Abstract
The kinetics of solvent extraction of Zr(IV) from acidic chloride solution by D2EHPA have been investigated by the single drop technique after 30-day ageing of the aqueous phase. The flux equations at 303 K have been derived for three aqueous acidities of 0.10, 1.00 and 5.00 M HCl, respectively, as: J (kmol/m 2 s)=10 −4.57(1+0.00036[Zr(IV)] −1) −1[H +][H 2A 2] (0); J (kmol/m 2 s)=10 −4.86(1+0.0056[Zr(IV)] −1) −1[H 2A 2] (0) and J (kmol/m 2/s)=10 −5.46(1+0.0056[Zr(IV)] −1) −1[H +][H 2A 2] (0). The values of activation energy ( E a) depend on the Zr(IV) concentration and temperature regions. The values of E a, Δ H ±, Δ S ± have been determined under various conditions. The flux equations and the values of E a indicate that the extraction processes are chemically controlled at lower temperature and Zr(IV) concentration regions. The reacting Zr(IV) species that satisfy the rate data are either [Zr 8(OH) 20(H 2O) 24Cl 13] − or [Zr 4(OH) 8/9(H 2O) 16Cl 9/8] − in 0.10 M HCl; [Zr 4(OH) 8(H 2O) 16Cl 8] or Zr(OH)Cl 3 in 1 M HCl and [Zr(H 2O) 4Cl 4] 2− in 5 M HCl. On the other hand, at higher temperature and Zr(IV) concentration regions, extraction processes are diffusion controlled, where the rates of diffusion of H 3A 2 + are slower than the rates of diffusions of [Zr 8(OH) 20(H 2O) 24Cl 13] −, [Zr 4(OH) 8(H 2O) 16Cl 8] and [Zr(H 2O) 4Cl 4] 2− in 0.10, 1 and 5 M HCl media, respectively.
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