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Though diluent is unable to extract metal ion from the aqueous phase, they greatly affect the extraction behavior of extractant (Habashi 1993).
Effects of the pH value in aqueous phase, the extractant concentration in organic phase and the number of stages on the extraction behavior in the mixer settler column are also shown.
Estimation results are consistent with the hypothesis that forest access regimes affect both forest extraction behavior and other livelihood strategies.
Al-doped SnO2 thin films prepared at a low temperature (190 °C) show a better charge transport and electron extraction behavior than the pristine SnO2.
Extraction behavior of rare earth metals within a mixer settler extraction column has been analyzed with the stage efficiency calculated from mass transfer coefficients and interfacial area.
The aim of this study was to investigate the extraction behavior of As, Pb, and Zn from mine tailings for considering the feasibility of soil washing.
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In this work, the extraction behaviors of zinc, H2O and NH3 in the organic phase have been investigated.
The extraction behaviors of V (V), V (IV), Fe (III), Fe (II), Mg (II), K (I), Na (I) in ELM process were reported and the effects of various impurities on vanadium extraction were also investigated.
It is this transformation that leads to the discrepancy of the extraction behaviors with C2-BTP in molecular diluents or RTILs, and the intermolecular interactions should be well tuned to design a delighting extracting system.
The extraction behaviors of Eu III) and Am III) from nitric acid medium by 2,6-bis 5,6-diethyl-1,2,4-triazin-3-yl) pyridine (C2,6-bis 5,6-diethyl-1,2,4-triazin-3-ylm temperature ionic liquids (RTILs), viz.
Arising from up-conversion and hole extraction behaviors of N-CQDs, a maximized power conversion efficiency (PCE) as high as 9.29% under one sun illumination is achieved for N300-CQDs/N719 co-sensitized DSSC in comparison with 8.09% for N300-CQDs-free device.
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