. . . . "RIV/00216275:25310/08:00007768" . . . "Separation of an aqueous solution of HCl+FeCl2 by anion-exchange membrane Neosepta-AFN was investigated in a conventional two-compartment cell. The experiments revealed that this membrane is a good separator for the mixture mentioned, ferrous chloride is efficiently rejected, while hydrochloric acid permeates well through the membrane. The separation is very efficient at low concentrations of ferrous chloride and high acid concentrations. The separation efficiency of the membrane was evaluated by the partial flux of ferrous chloride. The experiments showed that this partial flux is low, i.e. below 5.6 %. It decreases with an increasing acid concentration, but it increases with an increasing concentration of salt in the solution separated. Moreover, the separation process was quantified by the permeability of the membrane based on four concentration dependent phenomenological coefficients."@en . "Z(MSM0021627502)" . "Separation of HCl+FeCl2 Mixture by Anion-exchange Membrane" . "Proceedings of 18th International Congress of Chemical and Process Engineering" . . . . "[520DEA7AE425]" . . . . "Palat\u00FD, Zden\u011Bk" . "2008-08-28+02:00"^^ . "RIV/00216275:25310/08:00007768!RIV09-MSM-25310___" . "Praha" . . "Praha" . . . "Separation of HCl+FeCl2 Mixture by Anion-exchange Membrane" . "2"^^ . "394446" . "Separation of an aqueous solution of HCl+FeCl2 by anion-exchange membrane Neosepta-AFN was investigated in a conventional two-compartment cell. The experiments revealed that this membrane is a good separator for the mixture mentioned, ferrous chloride is efficiently rejected, while hydrochloric acid permeates well through the membrane. The separation is very efficient at low concentrations of ferrous chloride and high acid concentrations. The separation efficiency of the membrane was evaluated by the partial flux of ferrous chloride. The experiments showed that this partial flux is low, i.e. below 5.6 %. It decreases with an increasing acid concentration, but it increases with an increasing concentration of salt in the solution separated. Moreover, the separation process was quantified by the permeability of the membrane based on four concentration dependent phenomenological coefficients." . "diffusion dialysis; hydrochloric acid; ferrous chloride; anion-exchange membrane; batch cell"@en . "2"^^ . "Separation of HCl+FeCl2 Mixture by Anion-exchange Membrane"@en . . "\u010Cesk\u00E1 spole\u010Dnost chemick\u00E9ho in\u017Een\u00FDrstv\u00ED" . "Byla sledov\u00E1na separace vodn\u00E9ho roztoku HCl+FeCl2 v konven\u010Dn\u00ED dvoukomorov\u00E9 cele s anion-v\u00FDm\u011Bnnou membr\u00E1nou Neosepta-AFN. Experimenty uk\u00E1zaly, \u017Ee tato membr\u00E1na je pro danou sm\u011Bs dobr\u00FDm separ\u00E1torem, chlorid \u017Eeleznat\u00FD je membr\u00E1nou \u00FA\u010Dinn\u011B zadr\u017Eov\u00E1n, kde\u017Eto kyselina chlorovod\u00EDkov\u00E1 proch\u00E1z\u00ED membr\u00E1nou velmi snadno. Separace je velmi efektivn\u00ED p\u0159i n\u00EDzk\u00FDch koncentrac\u00EDch chloridu \u017Eeleznat\u00E9ho a vysok\u00FDch koncentrac\u00EDch kyseliny chlorovod\u00EDkov\u00E9. Separa\u010Dn\u00ED schopnost membr\u00E1ny byla posuzov\u00E1na na z\u00E1klad\u011B parci\u00E1ln\u00EDho toku chloridu \u017Eeleznat\u00E9ho. Experimenty uk\u00E1zaly, \u017Ee tento tok je mal\u00FD, tj. men\u0161\u00ED ne\u017E 5,6 %. Tok kles\u00E1 s rostouc\u00ED koncentrac\u00ED kyseliny, ale zvy\u0161uje se s rostouc\u00ED koncentrac\u00ED soli. Krom\u011B toho byl separa\u010Dn\u00ED proces kvantifikov\u00E1n permeabilitou membr\u00E1ny, kter\u00E1 byla vyj\u00E1d\u0159ena pomoc\u00ED \u010Dty\u0159 koncentra\u010Dn\u011B z\u00E1visl\u00FDch fenomenologick\u00FDch koeficient\u016F."@cs . . . "25310" . "Separace sm\u011Bsi HCl+FeCl2 anion-v\u00FDm\u011Bnnou membr\u00E1nou"@cs . "978-80-02-02047-9" . "Bendov\u00E1, Helena" . "Separace sm\u011Bsi HCl+FeCl2 anion-v\u00FDm\u011Bnnou membr\u00E1nou"@cs . . "Separation of HCl+FeCl2 Mixture by Anion-exchange Membrane"@en . "16"^^ .