブル3Aをオーバ
ーフローして環状空間通路14へ落下し,スクレーパ6
0aによって掻き寄せられて排石シュート60を経由し
てベルトコンベヤ70により機外へ搬送される。環状空
間通路14には,図示しないダクトにより上向きの気流
を流して,原料中の微粉や粉砕された微粉を空気搬送に
より排出口16より排出してサイクロンセパレータ11
0へ搬送する。
Next, the structure and operation of the vertical crusher 1A will be described with reference to FIGS. The vertical crusher 1A of the present invention is obtained by removing the separator 13 mounted on the top of the vertical crusher 1 of the conventional structure shown in FIG. 4, and is provided around the vertical axis via an unillustrated electric motor and speed reducer 2. The rotary table 3A that rotates, and the crushing roller 4 that swings through the arm 5 via the arm 5 and the shaft 6 and is pressed by the hydraulic cylinder 9 to the rotary table 3A, and the raw material in the upper center of the casing 15 are provided. The raw material supplied from the charging chute 17 onto the rotary table 3A is crushed between the rotary table 3A and the crushing roller 4, overflows the rotary table 3A and drops into the annular space passage 14, and the scraper 6
It is scraped by 0a and is conveyed to the outside of the machine by the belt conveyor 70 via the stone discharging chute 60. In the annular space passage 14, an upward airflow is caused to flow by a duct (not shown), and the fine powder in the raw material and the pulverized fine powder are discharged from the discharge port 16 by air transfer to the cyclone separator 11
Transport to 0.

【0012】本発明の竪型粉砕機1Aの粉砕ローラ4
は,このような竪型粉砕機にこれまで採用されていた粉
砕ローラの寸法よりも小さい小径ローラを採用し,か
つ,回転テーブル回転数も増速した。すなわち,従来の
粉砕ローラ平均直径dは回転テーブル3Aの直径をDと
したとき2ローラでは0.75D,3ローラでは0.6
3D,4ローラでは0.75Dとしていたが,本発明の
竪型粉砕機1Aの粉砕ローラ平均直径dはこれら従来値
の0.4〜0.8とした。一方,回転テーブル3Aの回
転数Nはこのような予備粉砕機として使用する竪型粉砕
機にあってはこれまで回転数NはN=K/D1/2 (Kは
実験定数でK=34.7を採用)という式で算定されて
いたが,これらの従来値の1.1〜2.0倍の回転数N
とした。このように,従来に比べて小径ローラで,か
つ,テーブル回転数を増速することにより,図3に示す
ように,従来例(a)に比べて本発明(b)の場合原料
噛込角θが増加するので,噛込み効率が上昇し一旦粉砕
ローラに噛込まれた原料は粉砕ローラの押付力(圧下
力)による粉砕ローラ上流側への逃げが少なくなり,粉
砕ローラの上下動が減って振動が低下する。また,テー
ブルスピードを増速したことによりテーブルスピードに
よる引込力Qが増加してローラ押付力Pとの合力である
粉砕力Fが増加し粉砕能力もアップする。粉砕ローラ平
均直径dの低減率0.4〜0.8のうち,下限値はこれ
以下の低減では粉砕能力が大幅に低下する限界を示し,
上限値は異常振動の発生する限界を示す。また,テーブ
ル回転数Nの範囲1.1〜2.0についても,下限値は
能力限界を示し,上限値は振動限界を示す。原料の被粉
砕性と客先要求能力を総合的に考慮してこれら両者の値
を適性に選択することが望ましい。
Crushing roller 4 of vertical crusher 1A of the present invention
Has adopted a small-diameter roller that is smaller than the size of the crushing roller used so far in such a vertical crusher, and has also increased the rotational speed of the rotary table. That is, the average diameter d of the conventional crushing roller is 0.75D for two rollers and 0.6 for three rollers, where D is the diameter of the rotary table 3A.
The 3D and 4 rollers were set to 0.75D, but the average diameter d of the crushing roller of the vertical crusher 1A of the present invention was set to these conventional values of 0.4 to 0.8. On the other hand, the rotation speed N of the rotary table 3A is such that in the vertical crusher used as such a preliminary crusher, the rotation speed N has been N = K / D 1/2 (K is an experimental constant K = 34). However, the rotation speed N is 1.1 to 2.0 times the conventional value.
And In this way, as shown in FIG. 3, in the case of the present invention (b), as compared with the conventional example (a), the raw material biting angle is smaller than that of the conventional case by increasing the number of rotations of the table by using the small diameter roller. Since θ increases, the biting efficiency increases, and the material once bitten into the crushing roller is less likely to escape to the upstream side of the crushing roller due to the pressing force (compression force) of the crushing roller, and the vertical movement of the crushing roller is reduced. Vibration is reduced. Further, since the table speed is increased, the pulling force Q due to the table speed is increased, the crushing force F which is the resultant force with the roller pressing force P is increased, and the crushing capacity is also improved. Of the reduction ratios of 0.4 to 0.8 of the average diameter d of the crushing roller, the lower limit value shows the limit that the crushing ability will be significantly reduced at a reduction below this value.
The upper limit indicates the limit at which abnormal vibration occurs. Further, also in the range of the table rotation speed N of 1.1 to 2.0, the lower limit shows the capacity limit and the upper limit shows the vibration limit. It is desirable to appropriately select both of these values in consideration of the pulverizability of the raw material and the required capacity of the customer.

【0013】本発明の粉砕設備は,このような竪型粉砕
機1Aを予備粉砕機として原料を予備粉砕しベルトコン
ベヤ70により排出された原料はバケットエレバータ8
0を経由しエアスライド90Aにより仕上ミル100へ
供給されるが,その輸送系路の途中に設けた分配ダンパ
90Bにより原料を1部竪型粉砕機1Aへ還元し閉回路
を形成する。
In the crushing equipment of the present invention, such a vertical crusher 1A is used as a preliminary crusher to pre-crush the raw material and the raw material discharged by the belt conveyor 70 is the bucket elevator 8
Although it is supplied to the finishing mill 100 by the air slide 90A via 0, the raw material is reduced to the one-part vertical crusher 1A by the distribution damper 90B provided on the way of the transportation system path to form a closed circuit.

【0014】以上説明したように,本発明の粉砕設備に
おいては,予備粉砕機としての竪型粉砕機1Aと仕上ミ
ル100との間に振動篩などの原料粒度選別装置が不要
で,竪型粉砕機は異常振動が少なく比較的高い粉砕能力
が得られる。
As described above, in the crushing equipment of the present invention, a raw material particle size selecting device such as a vibrating sieve is not required between the vertical crusher 1A as a preliminary crusher and the finishing mill 100, and the vertical crushing is performed. The machine has less abnormal vibration and can obtain a relatively high crushing capacity.

【0015】[0015]

【発明の効果】以上述べたように,本発明の粉砕設備に
おいては下記のような効果を奏する。 竪型粉砕機にはセパレータがなく,その分設備費と
ランニングコストが安いうえに,異常振動が少なく高い
粉砕能力を維持した連続安定運転が継続できる。 仕上ミルには最終製品となり得る微粉を予め除去し
た微粉を主体とした原料が供給されるから,粉砕比 ( r
eduction ratio )が小さく,粉砕効率が向上するととも
により細かい製品をつくることができる。 従来技術のような振動篩を使用しないので,摩耗部
品の取換え間隔が大きく,連続運転期間が長くなり生産
性が向上し,メインテナンス性が改善される。 予備粉砕と仕上粉砕との間に分級設備が不要で設備
費が安価である。
As described above, the crushing equipment of the present invention has the following effects. The vertical crusher does not have a separator, so the equipment cost and running cost are low, and it is possible to continue continuous stable operation with less abnormal vibration and high crushing capacity. The finishing mill is supplied with raw materials mainly composed of fine powder from which fine powder that could be the final product has been removed beforehand.
It has a small eduction ratio, improves crushing efficiency, and enables the production of finer products. Since the vibrating screen used in the prior art is not used, the replacement intervals of worn parts are long, the continuous operation period is long, the productivity is improved, and the maintainability is improved. No classification equipment is required between pre-grinding and finish grinding, and the equipment cost is low.

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

【図1】本発明の粉砕設備の実施例を示すフローシート
である。
FIG. 1 is a flow sheet showing an example of a crushing facility of the present invention.

【図2】本発明の実施例に係る竪型粉砕機の全体縦断面
図である。
FIG. 2 is an overall vertical cross-sectional view of a vertical crusher according to an embodiment of the present invention.

【図3】従来例と本発明の粉砕ローラへの原料噛込み状
況を説明する比較説明図である。
FIG. 3 is a comparative explanatory view for explaining a state of raw material biting into a crushing roller of a conventional example and the present invention.

【図4】従来の竪型粉砕機の全体縦断面図である。FIG. 4 is an overall vertical sectional view of a conventional vertical crusher.

【図5】従来の粉砕設備のフローシートである。FIG. 5 is a flow sheet of a conventional crushing facility.

【符号の説明】[Explanation of symbols]

1 竪型粉砕機 1A 竪型粉砕機 3A 回転テーブル 4 粉砕ローラ 5 アーム 6 軸 7 アーム 9 油圧シリンダ 14 環状空間通路 15 ケーシング 16 排出口 17 原料投入シュート 30 原料ホッパ 32 原料ホッパ 40 コンスタントフィード・ウェア 40A コンスタントフィード・ウェア 42 コンスタントフィード・ウェア 60 排石シュート 70 ベルトコンベヤ 80 バケットエレベータ 90 振動篩 90A エアスライド 90B 分配ダンパ 100 仕上ミル 100A エアスライド 100B バケットエレベータ 100C エアスライド 100D エアスライド 100E エアスライド 110 サイクロン・セパレータ 110A 押込ファン 120 集塵装置 130 吸引ファン 140 ダンパ θ 原料噛込角 θl 原料噛込角(標準ローラ) θs 原料噛込角(小径ローラ) F 粉砕力 P ローラ押付力(圧下力) Q テーブルスピードによる引込力1 Vertical Grinder 1A Vertical Grinder 3A Rotary Table 4 Grinding Roller 5 Arm 6 Shaft 7 Arm 9 Hydraulic Cylinder 14 Annular Space Passage 15 Casing 16 Discharge Port 17 Raw Material Input Chute 30 Raw Material Hopper 32 Raw Material Hopper 40 Constant Feed Wear 40A Constant Feed Wear 42 Constant Feed Wear 60 Stone Exhaust Chute 70 Belt Conveyor 80 Bucket Elevator 90 Vibrating Screen 90A Air Slide 90B Distribution Damper 100 Finishing Mill 100A Air Slide 100B Bucket Elevator 100C Air Slide 100D Air Slide 100E Air Slide 110 Cyclone Separator 110A Pushing fan 120 Dust collector 130 Suction fan 140 Damper θ Raw material trapping angle θ l Raw material trapping angle (standard roller) θ s Raw material biting angle (small diameter roller) F Crushing force P Roller pressing force (rolling down force) Q Table speed pulling force

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 竪型粉砕機を予備粉砕機として使用する
粉砕設備であって,該竪型粉砕機は回転テーブルの外周
部上面に複数個の回転自在な粉砕ローラを配設し,粉砕
ローラに所定の粉砕力を与えて回転テーブル上面と粉砕
ローラ周面との間で原料を粉砕する竪型粉砕機であっ
て,該粉砕ローラは平均直径が従来採用されていた粉砕
ローラ平均直径の標準値の0.4〜0.8となる小径ロ
ーラとするとともに,回転テーブル回転数を従来採用さ
れていた標準値の1.1〜2.0倍に増速した竪型粉砕
機とし,該竪型粉砕機へ原料を供給する原料供給設備
と,該竪型粉砕機と,該竪型粉砕機の粉砕産物を受け入
れて粉砕する仕上ミルと,該仕上ミルの粉砕産物を分級
する分級装置と,これら各機器を連結する輸送系路と,
からなる粉砕設備。
1. A crushing facility using a vertical crusher as a preliminary crusher, wherein the vertical crusher has a plurality of rotatable crushing rollers arranged on an upper surface of an outer peripheral portion of a rotary table. A vertical crusher for crushing raw materials between the upper surface of the rotary table and the peripheral surface of the crushing roller by applying a predetermined crushing force to the crushing roller. The vertical roller is a small diameter roller having a value of 0.4 to 0.8, and the rotational speed of the rotary table is increased to 1.1 to 2.0 times the standard value conventionally used. A raw material supply facility for supplying a raw material to a mold crusher, the vertical crusher, a finishing mill for receiving and crushing the crushed product of the vertical crusher, and a classifying device for classifying the crushed product of the finish mill, A transportation route connecting these devices,
Crushing equipment consisting of
JP5155594A 1993-06-25 1993-06-25 Crushing equipment Expired - Lifetime JP2858684B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5155594A JP2858684B2 (en) 1993-06-25 1993-06-25 Crushing equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5155594A JP2858684B2 (en) 1993-06-25 1993-06-25 Crushing equipment

Publications (2)

Publication Number Publication Date
JPH078819A true JPH078819A (en) 1995-01-13
JP2858684B2 JP2858684B2 (en) 1999-02-17

Family

ID=15609446

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5155594A Expired - Lifetime JP2858684B2 (en) 1993-06-25 1993-06-25 Crushing equipment

Country Status (1)

Country Link
JP (1) JP2858684B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105750064A (en) * 2016-03-21 2016-07-13 南通弘亚机械制造有限公司 Grinding equipment for dry type cement production line

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105750064A (en) * 2016-03-21 2016-07-13 南通弘亚机械制造有限公司 Grinding equipment for dry type cement production line

Also Published As

Publication number Publication date
JP2858684B2 (en) 1999-02-17

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