Computer Modeling of Strong Acid Cation Exchangers on Styrene: Divinylbenzene Matrix

2012 ◽  
pp. 509-545
Author(s):  
V. S. Soldatov ◽  
V. M. Zelenkovskii
2017 ◽  
Vol 314 ◽  
pp. 192-201 ◽  
Author(s):  
Pornsawai Praipipat ◽  
Medhat Mohamed El-Moselhy ◽  
Kulyakorn Khuanmar ◽  
Panomchai Weerayutsil ◽  
Trung Thanh Nguyen ◽  
...  

2016 ◽  
Vol 34 (5) ◽  
pp. 502-508 ◽  
Author(s):  
O. H. Altshuler ◽  
G. Yu. Shkurenko ◽  
H. N. Altshuler

2013 ◽  
Vol 2013 ◽  
pp. 1-7 ◽  
Author(s):  
Gulten Cetin ◽  
Sevgi Kocaoba ◽  
Goksel Akcin

The process in this study was conducted on removal of chromium(III) in a solution simulating a typical spent chrome tanning bath by the resin having matrix of styrene-divinylbenzene-based macroporous sulphonate, Amberjet 1200Na. The column experiments were carried out with the bed volumes of the resin as 751 mL and 1016 mL for different installation systems of the laboratory-scale pilot plant. The feeding solutions in the bed volumes of 200 and 190 were used for each installation system. The regeneration behaviour of the resin was determined by using reverse regeneration procedure with the solution of hydrogen peroxide in alkaline. The regeneration kinetics of the exhausted resin was examined with a range of the solutions having different concentration series of the alkaline hydrogen peroxide. The solutions of the basic chromium sulphate were recycled for each installation system following the regeneration cycles. The chromium ions in effluent were quantitatively eluted, and satisfactory removal of chromium(III) and recovery of chromium(VI) were achieved.


1988 ◽  
Vol 37 (12) ◽  
pp. 1114-1121 ◽  
Author(s):  
Wataru AGUI ◽  
Masahito TAKEUCHI ◽  
Masahiko ABE ◽  
Keizo OGINO

2021 ◽  
Vol 22 (1) ◽  
pp. 127-138
Author(s):  
Dilfuza Nuriddinova

In the research work, the adsorption equilibrium, kinetics, thermodynamics and dynamic separation of magnesium and calcium ions from industrial wastewater by new strong acid cation resin of SPVC (sulphonated polyvinylchloride) were investigated. The sorption capacity of the studied resin was 3.78 mmol/g and 3.74 mmol/g for magnesium and calcium ions, respectively, according to Langmuir isotherm. It was found that the pseudo−first−order model was better fitted for the adsorption kinetics of magnesium and calcium ions on the resin. The dynamic separation results confirmed that the selected resin effectively separated magnesium and calcium ions from industrial wastewater in the dynamic condition. The change of the standard Gibbs free energy (G) and enthalpy (H), and entropy (S) were calculated. The obtained results confirmed that the adsorption of magnesium and calcium ions on the selected resin is endothermic.


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