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This study investigates the kinetics of methane hydrate formation in a 1200 ml unstirred reactor, highlighting the effects of reactor size on hydrate formation behaviors. Key findings include heterogeneous hydrate distribution, a hollow inner structure in bulk hydrates, and variable optimal THF concentrations, which differ from stoichiometric expectations. These insights are crucial for advancing Solidified Natural Gas (SNG) technology for large-scale natural gas storage and commercialization.

Author

Arman Ahmad

Language

EN