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Optimization of gas hydrate reactors with slug flow
Affiliation:1. Universidad de Las Palmas de Gran Canaria, Departamento de Ingeniería de Procesos, Edificio de Ingenierías-Tafira Baja, 35017 Las Palmas, GC, Spain;2. Universidad Nacional de Educación a Distancia, UNED, E.T.S. Ingenieros Industriales, Departamento de Ingeniería Energética, C/ Juan del Rosal 12, 28040 Madrid, Spain;3. Universidad de Las Palmas de Gran Canaria, Departamento de Ingeniería Civil, Edificio de Ingenierías-Tafira Baja, 35017 Las Palmas, GC, Spain
Abstract:A model of heat transfer during gas hydrate formation at a gas-liquid interface in gas-liquid slug flow with liquid plugs containing small bubbles is suggested. Under the assumption of perfect mixing of liquid in liquid plugs, recurrent relations for temperature in the n-th liquid plug and heat and mass fluxes from the n-th unit cell in a gas-liquid slug flow are derived. The ratio of the total mass flux during gas hydrate formation in a cluster with N unit cells to the mass flux in a cluster with an infinite number of unit cells is determined. The number of unit cells that yield 95% of the total amount of gas hydrates in an infinite cluster of unit cells is calculated and formula for an optimal length of a gas hydrate slug flow reactor is derived.
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