This paper examines Ni(II) and Co(II) adsorption from an aqueous sulfate solution onto Lewatit TP-260 ion exchange resin, and the later desorption of these ions. The influence on metals adsorption of contact time, the pH of the metal-containing solution, the initial concentration of metals in the solution, and the amount of resin was examined in batch experiments. The coefficients of adsorption under different experimental conditions were then determined. Batch experiments were also performed to examine desorption or elution at different volumes/resin ratios and HCl (eluant) concentrations. Adsorption experiments were also performed in minicolumns to study the performance of the resin under conditions of continuous use. Different flo...
In this sixth part of the series, Manganese(II) was removed from aqueous solutions by the cationic e...
The adsorption of Ni (II) from nickel electro plating rinse water has been attempted. Indion 225 and...
The removal of nickel from aqueous solutions under different experimental conditions using a Ceralit...
This paper examines Ni(II) and Co(II) adsorption from an aqueous sulfate solution onto Lewatit TP-26...
This article describes the ion exchange of a heavy metal Ni(II) from aqueous solutions onto a Dowex ...
The cationic exchange resin Dowex C400 was used to remove nickel(II) from aqueous solutions of diffe...
Heavy metals are among the most inorganic hazardous pollutants. Therefore, the removal of metal ions...
A comparative study on the adsorption of zinc(II) and cobalt(II) from aqueous solutions onto Indion ...
Zinc(II) was removed, from aqueous solutions, by the ion exchange resin Lewatit OC-1026 (having di-2...
13-20The recovery and removal of Ni(II) by macroporous weak acid resin (D151 resin) have been inves...
Thesis (MTech (Chemical Engineering)--Cape Technikon, Cape Town, 1998Ion exchange resins are widely ...
Iron(II) was removed from aqueous solutions by the use of the cationic ion exchange resin Lewatit TP...
Equilibrium distributions of cobalt(II), nickel(II), zinc(II), cadmium(II), and copper(II) have been...
The adsorption of Ni(II) with D301R resin was investigated in this paper. The results showed that th...
This study aims to establish the potential of an iminodiacetic-based chelating resin (Purolite S930)...
In this sixth part of the series, Manganese(II) was removed from aqueous solutions by the cationic e...
The adsorption of Ni (II) from nickel electro plating rinse water has been attempted. Indion 225 and...
The removal of nickel from aqueous solutions under different experimental conditions using a Ceralit...
This paper examines Ni(II) and Co(II) adsorption from an aqueous sulfate solution onto Lewatit TP-26...
This article describes the ion exchange of a heavy metal Ni(II) from aqueous solutions onto a Dowex ...
The cationic exchange resin Dowex C400 was used to remove nickel(II) from aqueous solutions of diffe...
Heavy metals are among the most inorganic hazardous pollutants. Therefore, the removal of metal ions...
A comparative study on the adsorption of zinc(II) and cobalt(II) from aqueous solutions onto Indion ...
Zinc(II) was removed, from aqueous solutions, by the ion exchange resin Lewatit OC-1026 (having di-2...
13-20The recovery and removal of Ni(II) by macroporous weak acid resin (D151 resin) have been inves...
Thesis (MTech (Chemical Engineering)--Cape Technikon, Cape Town, 1998Ion exchange resins are widely ...
Iron(II) was removed from aqueous solutions by the use of the cationic ion exchange resin Lewatit TP...
Equilibrium distributions of cobalt(II), nickel(II), zinc(II), cadmium(II), and copper(II) have been...
The adsorption of Ni(II) with D301R resin was investigated in this paper. The results showed that th...
This study aims to establish the potential of an iminodiacetic-based chelating resin (Purolite S930)...
In this sixth part of the series, Manganese(II) was removed from aqueous solutions by the cationic e...
The adsorption of Ni (II) from nickel electro plating rinse water has been attempted. Indion 225 and...
The removal of nickel from aqueous solutions under different experimental conditions using a Ceralit...