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Regeneration of tri-octyl phosphine oxide solutions used to extract phenol from water

Technical Report ·
OSTI ID:5745763
Several potential extractant diluents were examined. Distillation was investigated for regenerating tri-octylphosphine oxide solutions loaded with phenol. Relative volatilities of phenol to the diluent were measured for the diluents isobutyl-heptyl ketone and dimethylnaphthalene, at both varying solute-to-extractant mole ratios and extractant concentrations in the solvent. A simple model based on the chemical complexation between the solute and extractant is proposed. The equilibrium constant for this reaction was determined to be roughly 5 L/gmole. Equilibrium distribution coefficients were also measured for the extraction of phenol from both pure water and coal-gasification condensate water, by a mixed TOPO solvent having acceptable regeneration capabilities. These data are consistent with the extraction mechanism model previously proposed by MacGlashan (1982). Losses of the extractant into the aqueous raffinates are also reported. Both the observed high distribution coefficients at low solute-to-extractant mole ratios, and the low relative volatilities indicate that the association between phenol and TOPO is strong. Hence, a high boiling diluent is needed for favorable regeneration via distillation. TOPO-based solvent extraction appears to be best suited for treatment of aqueous solutions having phenol concentrations on the order of 100 parts per million.
Research Organization:
Lawrence Berkeley Lab., CA (USA)
DOE Contract Number:
AC03-76SF00098
OSTI ID:
5745763
Report Number(s):
LBL-16577; ON: DE84000938
Country of Publication:
United States
Language:
English