Phosphate beneficiation process using methyl or ethyl esters as float oils
View Patent ↗A process for use in a phosphate ore beneficiation process to minimize the long-term environmental impact of the use of petroleum based hydrocarbon materials mixed with fatty acid based primary floatation reagents for froth flotation in the flotation of phosphate ores, wherein the process comprises substituting the petroleum based hydrocarbon materials with methyl and/or ethyl esters of fatty acids.
1. In a phosphate ore beneficiation process, a method for minimizing the long-term environmental impact of the use of petroleum based hydrocarbon materials mixed with fatty acid based anionic flotation reagents for froth flotation in the flotation of phosphate ores, the method comprising:
substituting said petroleum based hydrocarbon materials with methyl and/or ethyl esters of fatty acids and wherein the methyl and/or ethyl esters of fatty acids are blended with fatty acid based primary flotation reagents in a proportional ratio of from about 25:75 to 75:25.
2. The method according to claim 1 , wherein the esters of fatty acids are derived from:
an oil obtained from one of rapeseed, sunflower, corn, safflower, soybean, and fatty acids obtained from said oils;
tall oil derived fatty acids including heads and crude tall oil;
and combinations thereof.
3. The method according to claim 1 , wherein the methyl or ethyl esters and combinations thereof are derived from animal, plant and synthetic materials.
4. The method according to claim 2 , wherein when the fatty acid is a crude tall oil and residual rosin acids interfere with the flotation process, said residual rosin acids remaining after esterification are reacted with an alkaline earth base in stoichiometric quantities to neutralize the acid.
5. The method according to claim 4 , wherein when an increase in viscosity occuring by the neutralization process is undesirable, a desired proportion of non-crude tall oil derived methyl or ethyl ester is added to reduce the viscosity to an acceptable level.
6. The method according to claim 1 , wherein the blended esters and reagents are added to a deslimed and sized phosphate rock slurry at a level normally about 0.3 to 3.0 pounds per ton of dry feed.