Two-phase oxidizing flow in volatile removal assembly reactor under microgravity conditions

Volatile removal assembly (VRA) is a module installed in the International Space Station for removing contaminants (volatile organics) in the wastewater produced by the crew. The VRA contains a slim pack-bed reactor to perform catalyst oxidation of the wastewater at elevated pressure and temperature under microgravity conditions. Optimal design of the reactor requires a thorough understanding about how the reactor performs under microgravity conditions. The efficiency of catalyst oxidation is controlled by catalyst oxidation kinetics and oxygen gas distribution in the reactor. The process involves bubbly flow in porous media with chemical reactions in microgravity environment, which has not been previously studied. We have developed and used a mathematical model in this study to simulate the organics oxidation process in the VRA reactor. We conclude that 1) the remaining oxygen gas in the VRA reactor should decline exponentially with reactor length; 2) the minimum reactor length required to achieve a complete oxygen utilization is directly proportional to bubble size, oxygen density, and bubble velocity, and inversely proportional to rate of oxidation per unit area and bubble sphericity; 3) gravity affects oxygen utilization through changing several parameters including oxygen bubble size; and 4) the example VRA design is very conservative.