Appreciable separations between divalent or trivalent salt solutions and corresponding mineral acids can be achieved by hyperfiltration of mixtures through loose ion-exchange membranes. Porous charged membranes allowing high rates of volume flow were prepared by cross-linking of polyamines into a porous collodion matrix or by reaction of polyamines with a chemically modified collodion matrix. Hyperfiltration of salt-acid mixtures through these membranes gave enrichment of acid in the product and concentration of salt in the feed. The gap between rejections was larger in hyperfiltration of mixtures than in hyperfiltration of separate solutions.