Mass Transfer in High-Pressure Bubble Columns with Organic Liquids
β Scribed by U. Jordan; K. Terasaka; G. Kundu; A. Schumpe
- Publisher
- John Wiley and Sons
- Year
- 2002
- Tongue
- English
- Weight
- 190 KB
- Volume
- 25
- Category
- Article
- ISSN
- 0930-7516
No coin nor oath required. For personal study only.
β¦ Synopsis
Dedicated to Professor Dr. Wolf-Dieter Deckwer on the occasion of his 60th birthday Oxygen desorption from organic liquids (ethanol (96 %), 1-butanol, toluene) and water into nitrogen gas has been studied with an optical sensor. Gas hold-ups and volumetric mass transfer coefficients have been determined in the pressure range of 1Β±10 bar. In this range both quantities are found to increase with the gas density to the power of 0.24. However, by comparison with literature data and on theoretical grounds, the gas density effect can be shown to depend on the gas velocity and on gas density itself. The effect becomes negligible at gas velocities below 0.01 m/s and at gas densities below about 0.1 kg/m 3 .
π SIMILAR VOLUMES
Bubble column reactors are widely used in the fields of petrochemical, biochemical, and chemical engineering processes. They are comparable to other multiphase reactors because of their simplicity, low operating costs, and higher heat and mass transfer coefficients between phases. Since a continuous