JP4301605B2 - Vertical roller crusher - Google Patents

Vertical roller crusher Download PDF

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Publication number
JP4301605B2
JP4301605B2 JP30623098A JP30623098A JP4301605B2 JP 4301605 B2 JP4301605 B2 JP 4301605B2 JP 30623098 A JP30623098 A JP 30623098A JP 30623098 A JP30623098 A JP 30623098A JP 4301605 B2 JP4301605 B2 JP 4301605B2
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Japan
Prior art keywords
rotary table
radius
grinding
crushing
center
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JP30623098A
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Japanese (ja)
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JP2000126634A (en
Inventor
賢一 宇ノ木
茂斉 堀江
孝雄 関本
慎治 松本
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Mitsubishi Heavy Industries Ltd
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Mitsubishi Heavy Industries Ltd
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Priority to JP30623098A priority Critical patent/JP4301605B2/en
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Description

【0001】
【発明の属する技術分野】
本発明は、セメント原料、セメントクリンカ、燃料用石炭等の粒塊状物を粉砕する竪型ローラ粉砕機に関するものである。
【0002】
【従来の技術】
図7は従来の竪型ローラ粉砕機に用いている回転テーブルの断面図を示す。
【0003】
同図に示すように、回転テーブル12が駆動装置によって水平面内で回転駆動され、この回転テーブル12上に複数の粉砕ローラ9が配置されている。各粉砕ローラ9は回転テーブル12上面の粉砕部12Aに押し付けられて同回転テーブル12の回転に伴って摩擦で回転されるようになっており、上方のシュートから回転テーブル12上に供給される原料の粒塊状物を粉砕する構成となっている。
【0004】
また、図7には、回転テーブル12上の被粉砕物の溜り状態(層厚H)及び粉砕後の粗粒・粗粉がダムリング12Bに溜まる状態を実験的に計測し、その結果をも図示している。
【0005】
【発明が解決しようとする課題】
このような従来の竪型ローラ粉砕機では、図7で示すように回転テーブル12上の被粉砕物層厚Hが大きいために、粉砕ローラ9の回転テーブル中央側での層押し分け動力が大きくなるという問題があった。また、粉砕ローラ9に過大な押し分け力が掛るため、同粉砕ローラ9の偏摩耗が激しく、粉砕ローラ9の寿命が短いという不具合があった。
【0006】
本発明では、竪型ローラ粉砕機の回転テーブル上の粉砕物層厚みを低減して粉砕ローラの過大な押し分け動力を低減させ、粉砕ローラの摩耗を低減させることを目的としている。
【0007】
【課題を解決するための手段】
請求項1に係る本発明は、水平面内で回転する回転テーブルと、同回転テーブル上面に凹状の粉砕部が形成され、同粉砕部に係合して配置された複数の粉砕ローラと、被粉砕物を回転テーブル上へ供給する供給シュートと、前記回転テーブルの外周部に取着されたリング状のダムリングとを具えた竪型ローラ粉砕機であって、前記回転テーブル上面の粉砕部形状が、回転テーブルの外周側より中央側の高さを高くして形成され、前記回転テーブル上面の粉砕部形状が、前記粉砕ローラの粉砕面の半径をRとすると、中央側の半径をRとし、外周側の半径をRとした場合に、R<R<Rの関係にあり、さらに、半径Rの中心点は半径R線上にあり、半径RとRの中心点は粉砕ローラの粉砕面の中心線上にあり、これらの半径R・R・Rを連続して結んだ曲線によって形成するものである。請求項の発明は、前記回転テーブルの中央部と粉砕開始点までの傾斜部に水平状の棚部を設けるものである。請求項の発明は、前記ダムリングの上面に、内側が低く外側が高い傾斜部を形成するものである。
【0008】
【発明の実施の形態】
以下、図1ないし図6に基づいて本発明に係る竪型ローラ粉砕機の実施の形態を詳細に説明する。
図1は粒塊状物の粉砕装置の一例として、竪型ローラ粉砕機の概念図を示すものである。
同図に示すように、回転テーブル2が駆動装置1によって水平面内で回転駆動され、この回転テーブル2上にローラ軸10で支持された複数の粉砕ローラ9が配置されている。各粉砕ローラ9は回転テーブル2上面の粉砕部に押し付けられて同回転テーブル2の回転に伴って摩擦で回転されるようになっており、シュート4から回転テーブル2上に供給される原料の粒塊状物を粉砕する構成となっている。
【0009】
また、図3に示すように回転テーブル2上面の粉砕部形状は、回転テーブルの外周側より中央側の高さを高くして形成してあるとともに、回転テーブル2の中央部2aと粉砕開始点2dまでの傾斜部2bに水平状の棚部2cを設けている。この棚部2cは回転テーブル2の一部平面を示す図6に図示の通り、傾斜部2b,粉砕部2e,ダムリング3と同様、回転テーブル2の全周に設けられている。なお、棚部2cは粉砕部側に若干下がる方向に傾斜して設けてもよい。
【0010】
次に、図1において、熱ガス入口5から高温の熱ガスが供給され、回転テーブル2外周部のスロット11から上向きに吹出され、粉砕後の粗粒・粗粉を上方に搬送し、同時に残りの粒塊状物がスロット11から落下して溢出粉砕物の排出シュート8から取り出される。一方、熱ガスによって上方へ搬送される前記粗粒・粗粉のうち、粗粒は直接回転テーブル2上へ戻され、粗粉は上昇ガス流によって乾燥室3から分級機7へ搬送され、分級後の粗粒は再び回転テーブル2上へ戻されて前記粗粒及び粗粉は再粉砕される。そして、分級後の微紛は熱ガスとともに頂部のガス排出口6から取り出される構成になっている。
【0011】
前記排出シュート8から取り出された溢出粉砕物は、図示しない輸送機によって上方へ運ばれ再びシュート4を経て機内へ循環されて粉砕される。
図4は、粉砕ローラ9の配置を示す平面図で、回転テーブル2上に3個の粉砕ローラ9が均等に配置されている状態を示しているが、粉砕ローラ9の個数は3個に限定されるものではなく、粉砕条件によって任意に選択すればよい。図5は、被粉砕物が回転テーブル2上に供給された時に、各粉砕ローラ9のローラ圧下部21へ噛み込まれる被粉砕物の流れを図示したものである。
【0012】
本実施例は、特に、従来の回転テーブルの粉砕部形状を改良したもので、回転テーブル2の外周側よりも中央側の高さを高くし、ダムリング3から溢出し易い傾斜部を設けた形状に構成したものである。
【0013】
回転テーブル2の粉砕部形状は、図に示すように、粉砕ローラ9の粉砕面の半径をとすると、中央側の半径をR、外周側の半径をRとした場合に、R<R<Rの関係にあり、さらに、半径Rの中心点は半径R線上にあり、半径Rと半径Rの中心点は粉砕ローラ9粉砕面の中心線上にあり、これらの半径R・R・Rを連続して結んだ曲線で粉砕部が形成されている。
【0014】
このように構成した粉砕部によれば、従来の粉砕部よりも中央側の高さが高くなり、また、粉砕ローラ9と回転テーブル2間の中央側のギャップが小さくなる。
【0015】
回転テーブル2の外周部には粉砕後の粗粒・粗粉の溢出しを抑制するダムリング3が固定されており、同ダムリング3の上面には、その内側が低く外側が高い傾斜部3aが形成されている。
【0016】
上記のように構成された竪型ローラ粉砕機によれば、回転テーブル2上に被粉砕物が供給されると、複数の粉砕ローラ9と回転テーブル2の粉砕部に噛み込まれて、原料の粒塊状物が粉砕される。
この時、回転テーブル2の外周側より中央側が高く、かつ、棚部2cが形成されているので、供給された粉砕物は、図3で示すように回転テーブル2中央側から外周側に向けて滑らかに移動し、その層厚hが平準化しつつ薄くなる。
【0017】
そして、回転テーブル2の回転に伴って粉砕物を噛み込みながら粉砕ローラ9が回転すると、粉砕部の層厚hが低くなっていることにより粉砕ローラは、押し分け動力が少なくて粉砕することができる。しかも押し分け動力が小さいため粉砕ローラ9の偏摩耗を少なくすることができる。
【0018】
また、粉砕ローラ9と回転テーブル2の中央側のギャップが小さくなるように粉砕部が形成されているので、回転テーブル2中央側での粉砕が増加し、中央側から外周側へと粉砕が進み粉砕効果が改善される。
【0019】
さらに、粉砕部で粉砕された粗粉・粗粒は回転テーブル2の外周側から押し出され、低くなったダムリング3及び傾斜部3aをスムーズに移動し、さらに外側に溢出すようになっており、回転テーブル外周側の粉砕物の層厚を薄くすることができ、粉砕部分を回転テーブル2の中央寄りにもってくることができる。
【0020】
【発明の効果】
本発明は、水平面内で回転する回転テーブルと、同回転テーブル上面に凹状の粉砕部が形成され、同粉砕部に係合して配置された複数の粉砕ローラと、被粉砕物を回転テーブル上へ供給する供給シュートと、前記回転テーブルの外周部に取着されたリング状のダムリンとを具えた竪型ローラ粉砕機であって、前記回転テーブル上面の粉砕部形状が、回転テーブルの外周側より中央側の高さを高くして形成したので、粉砕物の層厚が薄くなり、粉砕ローラの押し分け動力を大幅に低減することができると共に、粉砕ローラの寿命を長くすることができる。
【0021】
さらに、前記回転テーブル上面の粉砕部形状が、前記粉砕ローラの粉砕面の半径をRとすると、中央側の半径をRとし、外周側の半径をRとした場合に、R<R<Rの関係にあり、さらに、半径Rの中心点は半径R線上にあり、半径RとRの中心点は粉砕ローラの粉砕面の中心線上にあり、これらの半径R・R・Rを連続して結んだ曲線によって形成することで、粉砕ローラと回転テーブルの中央側のギャップがより小さくなり、回転テーブル中央側での粉砕が増加し、中央側から外周側へと粉砕が進み粉砕効果が改善される。
【0022】
また、前記回転テーブルの中央部と粉砕開始点までの傾斜部に水平状の棚部を設けているので、粉砕物の一部が棚部に溜まり、粉砕物の全量が一度に粉砕ローラに供給されず、粉砕ローラの負荷が平均化し過負荷状態を防ぐので、更なる粉砕ローラの長寿命化が図れる。
【0023】
また、前記ダムリングの上面に、内側が低く外側が高い傾斜部を形成したので、回転テーブル外周部から粉砕物が溢れ出し易くなり、回転テーブル外周側の層厚を低減させることができる。
【0024】
本発明による竪型ローラ粉砕機の試験結果によれば、粉砕動力が従来のものに比べて約1/3低減することが明らかになっている。
【図面の簡単な説明】
【図1】本発明の一実施形態に係る竪型ローラ粉砕機全体を示す概念図である。
【図2】本実施形態の回転テーブル上面の断面形状を示す断面図である。
【図3】本実施形態の回転テーブル上面での粉砕状態を示す断面図である。
【図4】本実施形態の粉砕ローラの配置を示す平面図である。
【図5】本実施形態の粉砕ローラのローラ圧下部での粉砕物の流れを示す平面図である。
【図6】本実施形態の回転テーブルを示す平面図である。
【図7】従来の回転テーブル上面での粉砕状態を示す断面図である。
【符号の説明】
2 回転テーブル
2a 中央部
2b 傾斜部
2c 棚部
2d 粉砕開始点
3 ダムリング
3a 傾斜部
4 供給シュート
9 粉砕ローラ
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a vertical roller pulverizer for pulverizing agglomerates such as cement raw materials, cement clinker, and coal for fuel.
[0002]
[Prior art]
FIG. 7 shows a sectional view of a rotary table used in a conventional vertical roller pulverizer.
[0003]
As shown in the figure, the rotary table 12 is driven to rotate in a horizontal plane by a driving device, and a plurality of crushing rollers 9 are arranged on the rotary table 12. Each crushing roller 9 is pressed against the crushing portion 12A on the upper surface of the rotary table 12 and is rotated by friction as the rotary table 12 rotates, and the raw material supplied onto the rotary table 12 from the upper chute. It is the structure which grind | pulverizes the granular lump.
[0004]
Further, FIG. 7 experimentally measures the accumulation state (layer thickness H) of the object to be crushed on the rotary table 12 and the state where coarse particles / coarse powder after pulverization accumulates in the dam ring 12B, and the result is also shown. It is shown.
[0005]
[Problems to be solved by the invention]
In such a conventional vertical roller pulverizer, since the layer thickness H of the object to be crushed on the rotary table 12 is large as shown in FIG. There was a problem of becoming. Further, since an excessive pushing force is applied to the pulverizing roller 9, there is a problem that the pulverizing roller 9 is heavily worn and the pulverizing roller 9 has a short life.
[0006]
An object of the present invention is to reduce the thickness of a pulverized material layer on a rotary table of a vertical roller pulverizer, to reduce excessive pushing power of the pulverizing roller, and to reduce wear of the pulverizing roller.
[0007]
[Means for Solving the Problems]
According to a first aspect of the present invention, there is provided a rotary table that rotates in a horizontal plane, a plurality of crushing rollers that are provided with a concave crushing portion formed on an upper surface of the rotating table, and that are disposed in engagement with the crushing portion, A vertical roller crusher comprising a supply chute for supplying a product onto a rotary table and a ring-shaped dam ring attached to the outer periphery of the rotary table, wherein the shape of the crushing part on the upper surface of the rotary table is It is formed by increasing the height of the center side from the outer peripheral side of the rotary table, crushing section shape of the rotating table top surface, and the radius of the grinding surface of the grinding rollers and R 2, the center side of the radius R 1 and, the radius of the outer periphery side when the R 3, have a relationship of R 1 <R 2 <R 3, furthermore, the center point of the radius R 1 is the radius R 2 line, the radius R 2 and R 3 The center point is on the center line of the grinding surface of the grinding roller. And it forms the curve connecting consecutively a radius R 1 · R 2 · R 3 of al. According to a second aspect of the present invention, a horizontal shelf is provided at the central portion of the rotary table and the inclined portion up to the pulverization start point. According to a third aspect of the present invention, an inclined portion having a lower inner side and a higher outer side is formed on the upper surface of the dam ring.
[0008]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, an embodiment of a vertical roller pulverizer according to the present invention will be described in detail with reference to FIGS. 1 to 6.
FIG. 1 is a conceptual diagram of a vertical roller pulverizer as an example of a pulverizer for agglomerates.
As shown in the figure, the rotary table 2 is rotationally driven in a horizontal plane by the driving device 1, and a plurality of pulverizing rollers 9 supported by a roller shaft 10 are arranged on the rotary table 2. Each crushing roller 9 is pressed against a crushing portion on the upper surface of the rotary table 2 and is rotated by friction as the rotary table 2 rotates, and the raw material particles supplied from the chute 4 onto the rotary table 2 are rotated. The lump is crushed.
[0009]
Further, as shown in FIG. 3, the shape of the pulverized portion on the upper surface of the rotary table 2 is formed such that the height on the central side is higher than the outer peripheral side of the rotary table, and the central portion 2a of the rotary table 2 and the pulverization start point. A horizontal shelf 2c is provided on the inclined portion 2b up to 2d. As shown in FIG. 6, which shows a partial plane of the rotary table 2, the shelf 2 c is provided on the entire circumference of the rotary table 2, as with the inclined portion 2 b, the pulverizing portion 2 e, and the dam ring 3. Note that the shelf 2c may be provided so as to be inclined in a direction slightly lowering toward the pulverization unit.
[0010]
Next, in FIG. 1, hot hot gas is supplied from the hot gas inlet 5 and blown upward from the slot 11 on the outer periphery of the rotary table 2, and the crushed coarse particles / coarse powder are conveyed upward, while remaining The agglomerates fall from the slots 11 and are taken out from the discharge chute 8 for the spilled spilled material. On the other hand, among the coarse particles / coarse powder conveyed upward by the hot gas, the coarse particles are directly returned onto the rotary table 2, and the coarse powder is conveyed from the drying chamber 3 to the classifier 7 by the rising gas flow, and classified. The later coarse particles are returned to the rotary table 2 again, and the coarse particles and the coarse powder are pulverized again. And the fine powder after classification is taken out from the top gas discharge port 6 together with the hot gas.
[0011]
The overflow pulverized material taken out from the discharge chute 8 is conveyed upward by a transport machine (not shown), and is circulated again into the machine via the chute 4 and crushed.
FIG. 4 is a plan view showing the arrangement of the crushing rollers 9 and shows a state in which three crushing rollers 9 are evenly arranged on the rotary table 2. However, the number of crushing rollers 9 is limited to three. What is necessary is just to select arbitrarily by grinding | pulverization conditions. FIG. 5 illustrates the flow of the pulverized material that is bitten into the roller pressure lower portions 21 of the pulverizing rollers 9 when the pulverized material is supplied onto the rotary table 2.
[0012]
In this embodiment, in particular, the shape of the pulverized portion of the conventional rotary table is improved. The height of the central side is made higher than the outer peripheral side of the rotary table 2, and an inclined portion that easily overflows from the dam ring 3 is provided. It is configured in a shape.
[0013]
Crushing section shape of the rotary table 2, as shown in FIG. 2, the radius of the grinding surface of the grinding roller 9 When R 2, the radius of the central side R 1, the radius of the outer periphery side when the R 3 , R 1 <R 2 <R 3 , and the center point of the radius R 1 is on the radius R 2 line, and the center points of the radius R 2 and the radius R 3 are on the center line of the grinding roller 9 grinding surface. In addition, the pulverized portion is formed by a curve obtained by continuously connecting these radii R 1 , R 2, and R 3 .
[0014]
According to the pulverization unit configured as described above, the height on the center side is higher than that of the conventional pulverization unit, and the central gap between the pulverization roller 9 and the rotary table 2 is reduced.
[0015]
A dam ring 3 that suppresses the overflow of coarse particles and coarse powder after pulverization is fixed to the outer peripheral portion of the rotary table 2, and the upper surface of the dam ring 3 has an inclined portion 3 a that is low on the inside and high on the outside. Is formed.
[0016]
According to the vertical roller pulverizer configured as described above, when an object to be pulverized is supplied onto the rotary table 2, the pulverized portions of the pulverizing rollers 9 and the rotary table 2 are engaged with each other. The agglomerates are crushed.
At this time, since the central side is higher than the outer peripheral side of the rotary table 2 and the shelf portion 2c is formed, the supplied pulverized material is directed from the central side of the rotary table 2 toward the outer peripheral side as shown in FIG. It moves smoothly, and its layer thickness h becomes thinner while leveling.
[0017]
When the crushing rollers 9 while biting the ground product with the rotation of the rotary table 2 rotates, grinding roller 9 by a layer thickness h of the crushing portion is low, be thrust through ground less power it can. In addition, since the pushing power is small, uneven wear of the grinding roller 9 can be reduced.
[0018]
Further, since the pulverizing portion is formed so that the gap between the pulverizing roller 9 and the central side of the rotary table 2 is reduced, the pulverization at the central side of the rotary table 2 increases, and the pulverization proceeds from the central side to the outer peripheral side. The crushing effect is improved.
[0019]
Furthermore, the coarse powder and coarse particles pulverized in the pulverizing part are pushed out from the outer peripheral side of the rotary table 2 and smoothly move through the lowered dam ring 3 and the inclined part 3a and overflow further outward. The layer thickness of the pulverized material on the outer peripheral side of the rotary table can be reduced, and the pulverized portion can be brought closer to the center of the rotary table 2.
[0020]
【The invention's effect】
The present invention relates to a rotary table that rotates in a horizontal plane, a plurality of pulverizing rollers that are provided with a concave pulverizing portion formed on the upper surface of the rotating table, and arranged to engage with the pulverizing portion, and an object to be crushed on the rotary table. A vertical roller crusher comprising a supply chute to be fed to and a ring-shaped damlin attached to the outer peripheral portion of the rotary table, wherein the shape of the pulverized portion on the upper surface of the rotary table is the outer peripheral side of the rotary table Since the height on the center side is made higher, the layer thickness of the pulverized product is reduced, the pushing power of the pulverizing roller can be greatly reduced, and the life of the pulverizing roller can be extended.
[0021]
Further , when the radius of the grinding surface of the grinding roller is R 2 , the shape of the grinding part on the upper surface of the rotary table is R 1 <R 1 <when the center radius is R 1 and the outer radius is R 3. R 2 <R 3 , and the center point of the radius R 1 is on the radius R 2 line, and the center points of the radii R 2 and R 3 are on the center line of the grinding surface of the grinding roller. By forming a curved line continuously connecting R 1 , R 2, and R 3 , the gap on the center side of the crushing roller and the rotary table becomes smaller, and crushing on the center side of the rotary table increases. Grinding progresses toward the outer periphery, and the grinding effect is improved.
[0022]
In addition, since a horizontal shelf is provided at the central part of the rotary table and the inclined part to the pulverization start point, a part of the pulverized material is collected on the shelf, and the entire amount of the pulverized material is supplied to the pulverization roller at once. Since the load on the grinding roller is averaged and an overload state is prevented, the life of the grinding roller can be further extended.
[0023]
In addition, since an inclined portion having a low inside and a high outside is formed on the upper surface of the dam ring, the pulverized material easily overflows from the outer peripheral portion of the rotary table, and the layer thickness on the outer peripheral side of the rotary table can be reduced.
[0024]
According to the test results of the vertical roller pulverizer according to the present invention, it is clear that the pulverization power is reduced by about 1/3 compared with the conventional one.
[Brief description of the drawings]
FIG. 1 is a conceptual diagram showing an entire vertical roller crusher according to an embodiment of the present invention.
FIG. 2 is a cross-sectional view showing a cross-sectional shape of an upper surface of a turntable according to the present embodiment.
FIG. 3 is a cross-sectional view showing a pulverized state on the upper surface of the rotary table of the present embodiment.
FIG. 4 is a plan view showing the arrangement of crushing rollers of the present embodiment.
FIG. 5 is a plan view showing the flow of the pulverized material at the lower roller pressure of the pulverizing roller of the present embodiment.
FIG. 6 is a plan view showing a turntable of the present embodiment.
FIG. 7 is a cross-sectional view showing a pulverized state on the upper surface of a conventional rotary table.
[Explanation of symbols]
2 Rotary table 2a Central part 2b Inclined part 2c Shelf part 2d Grinding start point 3 Dam ring 3a Inclined part 4 Supply chute 9 Grinding roller

Claims (3)

水平面内で回転する回転テーブルと、同回転テーブル上面に凹状の粉砕部が形成され、同粉砕部に係合して配置された複数の粉砕ローラと、被粉砕物を回転テーブル上へ供給する供給シュートと、前記回転テーブルの外周部に取着されたリング状のダムリングとを具えた竪型ローラ粉砕機であって、前記回転テーブル上面の粉砕部形状が、回転テーブルの外周側より中央側の高さを高くして形成され、前記回転テーブル上面の粉砕部形状が、前記粉砕ローラの粉砕面の半径をRとすると、中央側の半径をRとし、外周側の半径をRとした場合に、R<R<Rの関係にあり、さらに、半径Rの中心点は半径R線上にあり、半径RとRの中心点は粉砕ローラの粉砕面の中心線上にあり、これらの半径R・R・Rを連続して結んだ曲線によって形成されていることを特徴とする竪型ローラ粉砕機。 A rotating table that rotates in a horizontal plane, a concave crushing portion is formed on the top surface of the rotating table, a plurality of crushing rollers arranged to engage with the crushing portion, and a supply for supplying an object to be crushed onto the rotating table A vertical roller crusher comprising a chute and a ring-shaped dam ring attached to the outer peripheral portion of the rotary table, wherein the shape of the pulverized portion on the upper surface of the rotary table is more central than the outer peripheral side of the rotary table is formed by increasing the height, crushing section shape of the rotating table top surface, and the radius of the grinding surface of the grinding rollers and R 2, the center side of the radius and R 1, the radius of the outer circumference side R 3 R 1 <R 2 <R 3 , the center point of the radius R 1 is on the radius R 2 line, and the center points of the radii R 2 and R 3 are on the grinding surface of the grinding roller. is on the center line, these radii R 1 · R 2 · Vertical roller mills you characterized by being formed by a curve connecting 3 the continuously. 前記回転テーブルの中央部と粉砕開始点までの傾斜部に水平状の棚部を設けることを特徴とする請求項1記載の竪型ローラ粉砕機。Vertical roller grinding machine of claim 1 Symbol placement and providing a horizontal-like ledge on the inclined portion to the center portion and the grinding start point of the rotary table. 前記ダムリングの上面に、内側が低く外側が高い傾斜部を形成したことを特徴とする請求項1記載の竪型ローラ粉砕機。Wherein the upper surface of the dam ring, vertical roller mills of claim 1 Symbol mounting, characterized in that the inner forming an outer high slope portion lower.
JP30623098A 1998-10-28 1998-10-28 Vertical roller crusher Expired - Fee Related JP4301605B2 (en)

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DE102009015037B4 (en) * 2009-03-26 2011-03-31 Loesche Gmbh roller mill
JP2016140854A (en) * 2015-02-05 2016-08-08 三菱日立パワーシステムズ株式会社 Carbon-containing solid fuel supply apparatus, carbon-containing solid fuel pulverization apparatus, and carbon-containing solid fuel pulverization apparatus control method

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