Liquid-liquid extraction of phosphorus from sulfuric acid solution using benzyl dimethyl amine

This study addresses the liquid-liquid extraction behavior of phosphorus from a sulfuric acid solution using benzyl dimethyl amine (BDMA) in kerosene. The extraction equilibria investigated with varied BDMA concentrations could reveal the formation of 3[BDMA].[H3PO4] over bar complex in the organic phase. The thermodynamic properties determined at various temperatures indicated that the process was exothermic with a calculated enthalpy (Delta H-circle minus) of -24.0 kJ.mol(-1). The organic-to-aqueous phase (O/A) volume ratio was varied to elucidate the quantitative extraction of phosphorus. The McCabe-Thiele diagram plotted for the extraction isotherm was validated for the requirement of three counter-current stages in the extraction at an O/A volume ratio of 2.0/3.5. The back-extraction of phosphorus from the loaded organic phase was quantitatively achieved by contacting 4.0 mol.L-1 H2SO4 solution in three stages of counter-current contact at an O/A volume ratio of 3/2. This study can be applied to remove phosphorus from the sulfuric acid leach solutions of monazite processing, and many other solutions.

Automated summary

This study investigates the liquid-liquid extraction behavior of phosphorus from a sulfuric acid solution using BDMA in kerosene, demonstrating the formation of a 3[BDMA].[H3PO4] over bar complex in the organic phase. Thermodynamic properties show that the extraction process is exothermic, and the McCabe-Thiele diagram confirms the need for three counter-current stages in the extraction at a specific O/A volume ratio. Additionally, quantitative back-extraction of phosphorus from the loaded organic phase is achieved by contacting H2SO4 solution in three stages of counter-current contact at a specific O/A volume ratio.