Abstract

The ball mill has an energy efficiency of no more than 3.5 % (taking into account the measures taken to intensify the process of grinding the material). This is due to the imperfection of the design of the grinding unit, which consists in the fact that it is impossible to completely convert the mechanical energy accumulated by the grinding load into grinding energy (i.e., energy directly spent on the destruction of material particles). Most of the stored energy is converted into heat, noise, and vibration. The existing directions of intensification of the grinding process are as follows: improvement of the design, internal equipment of the cement mill; changes in the physical and chemical properties of the grinding medium; improvement of the grinding scheme. The authors of this article work in the direction of improving the internal equipment, which is reflected in the scientifically based selection of the range of grinding media for the fine grinding chamber, since the rational composition of the grinding load can significantly reduce the energy consumption of the grinding process. The authors continue to study the possibility of using a two-ball loading in a fine grinding chamber. This article provides a brief overview of the different ranges of two-ball grinding loadings, which differ from each other only in the range of grinding media. The possibility of a significant increase in the productivity of the mill when replacing the traditional grinding load with a rational two-ball is shown

Highlights

  • Полученные результаты для наглядности представлены в виде графической зависимости между данным показателем и ассортиментом использовавшейся во второй камере мельницы двухшаровой мелющей загрузки

  • The ball mill has an energy efficiency of no more than 3.5 %

  • This is due to the imperfection of the design of the grinding unit, which consists in the fact that it is impossible to completely convert the mechanical energy accumulated by the grinding load into grinding energy

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Summary

ХИМИЧЕСКАЯ ТЕХНОЛОГИЯ

Авторы данной статьи продолжают исследования по созданию оптимального по составу двухшаровой мелющей загрузки для камеры тонкого измельчения, позволяющей снизить энергоемкость всего процесса помола. 2), на данной стадии измельчения клинкера под номерами 4 и 5 также имеют одинаковые значения данного показателя – 58 %, в это же время образец No3 имеет самое низкое значение ΣR008 (48%), а образец No6 – наоборот обладает самым большим остяком на сите No008 равным 61%. Спустя 10 мин помола во второй камере остается только одна пара образцов, характеризующиеся одинаковыми значениями полного остатка на сите – это клинкера под номерами 2 и 4 (ΣR008 = 5,1 %), в данном случае у обоих образцов произошло уменьшение значения данного показателя примерно в 10 раз. У образцов под номерами 1; 2; 4 и 5 произошло снижение величины данного показателя примерно в 3,5; 2; 2,5 и 1,3 раза соответственно

МЗ V МЗ VI
Обозначение мелющей загрузки
Findings
БИБЛИОГРАФИЧЕСКИЙ СПИСОК
Full Text
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