AbstractApplication of mole fractions and volume ones for creation of mathematical model for extraction processes with TBP was discussed. Method for calculating activity coefficients was provided. Water distribution was taken into account due to the significant importance of free water. Calculation of activity coefficients in three major systems, namely: H2O-TBP, H2O-HNO3-TBP-diluent, H2O-UO2(NO3) 2-TBP was performed. Information on experimental data and optimization criterion was provided. It shown that new method can provide adequate description of the system H2O-HNO3-UO2(NO3) 2-TBP-diluent and its subsystems. Three major potential challenges have been identified
This work follows a feasibility study (187) which suggested that a process for purifying wet-process...
A computer program has been developed for optimization and modelling of counter–current solvent extr...
The purpose of this paper is to explore the use of solvent extraction for the removal and recovering...
A mathematical model founded on the equilibrium constants expressions has been developed for the sim...
AbstractApplication of mole fractions and volume ones for creation of mathematical model for extract...
The chemical model presented is founded on the prediction of all chemical reactions taking place in ...
A mathematical model developed for the equilibrium HNO3-UO2(NO3)(2)-tri-n-butyl phosphate (TBP)-dilu...
Solvent extraction is considered as a multi-criteria optimization problem, since several chemical sp...
Uranium is a strategic element and plays an important role in energy resources. A H2O-HNO3-UO2(NO3)(...
The distribution of 0-8 M HNO3 between aqueous and 5- 100 vol % solutions of TBP in Amsco 125-82 has...
The extraction of uranium(VI) from acidic sulfate and nitrate media by Alamine 300 and di-n-octyl am...
A comparative study of reactive extraction of formic acid from water by tri-n-propyl amine (TPA) and...
Abstract: This paper presents a study on the statistical modelling of the results obtained at uraniu...
A process was developed to recover nitric acid from the waste stream of wafer industry using solvent...
The extraction equilibria of the type 2 ternary systems containing (water + isovaleric acid + solven...
This work follows a feasibility study (187) which suggested that a process for purifying wet-process...
A computer program has been developed for optimization and modelling of counter–current solvent extr...
The purpose of this paper is to explore the use of solvent extraction for the removal and recovering...
A mathematical model founded on the equilibrium constants expressions has been developed for the sim...
AbstractApplication of mole fractions and volume ones for creation of mathematical model for extract...
The chemical model presented is founded on the prediction of all chemical reactions taking place in ...
A mathematical model developed for the equilibrium HNO3-UO2(NO3)(2)-tri-n-butyl phosphate (TBP)-dilu...
Solvent extraction is considered as a multi-criteria optimization problem, since several chemical sp...
Uranium is a strategic element and plays an important role in energy resources. A H2O-HNO3-UO2(NO3)(...
The distribution of 0-8 M HNO3 between aqueous and 5- 100 vol % solutions of TBP in Amsco 125-82 has...
The extraction of uranium(VI) from acidic sulfate and nitrate media by Alamine 300 and di-n-octyl am...
A comparative study of reactive extraction of formic acid from water by tri-n-propyl amine (TPA) and...
Abstract: This paper presents a study on the statistical modelling of the results obtained at uraniu...
A process was developed to recover nitric acid from the waste stream of wafer industry using solvent...
The extraction equilibria of the type 2 ternary systems containing (water + isovaleric acid + solven...
This work follows a feasibility study (187) which suggested that a process for purifying wet-process...
A computer program has been developed for optimization and modelling of counter–current solvent extr...
The purpose of this paper is to explore the use of solvent extraction for the removal and recovering...