TL;DR: In this article, design principles for fines flotation and challenges common "myths" about fines and flotation cells are presented. And several operations where the design principles have been successfully applied, and describes performance on a size-by-size mineralogical basis.
TL;DR: In this article, the effect of particle properties, such as particle/particle sliding friction coefficient and particle restitution coefficient, particle density and particle size, on the particle flow in IsaMill was analyzed in terms of velocity distribution, porosity distribution, collision frequency, collision energy and power draw.
TL;DR: In this paper, the particle and energy flows in representative examples of the equipment used in many grinding processes are examined, including a 36′ semi-autogenous mill used in primary grinding for mineral processing, a ball mill used for cement clinker grinding, a grinding table also used for cements, a tower mill used both in mineral processing and for industrial minerals and finally for an Isamill which is used for ultra-fine grinding in mining.
Abstract: Particle size reduction is a critical unit process in many industries including mineral processing, cement, food processing, pigments and industrial minerals and pharmaceuticals. The aim is to take large feed material and as efficiently as possible reduce the size of the particles to a target size range. Over time, a very large range of equipment has been developed to perform this for many materials and in many different conditions. Discrete element method (DEM) modelling is a computational tool that can allow detailed exploration of the particle flow and breakage processes within comminution equipment and can assist in developing a clearer and more comprehensive understanding of the detailed processes occurring within. In this paper, we examine the particle and energy flows in representative examples of the equipment used in many grinding processes. We study a 36′ semi-autogenous mill used in primary grinding for mineral processing, a ball mill used for cement clinker grinding, a grinding table also used for cement grinding, a tower mill used for fine grinding both in mineral processing and for industrial minerals and finally for an Isamill, which is used for ultra-fine grinding in mineral processing. Copyright
TL;DR: In this article, the authors proposed to optimize the media size and quality to reduce energy consumption by a factor of two or more in a coarse-grained mill using the Isamill or stirred media detritor.
Abstract: Fine grinding, to P80 sizes as low as 7 μm, is becoming increasingly important as mines treat ores with smaller liberation sizes. This grinding is typically done using stirred mills such as the Isamill or Stirred Media Detritor. While fine grinding consumes less energy than primary grinding, it can still account for a substantial part of a mill’s energy budget. Overall energy use and media use are strongly related to stress intensity, as well as to media size and quality. Optimization of grinding media size and quality, as well as of other operational factors, can reduce energy use by a factor of two or more. The stirred mills used to perform fine grinding have additional process benefits, such as polishing the mineral surface, which can enhance recovery.
TL;DR: In this article, a series of dry grinding tests were performed in a prototype horizontal stirred mill (42L) to investigate the effects of operating parameters such as stirrer speed, feed rate, media filling and ball size on grinding considering the degree of size reduction and the energy consumption.