Examination of the Heat Transfer Model in Gas–Liquid–Solid Three Phases in Presence of Gas Hydrate Particle

Hydrate-based gas separation is often investigated using batch or semi-batch operations. To increase the throughput of mixture without increasing apparatus volume, it preferable to perform a continuous operation hydrate-based separation. Therefore, we proposed flow-type for performing formation with passing gaseous and subsequently decomposition hydrate particles. Characteristics multiple fluid heat mass transfer slurry are essential efficient apparatus. In this study, focused on characteristics in presence bubbles water surfactant solution. First, an apparent overall coefficient under pressure during steady was calculated simple assumption. Next, control amount position hydrate-decomposition hydrate-formation apparatus, temperature profile inside fluid. A model balance defining agitation made evaluate validity model, calculation value compared experimental value.