Selective transport of attached particles across the froth phase

Over many years, researchers in the field of flotation have developed an in-depth understanding of processes occurring in the pulp phase of flotation machines. Until recently, however, the froth phase has received little attention. The froth phase serves to separate bubble-particle aggregates from suspended slurry in a flotation cell. The mechanism of recovery by entrainment, its relationship to water recovery and particle size dependency is well understood. Froth recovery, (the fraction of particles entering the concentrate launder that entered the froth phase attached to air bubbles), is not well understood. Up until now, there has been doubt over whether this property is dependent on particle size and hydrophobicity. Difficulties in measuring froth recovery had previously prevented researchers from gaining a deeper understanding of the transport of attached particles across the froth phase. A novel device was designed and tested to measure froth recovery by isolating bubble-particle aggregates in the pulp-phase of flotation machines through the determination of the bubble loading in the pulp phase (mass of particles attached per unit volume of air bubbles). This technique can be used with other measurements to investigate froth selectivity by directly comparing these captured particles to those found in the froth phase. Evidence was collected at Red Dog Mine, Alaska and Newmont Golden Grove Operations, Western Australia which showed that the froth phase selectively transported more hydrophobic and smaller sized particles across the froth than less hydrophobic and larger particles. Particles collected in the device were compared to those found in the concentrate stream on a size by mineral by liberation class. Froth recovery was also calculated on a size by mineral by liberation class for two valuable sulphide minerals in a continuous 3m³ flotation cell. These results show that the froth phase is responsible for the upgrading of attached particles across the froth phase as well as for the separation of bubble-particle aggregates from suspended slurry. The pulp phase is responsible for creating bubble-particle aggregates through the attachment of hdyrophobic mineral particles to air bubbles. Many complex factors affect the extent to which this occurs including the size and hdyrophobicity of the particles, the size and number of air bubbles produced by the flotation machine, the rate of collisions between particles and bubbles and the overall chemistry of the system. This measurement of bubble loading presents an opportunity to measure the impact of all these factors on the successful creation of bubble-particle aggregates. Based on a literature review suggesting that there was a high probability of particles being detached at the pulp-froth interface due to the aggregates change in momentum, a three phase description of a flotation cell was proposed. The three phases were: pulp, pulp-froth interface and upper froth zones. A second froth recovery measurement technique (changing froth depth) was used in combination with the bubble load technique to determine the recovery across each of the two froth zones. It was found that the pulp-froth interface appears to be responsible for the selectivity observed across the froth phase as a whole. These findings will enable more in-depth research into the sub-process of the froth phase as well as assisting flotation cell design through a better understanding of the roles of the pulp-froth interface and the upper froth region