A. Kachaev, V. Sevost'yanov, G. Chemerichko, T. Orehova
{"title":"分解器研磨腔内离心两相流动力学的数学描述","authors":"A. Kachaev, V. Sevost'yanov, G. Chemerichko, T. Orehova","doi":"10.34031/2071-7318-2024-9-2-70-79","DOIUrl":null,"url":null,"abstract":"Rational control of equipment operating modes in the production of building materials is possible only in the case of a mathematical description of various technological processes. The sequence of calculation methods for determining the design and technological parameters of grinding equipment makes it possible to numerically present the results of calculations of rational operating modes of the equipment. The study presents a mathematical description of the dynamics of a two-phase flow inside the grinding chamber of a disintegrator, with the help of which it is possible to determine the speed characteristics of its operating modes for materials with different physical and mechanical properties. The nature of the change in the tangential components of the velocities of the two-phase flow has been established: the range of the current radius of the grinding chamber Ri has been determined, at which the radial components of the velocities of the carrier flow and particles of the ground material continue to increase. As a result of mathematical modeling, it was confirmed that with an increase in the concentration of dust particles in the increasing volume of the grinding chamber, the value of the tangential component of the velocity of a dynamic two-phase flow decreases in relation to the maximum parameters at Ri = 0.15 m by an average of 15.5%. It has been determined that the maximum velocity values for the tangential component are in the limit of Ri = 0.1-0.15 m and are 131 m/s for air, and 127.5 m/s for an average suspended particle with dsr = 40 μm. In the process of developing a mathematical description, it was established that in the range Ri = 0.15 - 0.3 m the increase in the radial components of the velocities of the air carrier medium and the weighted average particle flow is about 14.5%, which, in turn, indicates an increase in the kinetic energy of the crushed particles during the movement of a dynamic two-phase flow from the center to the periphery of the grinding chamber of the disintegrator.","PeriodicalId":9367,"journal":{"name":"Bulletin of Belgorod State Technological University named after. V. G. Shukhov","volume":null,"pages":null},"PeriodicalIF":0.0000,"publicationDate":"2024-01-09","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"MATHEMATICAL DESCRIPTION OF THE DYNAMICS OF CENTRIFUGAL TWO-PHASE FLOW IN THE GRINDING CHAMBER OF A DISINTEGRATOR\",\"authors\":\"A. Kachaev, V. Sevost'yanov, G. Chemerichko, T. 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The nature of the change in the tangential components of the velocities of the two-phase flow has been established: the range of the current radius of the grinding chamber Ri has been determined, at which the radial components of the velocities of the carrier flow and particles of the ground material continue to increase. As a result of mathematical modeling, it was confirmed that with an increase in the concentration of dust particles in the increasing volume of the grinding chamber, the value of the tangential component of the velocity of a dynamic two-phase flow decreases in relation to the maximum parameters at Ri = 0.15 m by an average of 15.5%. It has been determined that the maximum velocity values for the tangential component are in the limit of Ri = 0.1-0.15 m and are 131 m/s for air, and 127.5 m/s for an average suspended particle with dsr = 40 μm. 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引用次数: 0
摘要
只有在对各种技术过程进行数学描述的情况下,才有可能对建筑材料生产中的设备运行模式进行合理控制。确定碾磨设备的设计和技术参数的一系列计算方法,使得以数字形式呈现设备合理运行模式的计算结果成为可能。该研究提出了分解机研磨腔内两相流动力学的数学描述,借助该描述可以确定具有不同物理和机械特性的材料的运行模式的速度特性。已确定两相流速度切向分量变化的性质:已确定研磨室当前半径 Ri 的范围,在该范围内,载流和研磨材料颗粒速度的径向分量继续增加。数学建模的结果证实,随着研磨室容积增大,粉尘颗粒浓度增加,动态两相流速度的切线分量值相对于 Ri = 0.15 米时的最大参数平均下降 15.5%。经测定,切向分量的最大速度值在 Ri = 0.1-0.15 m 的范围内,空气为 131 m/s,dsr = 40 μm 的平均悬浮颗粒为 127.5 m/s。在建立数学描述的过程中,确定了在 Ri = 0.15 - 0.3 m 的范围内,空气载体介质和加权平均颗粒流速度的径向分量增加了约 14.5%,这反过来又表明,在动态两相流从分解器研磨室的中心向外围移动的过程中,被粉碎颗粒的动能增加了。
MATHEMATICAL DESCRIPTION OF THE DYNAMICS OF CENTRIFUGAL TWO-PHASE FLOW IN THE GRINDING CHAMBER OF A DISINTEGRATOR
Rational control of equipment operating modes in the production of building materials is possible only in the case of a mathematical description of various technological processes. The sequence of calculation methods for determining the design and technological parameters of grinding equipment makes it possible to numerically present the results of calculations of rational operating modes of the equipment. The study presents a mathematical description of the dynamics of a two-phase flow inside the grinding chamber of a disintegrator, with the help of which it is possible to determine the speed characteristics of its operating modes for materials with different physical and mechanical properties. The nature of the change in the tangential components of the velocities of the two-phase flow has been established: the range of the current radius of the grinding chamber Ri has been determined, at which the radial components of the velocities of the carrier flow and particles of the ground material continue to increase. As a result of mathematical modeling, it was confirmed that with an increase in the concentration of dust particles in the increasing volume of the grinding chamber, the value of the tangential component of the velocity of a dynamic two-phase flow decreases in relation to the maximum parameters at Ri = 0.15 m by an average of 15.5%. It has been determined that the maximum velocity values for the tangential component are in the limit of Ri = 0.1-0.15 m and are 131 m/s for air, and 127.5 m/s for an average suspended particle with dsr = 40 μm. In the process of developing a mathematical description, it was established that in the range Ri = 0.15 - 0.3 m the increase in the radial components of the velocities of the air carrier medium and the weighted average particle flow is about 14.5%, which, in turn, indicates an increase in the kinetic energy of the crushed particles during the movement of a dynamic two-phase flow from the center to the periphery of the grinding chamber of the disintegrator.