Тип публикации: статья из журнала

Год издания: 2011

Ключевые слова: anion exchangers, chloride solutions, Chloride-sulfate solutions, sorption, 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-sulfПоказать полностьюate systems were investigated at molar ratios of HCl:H2SO4 = 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. © 2011 Elsevier B.V. All rights reserved.

Журнал: Desalination

ISSN журнала: 00119164

Издатель: Elsevier Science Publishing Company, Inc.

• Kononova O.N. (Department of Chemistry, Siberian Federal University, Svobodny Pr. 79, 660041 Krasnoyarsk, Russian Federation)
• Mikhaylova N.V. (Department of Chemistry, Siberian Federal University, Svobodny Pr. 79, 660041 Krasnoyarsk, Russian Federation)
• Melnikov A.M. (Department of Chemistry, Siberian Federal University, Svobodny Pr. 79, 660041 Krasnoyarsk, Russian Federation)
• Kononov Y.S. (Institute of Chemistry and Chemical Technology, Siberian Department of the Russian Academy of Science, Karl Marx Pr. 42, 660049 Krasnoyarsk, Russian Federation)

• Ядро РИНЦ (eLIBRARY.RU)