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In the Fischer−Tropsch (FT) synthesis, a mixture of CO and H₂ is converted into hydrocarbons and water with diluted organics. This water fraction with oxygenated hydrocarbons can be processed through aqueous-phase reforming (APR) to produce H₂. Therefore, the APR of FT water may decrease the environmental impact of organic waters and improve the efficiency of the FT process. This work aimed at developing a kinetic model for the APR of FT water. APR experiments were conducted with real FT water in a continuous packed-bed reactor at different operating conditions of temperature (210−240 °C), pressure (3.2−4.5 MPa) and weight hourly space velocity (WHSV) (40−200 h^−1) over a nickel-copper catalyst supported on ceria-zirconia. The kinetic model considered C₁-C₄ alcohols as reactants, H₂, CO, CO₂ and CH₄ as the gaseous products, and acetic acid as the only liquid product. The kinetic model included seven reactions, the reaction rates of which were expressed with power law equations. The kinetic parameters were estimated with variances and confidence intervals that explain the accuracy of the model to estimate the outlet liquid composition resulting from the APR of FT water. The kinetic model developed in this work may facilitate the development of APR to be integrated in a FT synthesis process.