Monday, June 6, 2011
Ontario Exhibit Hall (Detroit Marriott Hotel at the Renaissance Center )
The mass transfer and reaction rates of rotating solid foam reactors were compared to a slurry reactor using the oxidation of glucose as a three-phase model reaction. Using the kinetic and mass transfer parameters the process conditions and the catalytic stirrer geometry have been optimized.
Extended Abstracts:
- Abstract_NAM22_Roman.pdf (288.6KB) - Extended Abstract