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The global imperative to mitigate climate change has positioned CCS as a key strategy for reducing CO2 emissions from large industrial sources. Depleted oil and gas reservoirs are among the most promising storage sites due to their proven containment integrity and existing infrastructure. However, injection of dense-phase CO2 into such low-pressure reservoirs presents operational challenges, particularly near the injection well. The isenthalpic expansion of CO2 generates a Joule-Thomson cooling effect, which in the presence of brine can trigger hydrate formation. Hydrate nucleation and growth reduce reservoir permeability and may impair injectivity, posing risks to storage efficiency. While the thermodynamic conditions for hydrate formation are well established, its kinetic behavior in porous media remains poorly understood due to the stochastic nature of nucleation and variability in growth and dissociation rates. This study investigates hydrate kinetics through dynamic core-flood experiments under varying subcooling levels and thermal protocols (isothermal, step-cooling/heating, and ramp-cooling/heating). A medical CT scanner was employed in selected tests to monitor hydrate dynamics and quantify saturations. Statistical analyses of induction times and growth rates were performed as functions of subcooling and fugacity difference, respectively. Results yield a master curve that enhances predictive capability for hydrate kinetics under CCS conditions.