Froth flotation of coal fines: The influence of turbulence on cell performance

The paper identifies two zones in a Leeds flotation cell. The ratio (13)of the dissipative forces and the interfacial tension force acting on a bubble and a solid particle are shown mathematically to be proportional to the square of the particle diameter for the quiescent zone and inversely proportional to the particle diameter for the turbulent zone. To locate the range of operation, correlations were established for the bubble diameter through photography and bubble counts. 13was found to be fairly constant in the particle size range 38 to 150 ",m, and the level of turbulence unlikely to affect the bubble-particle attachment and hence the beneficiation efficiency. This was verified in a series of flotation runs with a standard Leeds cell and a modified cell of twice the height to increase the capacity of the quiescent zone. A series of tests on the size range 300 to 600 ",m showed that the turbulence level had a marked effect on the cell performance through a relative improvement in the beneficiation efficiency due to the increased height of the cell. To identify the significant variables in the size range 38 to 150 ",m, a factorial design was carried out. Promoter dosage and particle size were found to be significant, aeration rate and impeler speed being insignificant at the 95 per cent confidence level. Multiple regression correlations were established for the recovery of organic material, mineral rejection, and beneficiation efficiency.