IWS designs and manufactures the LIQUAREX (tm) range of decentralised Water and Wastewater Treatment Systems


Mineral Processing

Fluorine technology - breakthrough in recovery of precious metals from minerals

The growing demand for new technologies capable of producing high quality end products at low cost with minimal impact on the environment, has led to IWS from New Plymouth to create a new approach to processing minerals.

The new F-process (patent pending) is based on the ability of a number of elements to form volatile salts after their reaction with a fluorine-bearing agent. The volatilized salts then undergo selective condensation, producing high purity metal oxides (> 99.9%).

Of special interest is the recovery of the silicon and titanium oxides from refractory minerals containing precious and/or rare metals. At the initial stages of the process, fluorination causes liberation of precious metals (quartz, ilmenite, etc. - see schematic). The volatilized silicon and titanium are then converted to valuable oxides, while the non-fluorinated residue undergoes further refining to produce the precious/rare metals fraction. Additionally, the process allows recovery of a high purity metallic iron.

The major advantages of the F-technology are as follows:

  • Process is continuous and can be easily automated;
  • Involves relatively low temperature (<700 °C) and minimal number of steps;
  • Not sensitive to particle size of the raw material;
  • Active reagent is easy to handle and is reused in the process;
  • Waste free.

The following example will explain the above in more detail:

A sample of the ore made up of separate mineral ingredients was taken for processing with the following characteristics:

   

click to enlarge

  • Fraction size: 0.5 - 3.0 mm;
  • Major oxides content: 58% Fe2O3; 26% SiO2; 6% CaO; 6% AI2O3;
  • Gold content: 13.9 g/t (locked in quartz).
1000 g of this ore underwent magnetic separation, producing 432 g of the silicate fraction with 31.9 g/t of gold, and 568 g magnetics. The silicate part was F-processed, yielding 244 g of silicone dioxide(> 99.9%) and also 95 g of non-fluorinated residue with 145.7 g/t of gold. The residue was then treated with the halide solution, producing 13.5 mg of the dissolved metal. The extraction rate reported was 97.1% at the power consumption of 2.4 kWhr per 1 kg of ore.

Previous page: Conclusions
Next page: Projects