JPH04256449A - Vertical crusher - Google Patents
Vertical crusherInfo
- Publication number
- JPH04256449A JPH04256449A JP10224691A JP10224691A JPH04256449A JP H04256449 A JPH04256449 A JP H04256449A JP 10224691 A JP10224691 A JP 10224691A JP 10224691 A JP10224691 A JP 10224691A JP H04256449 A JPH04256449 A JP H04256449A
- Authority
- JP
- Japan
- Prior art keywords
- gas duct
- hot gas
- rotary table
- raw material
- vertical crusher
- 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
Links
- 239000002994 raw material Substances 0.000 claims description 18
- 239000000843 powder Substances 0.000 claims description 5
- 239000008187 granular material Substances 0.000 claims description 3
- 239000007789 gas Substances 0.000 abstract description 40
- 238000010298 pulverizing process Methods 0.000 abstract description 8
- 238000007664 blowing Methods 0.000 abstract description 7
- 238000000227 grinding Methods 0.000 description 3
- 230000002093 peripheral effect Effects 0.000 description 3
- 230000000630 rising effect Effects 0.000 description 3
- 235000019738 Limestone Nutrition 0.000 description 2
- 239000004568 cement Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000006028 limestone Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000002893 slag Substances 0.000 description 2
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000009827 uniform distribution Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C15/00—Disintegrating by milling members in the form of rollers or balls co-operating with rings or discs
- B02C15/001—Air flow directing means positioned on the periphery of the horizontally rotating milling surface
Landscapes
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Crushing And Grinding (AREA)
Abstract
Description
【0001】0001
【産業上の利用分野】本発明は,回転テーブルと粉砕ロ
ーラとの協働により,石灰石や高炉スラグ,セメント原
料などの原料を粉砕する竪型粉砕機に関するものである
。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a vertical pulverizer for pulverizing raw materials such as limestone, blast furnace slag, and cement raw materials through the cooperation of a rotary table and pulverizing rollers.
【0002】0002
【従来の技術】石灰石や高炉スラグ,セメント原料など
の原料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1aの下部においてモータ2A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。[Prior Art] As a type of pulverizer that finely grinds raw materials such as limestone, blast furnace slag, and cement raw materials into powder,
As shown in FIG. 4, a vertical crusher 1 equipped with a rotating table and crushing rollers is widely used. This type of crusher includes a disc-shaped rotary table 3A that is driven by a motor 2A and a reducer 2 to rotate at low speed in the lower part of a cylindrical casing 1a, and a hydraulic pressure installed at a portion that equally divides the outer periphery of the upper surface in the circumferential direction. The crushing roller 4 is provided with a plurality of crushing rollers 4 that are pressed against each other and rotated as a result of rotation.
【0003】粉砕ローラ4はケーシング1a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
れ原料層圧を調整するダムリング,14は回転テーブル
3A周囲のガス吹上用の環状空間通路,15は熱風吹上
通路,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り出す排
出口,17は原料投入シュートである。また,図5や図
6に示すように,回転テーブル3Aの外周下側には円環
状の熱ガスダクト32が配設され,左右の取入口30,
30より熱ガスまたは空気を導入している。The crushing roller 4 is connected to a piston rod 10 of a hydraulic cylinder 9 via an arm 5 and an arm 7 which are pivotally supported by a shaft 6 on the casing 1a, and when the hydraulic cylinder 9 is actuated, the crushing roller 4 is , the crushing roller 4 is pressed onto the rotary table 3A to apply crushing pressure to the raw material. 3B is a dam ring provided on the outer peripheral edge of the rotary table 3A to adjust the raw material layer pressure, 14 is an annular space passage around the rotary table 3A for blowing up gas, 15 is a hot air blowing passage, and 13 is a raw material pulverized by the blade 13A. 16 is an outlet for taking out the product together with the gas, and 17 is a raw material input chute. In addition, as shown in FIGS. 5 and 6, an annular hot gas duct 32 is provided below the outer periphery of the rotary table 3A, and the left and right intake ports 30,
Hot gas or air is introduced from 30.
【0004】このような竪型粉砕機において,回転テー
ブル3A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3A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3A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み込まれて粉砕される。[0004] In such a vertical crusher, the raw material supplied to the center of the rotary table 3A through the raw material input chute 17 is subjected to centrifugal force in the radial direction of the table due to the rotation of the rotary table 3A, and flows over the rotary table 3A. When it slides, it receives a rotational force from the rotary table 3A, slides between it and the rotary table 3A, and rotates somewhat slower than the rotation speed of the rotary table 3A. The above two forces, that is, the forces in the radial direction and the force in the rotational direction are combined, and the raw material moves to the outer circumference of the rotary table 3A while drawing a spiral trajectory on the rotary table 3A. A roller is pressed against this outer periphery and rotates, so the raw material drawn in the spiral line is transferred to the crushing roller 4.
The particles enter between the roller and the rotary table 3A from a direction forming a certain angle with the axial direction of the roller, and are bitten and crushed.
【0005】一方,ケーシング1aの基部には熱ガスダ
クト32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通路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1a内を上昇し,上部に位置するセパレータ1
3の羽根13A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 1a by a hot gas duct 32, and this gas flows through the annular space passage between the outer peripheral surface of the rotary table 3A and the inner peripheral surface of the casing. By blowing up from 14, the crushed fine powder is accompanied by gas and rises inside the casing 1a, and reaches the separator 1 located at the upper part.
The products having a predetermined particle size are discharged from the discharge port 16 together with the gas and sent to the next process.
【0006】熱ガスダクト32から竪型粉砕機1の下流
に設けた吸引ファンの吸引力により熱風吹上通路15を
通って上昇する気流は出来るだけ回転テーブル3Aの外
周均等に分配されるのが望ましく,そのため,熱ガスダ
クト32への取入口30は出来るだけ多く設けて均等配
置することが望ましい。しかしながら,スペース的な制
約のため対角線上の2個所しか設けられないのが実状で
ある。It is desirable that the airflow rising from the hot gas duct 32 through the hot air blowing passage 15 by the suction force of the suction fan provided downstream of the vertical crusher 1 be distributed as evenly as possible around the outer circumference of the rotary table 3A. Therefore, it is desirable to provide as many intake ports 30 to the hot gas duct 32 as possible and to arrange them evenly. However, in reality, due to space constraints, only two diagonal locations can be provided.
【0007】[0007]
【発明が解決しようとする課題】このような取入口30
をもつ熱ガスダクト32においては,取入口30が対角
線に配置(180度の位置)されているので,一見する
と供給された熱ガスまたは空気は全く対称に熱ガスダク
ト32内へ入り,熱ガスダクト32の上方にある円環状
の熱風吹上通路15および環状空間通路14へほぼ均等
に分配されるように思われる。しかし,実際には,回転
テーブル3Aが高速で回転しているために翼車効果が働
き,図6に示すように,2個所の取入口30,30から
熱ガスダクト32内に入った気流が図中に示すP点およ
びQ点において渦を発生させ,このため大きな圧力損失
を生じるとともに,熱風吹上通路15への気流の均等配
分を阻害する。この現象は究極的には粉砕効率の低下を
招くので望ましくない。[Problem to be solved by the invention] Such an intake port 30
In a hot gas duct 32 with It appears that the hot air is almost evenly distributed to the annular hot air blow-up passage 15 and the annular space passage 14 located above. However, in reality, since the rotary table 3A is rotating at high speed, the impeller effect comes into play, and as shown in FIG. Vortices are generated at points P and Q shown in the figure, resulting in a large pressure loss and impeding the uniform distribution of airflow to the hot air blow-up passage 15. This phenomenon is undesirable because it ultimately leads to a decrease in grinding efficiency.
【0008】[0008]
【課題を解決するための手段】上に述べた課題を解決す
るために,本発明の竪型粉砕機は,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置し,原料
投入シュートを経由して供給した原料を粉砕ローラに所
定の粉砕圧力を与えて回転テーブル上面と粉砕ローラ周
面との間で粉砕し,粉砕後の粉粒体を回転テーブル外周
下部に配設した円環状の熱ガスダクトより供給された上
昇気流に随伴して搬送する竪型粉砕機において,該熱ガ
スダクトの取入口の内部に垂直軸回りに回動自在で導入
ガスを回転テーブルの回転方向に整流させるために屈曲
したガイドベーンを少なくとも1個以上配設した構成と
した。[Means for Solving the Problems] In order to solve the above-mentioned problems, the vertical crusher of the present invention has a plurality of rotatable crushing rollers arranged on the upper surface of the outer periphery of a rotary table, and the raw material is inputted. The raw material supplied via the chute is crushed between the top surface of the rotary table and the circumferential surface of the crushing roller by applying a predetermined crushing pressure to the crushing roller, and the powder and granules after being crushed are placed in a circle at the bottom of the outer periphery of the rotary table. In a vertical crusher that is transported along with an upward airflow supplied from an annular hot gas duct, the gas introduced into the hot gas duct is rotatable around a vertical axis inside the intake port of the hot gas duct and rectified in the direction of rotation of the rotary table. At least one bent guide vane is provided for this purpose.
【0009】[0009]
【作用】本発明の竪型粉砕機における熱ガスダクトの取
入口には回転テーブルの回転方向と同一の偏流を生じさ
せるガイドベーンを1個あるいは複数個配列し,しかも
,このガイドベーンを任意に竪軸回りに回動可能に設け
たので,導入ガス同志が熱ガスダクト内部で衝突するこ
ともなく,したがって渦の発生もなく円滑に流れて熱風
吹上通路へほぼ均等に上昇し分配される。この結果,熱
ガスダクト内の気体の圧力損失が少なく,粉砕後の粉粒
体も円周均等に上昇気流に乗って粉砕機上部に設置され
たセパレータへ向かうのでミル内圧力損失が少なく安定
的な粉砕が連続的に実施されるため粉砕効率が向上する
。[Operation] One or more guide vanes are arranged at the intake port of the hot gas duct in the vertical crusher of the present invention to produce a drifted flow in the same direction as the rotational direction of the rotary table. Since it is provided so as to be rotatable around the axis, the introduced gases do not collide with each other inside the hot gas duct, and therefore flow smoothly without the generation of vortices, rising almost evenly to the hot air blowing passage and being distributed. As a result, the pressure loss of the gas in the hot gas duct is small, and the powder and granules after pulverization also ride the rising airflow evenly around the circumference and head toward the separator installed at the top of the pulverizer, resulting in less pressure loss inside the mill and stable production. Since pulverization is carried out continuously, pulverization efficiency is improved.
【0010】0010
【実施例】以下,本発明の実施例を図面に基づいて詳細
に説明する。図1〜図3は本発明の実施例に係り,図1
は熱ガスダクトの斜視図,図2は図1II−II視の平
面図,図3は熱ガスダクト内を流れる気流を示す概略平
面図である。Embodiments Hereinafter, embodiments of the present invention will be described in detail with reference to the drawings. 1 to 3 relate to embodiments of the present invention, and FIG.
2 is a perspective view of the hot gas duct, FIG. 2 is a plan view taken along line II-II of FIG. 1, and FIG. 3 is a schematic plan view showing the airflow flowing inside the hot gas duct.
【0011】図において,円環状の熱ガスダクト32の
取入口30,30には各々図3に示すように回転テーブ
ルの回転方向(本実施例では時計回り)に屈曲して気流
に偏流を起こさせるガイドベーン50がほぼ中央の回転
軸50a回りに回動自在に複数個配列されて上下端の軸
受50b,50bに軸承されて取り付けられる。回転軸
50aの上端はリンク60にキー止めされ,さらに各リ
ンク60,60,…の他端は水平のコネクティングロッ
ド76に設けた長穴62を介してピン61でピン接合さ
れ,コネクティングロッド76は摺動環74,75に保
持されて軸方向にスライドできるように配設される。摺
動環74,75の中間には,内部に減速電動機によって
回転される3腕回転子71およびこれと当接する対角線
状に配置された2個の突起72,73を有するフレーム
70が連結されている。なお,ガイドベーン50は図3
に示すへの字形のほか,滑らかに湾曲する曲線形のもの
でも良い。In the figure, the intake ports 30 and 30 of the annular hot gas duct 32 are each bent in the direction of rotation of the rotary table (clockwise in this embodiment) as shown in FIG. 3 to cause a bias in the airflow. A plurality of guide vanes 50 are arranged so as to be rotatable around a substantially central rotating shaft 50a, and are supported and attached to bearings 50b, 50b at the upper and lower ends. The upper end of the rotating shaft 50a is keyed to a link 60, and the other end of each link 60, 60,... is pin-jointed with a pin 61 through an elongated hole 62 provided in a horizontal connecting rod 76. It is arranged so that it can be held by sliding rings 74 and 75 and slid in the axial direction. A frame 70 having a three-arm rotor 71 rotated by a reduction motor and two diagonally arranged protrusions 72 and 73 in contact with the three-arm rotor 71 is connected between the sliding rings 74 and 75. There is. Note that the guide vane 50 is shown in Figure 3.
In addition to the shape shown in , a smoothly curved curved shape may also be used.
【0012】以上のように構成された本発明の竪型粉砕
機1の作動について説明する。フレーム70内の減速電
動機に通電することにより,3腕回転子71は時計回り
に回転し,突起72の側面に当接して,これを右側に移
動せしめ,フレーム70とこれに接続されたコネクティ
ングロッド76は摺動環74,75を右側へ移動する結
果,各リンク60は時計回りに回動する。その後,短時
間フレーム70は停止するが,やがて3腕回転子71と
もうひとつの突起73の当接によりフレーム70は左側
へ移動し,リンク60は反時計回りにある角度回動する
。このようにして,リンク60と回転軸50aを介して
結合されたガイドベーン50の傾きを,熱ガスダクト3
2の気流の圧力損失が最も低くなる位置に選定して減速
電動機の通電を遮断する。その結果,熱ガスダクト32
内の気流は回転テーブルの回転方向の層流となってほぼ
均等に熱風吹上通路を上昇する。なお,粉砕機内の原料
の挙動については従来技術で説明したとおりであるので
説明を省略する。The operation of the vertical crusher 1 of the present invention constructed as described above will be explained. By energizing the reduction motor in the frame 70, the three-arm rotor 71 rotates clockwise, comes into contact with the side surface of the protrusion 72, moves it to the right, and connects the frame 70 and the connecting rod connected thereto. 76 moves the sliding rings 74 and 75 to the right, and as a result, each link 60 rotates clockwise. Thereafter, the frame 70 stops for a short time, but eventually the frame 70 moves to the left due to contact between the three-arm rotor 71 and another protrusion 73, and the link 60 rotates counterclockwise by a certain angle. In this way, the inclination of the guide vane 50 coupled to the link 60 via the rotating shaft 50a is controlled by the hot gas duct 3.
2, the position where the pressure loss of the airflow is the lowest is selected, and the deceleration motor is de-energized. As a result, the hot gas duct 32
The airflow inside becomes a laminar flow in the direction of rotation of the rotary table and rises almost evenly through the hot air blowing passage. Note that the behavior of the raw material inside the crusher is the same as described in the prior art, so the explanation will be omitted.
【0013】[0013]
【発明の効果】以上説明したように,本発明の竪型粉砕
機における熱ガスダクトには,取入口に回転可能なガイ
ドベーンを配列したので,熱ガスダクト内に流れる気流
には渦の発生は無く,回転テーブルと同一方向の整流さ
れた層流が形成されるので,圧力損失が少なく,かつ,
回転テーブルの外周にほぼ均等に上昇気流ができる。し
たがって,振動の少ない長期連続安定運転が確保され,
粉砕効率が向上する。[Effects of the Invention] As explained above, since rotatable guide vanes are arranged at the intake port of the hot gas duct in the vertical crusher of the present invention, there is no generation of vortices in the airflow flowing inside the hot gas duct. , a rectified laminar flow is formed in the same direction as the rotary table, so pressure loss is small and
An upward air current is created almost evenly around the outer circumference of the rotary table. Therefore, long-term continuous stable operation with little vibration is ensured.
Grinding efficiency is improved.
【図1】本発明の竪型粉砕機の実施例に係る熱ガスダク
トの斜視図である。FIG. 1 is a perspective view of a hot gas duct according to an embodiment of a vertical crusher of the present invention.
【図2】本発明の竪型粉砕機の実施例に係る熱ガスダク
トを示す図1II−II視の平面図である。FIG. 2 is a plan view taken from FIG. 1II-II showing a hot gas duct according to an embodiment of the vertical crusher of the present invention.
【図3】本発明の竪型粉砕機の実施例に係る熱ガスダク
ト内を流れる気流を示す概略平面図である。FIG. 3 is a schematic plan view showing airflow flowing in a hot gas duct according to an embodiment of the vertical crusher of 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】従来の竪型粉砕機の全体側断面図である。FIG. 5 is an overall side sectional view of a conventional vertical crusher.
【図6】従来の竪型粉砕機の熱ガスダクト内を流れる気
流を示す概略平面図である。FIG. 6 is a schematic plan view showing airflow flowing in a hot gas duct of a conventional vertical crusher.
1 竪型粉砕機 3A 回転テーブル 4 粉砕ローラ 30 取入口 32 熱ガスダクト 50 ガイドベーン 50a 回転軸 50b 軸受 60 リンク 61 ピン 62 長穴 70 フレーム 71 3腕回転子 72 突起 73 突起 74 摺動環 75 摺動環 76 コネクティングロッド 1 Vertical crusher 3A Rotary table 4 Grinding roller 30 Intake port 32 Hot gas duct 50 Guide vane 50a Rotating axis 50b bearing 60 Link 61 pin 62 Long hole 70 frame 71 3 arm rotor 72 Protrusion 73 Protrusion 74 Sliding ring 75 Sliding ring 76 Connecting rod
Claims (1)
回転自在な粉砕ローラを配置し,原料投入シュートを経
由して供給した原料を粉砕ローラに所定の粉砕圧力を与
えて回転テーブル上面と粉砕ローラ周面との間で粉砕し
,粉砕後の粉粒体を回転テーブル外周下部に配設した円
環状の熱ガスダクトより供給された上昇気流に随伴して
搬送する竪型粉砕機において,該熱ガスダクトの取入口
の内部に垂直軸回りに回動自在で導入ガスを回転テーブ
ルの回転方向に整流させるために屈曲したガイドベーン
を少なくとも1個以上配設したことを特徴とする竪型粉
砕機。Claim 1: A plurality of rotatable crushing rollers are arranged on the upper surface of the outer periphery of a rotary table, and a predetermined crushing pressure is applied to the raw material supplied through the raw material input chute to the crushing rollers to crush the raw material on the upper surface of the rotary table. In a vertical crusher, the powder and granules are crushed between the roller circumferential surface and transported along with an upward air current supplied from an annular hot gas duct placed at the lower part of the outer periphery of the rotary table. A vertical crusher characterized in that at least one guide vane is arranged inside an intake port of a gas duct and is rotatable around a vertical axis and bent in order to rectify introduced gas in the direction of rotation of a rotary table.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10224691A JP2839116B2 (en) | 1991-02-08 | 1991-02-08 | Vertical crusher |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10224691A JP2839116B2 (en) | 1991-02-08 | 1991-02-08 | Vertical crusher |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH04256449A true JPH04256449A (en) | 1992-09-11 |
JP2839116B2 JP2839116B2 (en) | 1998-12-16 |
Family
ID=14322256
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP10224691A Expired - Lifetime JP2839116B2 (en) | 1991-02-08 | 1991-02-08 | Vertical crusher |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2839116B2 (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006231112A (en) * | 2005-02-22 | 2006-09-07 | Babcock Hitachi Kk | Crushing machine |
WO2014109025A1 (en) * | 2013-01-09 | 2014-07-17 | 宇部興産機械株式会社 | Vertical crusher |
JP2015044150A (en) * | 2013-08-28 | 2015-03-12 | 宇部興産機械株式会社 | Vertical mill, and method for operating vertical mill |
JP2015044151A (en) * | 2013-08-28 | 2015-03-12 | 宇部興産機械株式会社 | Crushing system |
CN112058408A (en) * | 2020-07-30 | 2020-12-11 | 河南黎明重工科技股份有限公司 | Pressure balancing device for vertical roller mill |
-
1991
- 1991-02-08 JP JP10224691A patent/JP2839116B2/en not_active Expired - Lifetime
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006231112A (en) * | 2005-02-22 | 2006-09-07 | Babcock Hitachi Kk | Crushing machine |
WO2014109025A1 (en) * | 2013-01-09 | 2014-07-17 | 宇部興産機械株式会社 | Vertical crusher |
JPWO2014109025A1 (en) * | 2013-01-09 | 2017-01-19 | 宇部興産機械株式会社 | Vertical crusher |
JP2015044150A (en) * | 2013-08-28 | 2015-03-12 | 宇部興産機械株式会社 | Vertical mill, and method for operating vertical mill |
JP2015044151A (en) * | 2013-08-28 | 2015-03-12 | 宇部興産機械株式会社 | Crushing system |
CN112058408A (en) * | 2020-07-30 | 2020-12-11 | 河南黎明重工科技股份有限公司 | Pressure balancing device for vertical roller mill |
Also Published As
Publication number | Publication date |
---|---|
JP2839116B2 (en) | 1998-12-16 |
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