CH 4 /CO 2 mixed hydrate forms upon CO 2 gas injection into the CH 4 gas hydrate reservoir. An improved understanding of the dissociation behavior of the CH 4 /CO 2 hydrate system is necessary to increase the yield of CH 4 production and CO 2 storage. In this study, CH 4 /CO 2 mixed hydrates (in bulk and unconsolidated coarse sand) were dissociated using the multistep cyclic depressurization (MCD) method. Visual and kinetic data were collected using a high-pressure reactor and gas chromatography (GC) setup to study the change in morphology and mole fraction of CH 4 and CO 2 in the released gas. The influence of chemicals (methionine, sodium dodecyl sulfate, and methanol) in the aqueous phase and reservoir temperature (below and above 0 °C) on recovery and storage yield was also investigated. This study reported additional CH 4 recovery below the CH 4 hydrate stability pressure when cyclic depressurization was implemented between CH 4 and CO 2 hydrate stability pressures. A rapid increase in CH 4 mole fraction and a decrease in CO 2 mole fraction were observed due to simultaneous CH 4 hydrate dissociation and CO 2 hydrate reformation. This phenomenon was accelerated at high liquid saturation. CH 4 recovery potential was positively correlated with hydrate saturation and for T > 0 °C conditions. Morphology study showed the expansion of hydrate volume during cyclic depressurization, which confirmed hydrate reformation from released water from dissociation. The chemicals affected the mixed CH 4 /CO 2 hydrate synthesis, reformation kinetics, and subsequent CO 2 storage. This study demonstrates a novel application of cyclic depressurization to enhance CH 4 production and improve CO 2 storage. A new hydrate production method is also proposed that includes constantrate depressurization, kinetic inhibitor-based CO 2 injection, and cyclic depressurization.