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Tn- n-butyl

Solovkin,A.S. Rubisov,V.N. Smelov,V.S. Druzherukov,V.I. Starikov,V.M. Muratova, G.G. Simulating equilibria in two-phase systems I I2()-I INOrI I2S()4-An(IV )-tn-n-butyl-phosphate-n-alkanes, Sov. Atomic Energy (English Trans.) 62 (1987) 385-390. [Pg.110]

Thorex [Thorium extraction] A process for separating the products from the nuclear breeder reaction in which uranium-233 is produced by the neutron bombardment of thorium-232. It uses solvent extraction into tri-n-butyl phosphate. Developed at the Oak Ridge National Laboratory, TN, in the early 1960s. See also Butex, Purex, Redox. [Pg.270]

Bums, J.H. 1983. Solvent-extraction complexes of the uranyl ion. 2. Crystal and molecular structures of cafe a-Bis( r-di- -butyl phosphato-0,0 ) dioxouranium(VI) and Bisfp-di-n-butyl phosphato-O, O )bis[(nitrato)(tn-n-butylphophine oxide) dioxouranium(VI)]. Inorg. Chem. 22 1174—1178. [Pg.502]

FIG. 16.18 Non-Newtonian viscosity ratio for solutions of narrow molecular weight distribution polystyrenes in n-butyl benzene, plotted vs. reduced shear rate q/q0, where qa, equal to the reciprocal of the characteristic time constant Tn, is chosen empirically for each solution. The data were obtained for molecular weights ranging from 160 to 2400 kg/mol and for concentrations ranging from 0.255 to 0.55 g/ml at temperatures from 30 to 60 °C.The full line is calculated with the aid of Eqs. (16.52)—(16.55). From Graessley, Hazleton and Lindeman (1967). Courtesy Society of Rheology. [Pg.628]

Curves 1 and 2 in Fig. 22 describe theoretical dependences [n /tn] = f (M) plotted according to Eq. (70) at Vn, = 0.57. In this plot such values of the and parameters ate selected that ensure the best agreement between theoretical curves and experimental data (points) for poly-(butyl isocyanate) and po y(chlorohexyl isocyanate) in tetrachlormethane. The corresponding values of Aa, (3, Mg, S and A are given in Table 9. [Pg.144]


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