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Gas–liquid interphase mass transfer was investigated in a slurry bubble column under CO2 hydrate forming operating conditions. Modeling gas hydrate formation requires knowledge of mass transfer and the hydrodynamics of the system. The pressure was varied from 0.1 to 4MPa and the temperature from ambient to 277K while the superficial gas velocity reached 0.20m/s. Wettable ion-exchange resin particles...
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