This study reports an investigation of the ion exchange treatment of sodium chloride solutions in relation to use of resin technology for applications such as desalination of brackish water. In particular, a strong acid cation (SAC) resin (DOW Marathon C) was studied to determine its capacity for sodium uptake and to evaluate the fundamentals of the ion exchange process involved. Key questions to answer included: impact of resin identity; best models to simulate the kinetics and equilibrium exchange behaviour of sodium ions; difference between using linear least squares (LLS) and non-linear least squares (NLLS) methods for data interpretation; and, effect of changing the type of anion in solution which accompanied the sodium species. Kineti...
230-233Equilibrium exchange studies of K+/Na+, Rb+/Na+ and Cs+/Na+ systems on phosphonated toluene-p...
This paper provides new insights on the regeneration step of an ion exchange process for the treatme...
<p>An amphoteric ion-exchange resin hardly shrank in 550 and 300 g/L glucose and sodium chloride sol...
This study reports an investigation of the ion exchange treatment of sodium chloride solutions in re...
Common to many types of water and wastewater is the presence of sodium ions which can be removed by ...
Highlights - The BWS kinetic expression was found to be an optimal engineering model for sodium exch...
<b>Highlights</b>\ud \ud - The BWS kinetic expression was found to be an optimal engineering model ...
Ion exchange and its industrial applications to water treatment are briefly reviewed. The emphasis h...
Coal seam gas production has resulted in the production of large volumes of associated water which c...
This paper relates to the importance of impact of the chosen bottle-point method when conducting ion...
This study evaluated the complexity of calcium ion exchange with sodium exchanged weak acid cation r...
A study has been made of methods for the characterization and prediction of ion exchange equilibria....
The exchange of iron species from iron (III) chloride solutions with a strong acid cation resin has ...
The present paper deals with the application of thermodynamic concept in understanding the preferent...
Bibliography: p. 218-224.Fresh water is becoming increasingly scarce in the modern technological wor...
230-233Equilibrium exchange studies of K+/Na+, Rb+/Na+ and Cs+/Na+ systems on phosphonated toluene-p...
This paper provides new insights on the regeneration step of an ion exchange process for the treatme...
<p>An amphoteric ion-exchange resin hardly shrank in 550 and 300 g/L glucose and sodium chloride sol...
This study reports an investigation of the ion exchange treatment of sodium chloride solutions in re...
Common to many types of water and wastewater is the presence of sodium ions which can be removed by ...
Highlights - The BWS kinetic expression was found to be an optimal engineering model for sodium exch...
<b>Highlights</b>\ud \ud - The BWS kinetic expression was found to be an optimal engineering model ...
Ion exchange and its industrial applications to water treatment are briefly reviewed. The emphasis h...
Coal seam gas production has resulted in the production of large volumes of associated water which c...
This paper relates to the importance of impact of the chosen bottle-point method when conducting ion...
This study evaluated the complexity of calcium ion exchange with sodium exchanged weak acid cation r...
A study has been made of methods for the characterization and prediction of ion exchange equilibria....
The exchange of iron species from iron (III) chloride solutions with a strong acid cation resin has ...
The present paper deals with the application of thermodynamic concept in understanding the preferent...
Bibliography: p. 218-224.Fresh water is becoming increasingly scarce in the modern technological wor...
230-233Equilibrium exchange studies of K+/Na+, Rb+/Na+ and Cs+/Na+ systems on phosphonated toluene-p...
This paper provides new insights on the regeneration step of an ion exchange process for the treatme...
<p>An amphoteric ion-exchange resin hardly shrank in 550 and 300 g/L glucose and sodium chloride sol...