In a specific bubble column system, the hydrodynamics depend on operating conditions in terms of pressure and temperature in which high-pressure operations are common in industrial applications. The gas holdup and bubble size determine the bubble surface area that affect the mass-transfer between phases. High pressure enhances surface area while the feedstock is kept as constant. Therefore, there is a need for a CFD model involving a realistic gas-liquid contacting area in a bubble column under high pressure. The objectives of this project are:
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