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    • 1. 发明公开
    • Method and apparatus for grinding material particles
    • 用于颗粒物质的研磨方法和装置。
    • EP0648538A2
    • 1995-04-19
    • EP94110112.3
    • 1994-06-29
    • KAWASAKI JUKOGYO KABUSHIKI KAISHACHICHIBU CEMENT CO., LTD.
    • Sawamura, SeisukeUeda, HiroshiSutou, KanzaburoMurata, Mitsuaki
    • B02C21/00B02C23/12
    • B02C23/12B02C21/002
    • A grinding apparatus includes a roller mill (10) in which material particles are pre-ground, a tube mill (40) connected to the roller mill (10) through a fluidized-bed-type classifying device (30) in which the material particles are classified in the sizes under control, and a circulation line (20) is connected between the classifying device (30) and the roller mill (10), wherein a fluidized portion of fine material component is fed into the tube mill (40), a remaining portion of not fed to the tube mill (40) is returned to the roller mill (10) through the circulation line (20) and the returned portion of the material component is again ground together with newly fed material particles in the roller mill (10). The fluidized-bed-type classifying device (30) is provided with a first chute (35) through which the fine material component is flowed out to the tube mill (40) and a second chute (36) connected to the circulation line through which the remaining material component is returned to the roller mill (10). The inner hollow space of the fluidized-bed-type classifying device is divided into an air introduction section (34) and a fluidized bed section (33) by a porous partition plate (32) arranged horizontally with inclination toward the second chute (36). The fluidized bed section (33) is communicated with both the tube mill (40) and the roller mill (10) and the air introduction section (34) is communicated with the material fluidizing fluid, such as air, of which a flow rate is controllable.
    • 2. 发明公开
    • Method and apparatus for grinding material particles
    • 用于研磨材料颗粒的方法和设备
    • EP0648538A3
    • 1995-10-11
    • EP94110112.3
    • 1994-06-29
    • KAWASAKI JUKOGYO KABUSHIKI KAISHACHICHIBU CEMENT CO., LTD.
    • Sawamura, SeisukeUeda, HiroshiSutou, KanzaburoMurata, Mitsuaki
    • B02C21/00B02C23/12
    • B02C23/12B02C21/002
    • A grinding apparatus includes a roller mill (10) in which material particles are pre-ground, a tube mill (40) connected to the roller mill (10) through a fluidized-bed-type classifying device (30) in which the material particles are classified in the sizes under control, and a circulation line (20) is connected between the classifying device (30) and the roller mill (10), wherein a fluidized portion of fine material component is fed into the tube mill (40), a remaining portion of not fed to the tube mill (40) is returned to the roller mill (10) through the circulation line (20) and the returned portion of the material component is again ground together with newly fed material particles in the roller mill (10). The fluidized-bed-type classifying device (30) is provided with a first chute (35) through which the fine material component is flowed out to the tube mill (40) and a second chute (36) connected to the circulation line through which the remaining material component is returned to the roller mill (10). The inner hollow space of the fluidized-bed-type classifying device is divided into an air introduction section (34) and a fluidized bed section (33) by a porous partition plate (32) arranged horizontally with inclination toward the second chute (36). The fluidized bed section (33) is communicated with both the tube mill (40) and the roller mill (10) and the air introduction section (34) is communicated with the material fluidizing fluid, such as air, of which a flow rate is controllable.
    • 本发明提供一种粉碎装置,其特征在于,具有:预先粉碎原料粒子的辊式粉碎机(10);通过流化床式分级装置(30)与辊式粉碎机(10)连接的管磨机(40) (30)和辊式粉碎机(10)之间连接循环管线(20),其中精细材料成分的流化部分被送入管磨机(40)中, 未输送到管磨机(40)的剩余部分通过循环管线(20)返回到辊式粉碎机(10),并且材料成分的返回部分再次与辊式粉碎机中新输入的材料颗粒一起被粉碎 (10)。 流化床式分级装置(30)具有第一滑槽(35)和第二滑槽(36),第一滑槽(35)通过该第一滑槽(35)流出到管磨机(40),循环管路 剩余的材料组分被返回到辊磨机(10)。 流化床型分级装置的内部中空空间通过水平向第二滑道(36)倾斜布置的多孔分隔板(32)分成空气引入部分(34)和流化床部分(33) 。 流化床部分33与管磨机40和辊磨机10两者连通,并且空气引入部分34与空气等物料流化流体连通, 可控。
    • 4. 发明公开
    • Cement clinker grinding method using vertical roller mill and apparatus thereof
    • 用于使用立式辊磨机磨碎水泥熟料的方法和装置
    • EP0858839A1
    • 1998-08-19
    • EP98102375.7
    • 1998-02-11
    • KAWASAKI JUKOGYO KABUSHIKI KAISHAChichibu Onoda Cement Corporation
    • Mitsuda, YoshihiroSawamura, SeisukeUeda, HiroshiAndo, FuminoriSutoh, KanzaburoMurata, MitsuakiTakayama, Akihiko
    • B02C15/00B02C23/12B02C23/18
    • B02C15/04B02C23/12B02C23/18B02C2015/002Y02P40/20
    • A method of grinding cement clinkers and a cement clinker grinding apparatus having a vertical roller mill (11) are provided. In the method, feed material is ground by a table (13) and rollers (16). Next, substantially all the resultant ground material is taken out from an underside of the table and then conveyed to a separator (37) for classifying the ground material by a bucket elevator (38). The resultant coarse powder (46) provided by the separator is returned to a center of the table. In grinding, an pressing force of each of the rollers onto the table is selected so that a roller pressure per full sectional area of the roller ranges from 10 to 15 kg/cm 2 . Further, a circulation quantity of the coarse powder to be returned to the vertical roller mill is selected from 100 to 300 % of the feed material charged into the center of the table. And the liquid of 0.5 to 3 % of the feed material to be ground such as water alone or a mixture of water and diethylene glycol is sprayed on the only frictional grinding zone (Z2) which is positioned outside a position where a relative speed between said table and each of said rollers is equal to zero, in the radial direction of said table. By spraying the liquid on the only frictional grinding zone (Z2), the materials are involved firmly between the table (13) and the roller (16) to form the layer of the ground materials, so that the vibration of the roller and table are restrained
    • 提供磨碎水泥熟料的方法和具有垂直滚磨机(11)水泥熟料研磨设备。 在该方法中,进料是由表(13)和辊子(16)接地。 接着,基本上所有所得地面材料的从在表中的下侧取出,然后输送到用于由斗式提升机(38)的地面材料进行分类的分离器(37)。 由分离器提供所得到的粗粉(46)返回到表中的一个中心。 在磨到走上被选择的表按压每个辊的力,从而确实从10至15千克/厘米<2>每辊范围的全截面面积的磨滚压力。 此外,粗粉末的循环量被返回到垂直滚磨机被从装入台的中心进料的100至300%选择。 和进料的0.5〜3%的液体被粉碎:例如单独的水或喷洒在其上的位置外侧的位置的唯一的磨擦碾磨区(Z2)的所有的水和二甘醇的混合物,其中所述之间的相对速度 表和每个所述滚轮是等于零,在所述表中的径向方向。 通过在仅磨擦碾磨区(Z2)喷射液体,所述材料涉及到的表(13)和所述辊(16),以形成研磨材料层之间牢固,所以没有辊与表的振动是 约束
    • 8. 发明公开
    • Fluidized-bed classifier
    • Wirbelbettsortierer
    • EP0801988A3
    • 1999-03-10
    • EP97106391.2
    • 1997-04-17
    • KAWASAKI JUKOGYO KABUSHIKI KAISHAChichibu Onoda Cement Corporation
    • Mitsuda, YoshihiroSawamura, SeisukeOkamura, RyuichiUeda, HiroshiAndo, FuminoriSutoh, KazaburoMurata, MitsuakiHirobe, Tsutomu
    • B03B4/00
    • B03B4/00
    • A fluidized-bed classifier has a vessel (20) defining a space divided into an upper fluidized-bed chamber (22) and a lower gas chamber (23) by a perforated dispersion plate (21) having the shape of a funnel. Rising currents of a gas, such as air, are blown through the dispersion plate (21) into the upper fluidized-bed chamber to produce a fluidized bed of a particulate material over the dispersion plate. The lower gas chamber (23) is divided into a first gas chamber (23a) and a second gas chamber (23b) by a partition plate (29). The gas is supplied into the first air chamber (23b) so that rising gas currents of a velocity necessary for fluidizing coarse particles contained in the particulate material red into the vessel are blown from the first air chamber (23a) through the dispersion plate (21) into the fluidized-bed chamber. The gas is supplied into the second air chamber(23b) so that rising gas currents of a velocity lower than the velocity of the rising gas currents blown from the first air chamber (23a) into the fluidized-bed chamber (22) are blown into the fluidized-bed chamber so that coarse particles contained in the particulate material are not fluidized and does not flow together with fine particles into a fine particle discharge chute (28).
    • 流化床分级器具有通过具有漏斗形状的穿孔分散板(21)限定分隔成上流化床室(22)和下气室(23)的空间的容器(20)。 诸如空气的气体的上升流通过分散板(21)吹入上流化床室,以在分散板上产生颗粒材料的流化床。 下部气室(23)通过隔板(29)分为第一气室(23a)和第二气室(23b)。 将气体供给到第一空气室(23b)中,使得将容纳在颗粒材料中的粗颗粒流入容器所需的速度的上升气流从第一空气室(23a)通过分散板(21)吹送 )进入流化床室。 将气体供给到第二空气室(23b)中,使得低于从第一空气室(23a)吹入流化床室(22)的上升气流速度的速度的上升气流被吹入 流化床室使得包含在颗粒材料中的粗颗粒不被流化,并且不与细颗粒一起流入细颗粒排出槽(28)。