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Fig. 4


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Viscosity increase due to increasing uranyl concentration in the organic phase for different extractants at 25 °C. Left: apparent viscosity at a shear rate of 50 1/s. Right: relative viscosity normalized by the viscosity of the non-contacted extractant/diluent mixtures. ■ 1.5 M DEHDMBA, 1.5 M DEHiBA, 1.5 M DEHBA, 1.5 M MOEHA, 1.5 M TBP diluted in Isane IP 175 versus the molar ratio uranyl/extractant.

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