This article describes the ion exchange of a heavy metal Ni(II) from aqueous solutions onto a Dowex HCR-S, cationic resin. Batch adsorption studies were conducted to evaluate the effect of various parameters such as pH, resin dose, stirring speed, temperature, contact time and initial Ni(II) concentration on the removal of Ni(II). Adsorption rate increased with the increase in initial nickel concentration, stirring speed and temperature. Equilibrium adsorption isotherms were measured for the single component system, and the experimental data were analyzed by using Langmuir, Freundlich, Elovich, Temkin, Khan, Sips, Toth, Koble-Corrigan and Radke-Prausnitz isotherm equations. The Sips equation appears to fit the equilibrium data. Different mo...
Cadmium(II) adsorption from aqueous sulphate medium on Lewatit TP260 cationic (di-Na+) ion exchange ...
This paper describes the recovery of Ni (II) from electroplating rinse water using the Hectorite cla...
In order to predict the efficiency of a SPE procedure, both the thermodynamics and the kinetics of t...
This paper estimates the suitability of the strongly basic anion exchangers, Dowex PSR2 and Dowex PS...
The adsorption of Ni(II) with D301R resin was investigated in this paper. The results showed that th...
13-20The recovery and removal of Ni(II) by macroporous weak acid resin (D151 resin) have been inves...
This paper examines Ni(II) and Co(II) adsorption from an aqueous sulfate solution onto Lewatit TP-2...
The cationic exchange resin Dowex C400 was used to remove nickel(II) from aqueous solutions of diffe...
This paper examines Ni(II) and Co(II) adsorption from an aqueous sulfate solution onto Lewatit TP-26...
The removal of nickel from aqueous solutions under different experimental conditions using a Ceralit...
The capacity of ion exchange resins, Dowex HCR-S, for removal of Zinc from aqueous solution was inve...
BACKGROUND: Nickel is a highly toxic metal which is discharged into receiving waters by several indu...
Sorption of nickel(II) and cadmium(II) ions from chloride solutions was tested. Three different stro...
Cadmium is a highly toxic metal which is found in the effluent of battery manufacturing plants. In t...
This paper reports the application of poly(azomethinethioamide) (PATA) resin having the pendent chlo...
Cadmium(II) adsorption from aqueous sulphate medium on Lewatit TP260 cationic (di-Na+) ion exchange ...
This paper describes the recovery of Ni (II) from electroplating rinse water using the Hectorite cla...
In order to predict the efficiency of a SPE procedure, both the thermodynamics and the kinetics of t...
This paper estimates the suitability of the strongly basic anion exchangers, Dowex PSR2 and Dowex PS...
The adsorption of Ni(II) with D301R resin was investigated in this paper. The results showed that th...
13-20The recovery and removal of Ni(II) by macroporous weak acid resin (D151 resin) have been inves...
This paper examines Ni(II) and Co(II) adsorption from an aqueous sulfate solution onto Lewatit TP-2...
The cationic exchange resin Dowex C400 was used to remove nickel(II) from aqueous solutions of diffe...
This paper examines Ni(II) and Co(II) adsorption from an aqueous sulfate solution onto Lewatit TP-26...
The removal of nickel from aqueous solutions under different experimental conditions using a Ceralit...
The capacity of ion exchange resins, Dowex HCR-S, for removal of Zinc from aqueous solution was inve...
BACKGROUND: Nickel is a highly toxic metal which is discharged into receiving waters by several indu...
Sorption of nickel(II) and cadmium(II) ions from chloride solutions was tested. Three different stro...
Cadmium is a highly toxic metal which is found in the effluent of battery manufacturing plants. In t...
This paper reports the application of poly(azomethinethioamide) (PATA) resin having the pendent chlo...
Cadmium(II) adsorption from aqueous sulphate medium on Lewatit TP260 cationic (di-Na+) ion exchange ...
This paper describes the recovery of Ni (II) from electroplating rinse water using the Hectorite cla...
In order to predict the efficiency of a SPE procedure, both the thermodynamics and the kinetics of t...