Abstract
A new method is described for the separation of strong mineral acids from other species present in aqueous solutions, by liquid-liquid extraction. An extracted acid can be recovered by backwashing of the extractant phase with water at concentrations approaching those in the original solutions. Even higher concentrations may be obtained using common ion effects or temperature effects. Extractants consist of a strong organic acid and an amine dissolved in a carrier solvent. Both the organic acid and the amine are water insoluble, in free and in salt form. Extractant characteristics to satisfy the requirements of a given process are obtained through the selection of the acid and of the amine that form the extracting couple and adjustment of their molar ratio. Processes achievable include the separation and recovery of acids from mixtures of acids (e.g., recovery of H2SO4, H2SiF6, and H3PO4 from “wet process” phosphoric acid) and conversions by reaction in acid media (e.g. conversion of KCI to KNO3 by HNO3 with the recovery of concentrated HCI).
Original language | English |
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Pages (from-to) | 334-337 |
Number of pages | 4 |
Journal | Industrial and Engineering Chemistry Process Design and Development |
Volume | 21 |
Issue number | 2 |
DOIs | |
State | Published - 1 Apr 1982 |