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(2)A(2)]((0)); J (kmol/m(2)s) = 10(-4.86)(1 + 0.0056[Zr(IV)](-1))(-1)[H(2)A(2)]((0)) and J (kmol/m(2)/s) = 10(-5.46)(1 + 0.0056[Zr(IV)](-1))(-1)[H+][H(2)A(2)]((0)). The values of activation energy (E.) depend on the Zr(IV) concentration and temperature regions. The values of E., AH-+, AV: have been determined under various conditions. The flux equations and the values of E, 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)(H2O)(24)Cl-13](-) or [Zr-4(OH)(8/9)(H2O)(16)Cl-9/8](-) in 0.10 M HCl; [Zr-4(OH)(8)(H2O)(16)Cl-8] or Zr(OH)Cl-3 in 1 M HCl and [Zr(H2O)(4)Cl-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(3)A(2)(+) are slower than the rates of diffusions of [Zr-8(OH)(20)(H2O)(24)Cl-13](-), [Zr-4(OH)(8)(H2O)(16)Cl-8] and [Zr(H2O)(4)Cl-4](2-) in 0.10, 1 and 5 M HCl media, respectively, (C) 2004 Elsevier B.V. All rights reserved.