Тип публикации: статья из журнала
Год издания: 2011
Идентификатор DOI: 10.1016/j.desal.2011.02.005
Ключевые слова: Sorption, Zinc, Anion exchangers, Chloride solutions, Chloride-sulfate solutions, Anion exchangers, Chloride solutions, Chloride-sulfate solutions, Sorption, Zinc, Anion exchangers, Chemical structure, Chloride solutions, Chloride-sulfate solutions, Industrial solutions, Initial solution, Kinetic properties, Molar ratio, Purolite, Sulfate solutions, Sulfate system, Zinc concentration, Zinc ions, Zinc recovery, Zinc removal, Chlorine compounds, Ion exchange, Ion exchange resins, Ions, Recovery, Sewage, Sorption, Wastewater, Zinc, Zinc compounds, Hydrochloric acid, aqueous solution, chloride, ion exchange, reaction kinetics, sulfate, zinc
Аннотация: The present work is focused on sorption recovery of zinc (II) ions from chloride and chloride-sulfate solutions on some commercial anion exchangers with different physical and chemical structures. Initial zinc concentration was 1.0-5.0 mmol/L HCl concentration in initial solutions was from 0.001 to 4.0 mol/L, whereas chloride-sulfate systems were investigated at molar ratios of HCl:H(2)SO(4)=1:1; 1:2 and 1:4. Acids concentrations were 0.001 and 2.0 mol/L It was shown that the anion exchangers investigated possess good sorption and kinetic properties. After ion exchange recovery, zinc was effectively eluted by means of 2 M HCl. The elution results in complete zinc removal from the sorbents investigated and complete purification of solutions from zinc. Based on the data obtained, the anion exchangers Purolite S 985, Purolite A 500 and AM-2B can be recommended for zinc recovery from industrial solutions and waste water. (C) 2011 Elsevier B.V. All rights reserved.
Выпуск журнала: Vol. 274, Is. 01.03.2017
Номера страниц: 150-155
ISSN журнала: 00119164
Место издания: AMSTERDAM
Издатель: ELSEVIER SCIENCE BV
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