CABEQ 21(4) 2007

«. Kurtanjek, I. Butula, M. PopoviŠ, A. Schumpe, A. Zeng
In memoriam: Prof. Dr. Wolf-Dieter Deckwer

P. Gluszcz, S. Ledakowicz, J. Petera ,and W-D. Deckwer
Thermodynamic and Kinetic Aspects of Mercury Sorption on Activated Carbon inthe Process of Mercury Bioreduction

J. Bader, K. Schwab, M.K. PopoviŠ, R. Bajpai, and B. Neumann
Application of pH and pO2 Probes During Bacillus caldolyticus Fermentation: An Additional Approach for Improving a Feeding Strategy

C. Ulmer and A.-P. Zeng
Microbial Production of 3-Hydroxypropionaldehyde from Glycerol Bioconversion

S. Nedeltchev and A. Schumpe
Theoretical Prediction of Mass Transfer Coefficients in a Slurry Bubble Column Operated in the Homogeneous Regime

E. Franco-Lara, R. Krull, D.-C. Hempel, and A. Haarstrick
Specification and Supervision of System Performance in Yeast Bioprocesses

J. C.Merchuk,F.Garcia-Camacho,andE.Molina-Grima
Photobioreactor Design and Fluid Dynamics

T. Goshima and K. Terasaka
Simultaneous Measurements of Gas-Solid Flow Rates and Pressure Drop in Downcomer of J-Valvein CFB

M. Yoshimoto, S. Suenaga, K. Furumoto, K. Fukunaga, and Katsumi Nakao
Gas-Liquid Interfacial Area, Bubble Size and Liquid-Phase Mass Transfer Coefficient in a Three-Phase External Loop Airlift Bubble Column

K. Nakao, S. Suenaga, K. Furumoto, M. Yoshimoto, and K. Fukunaga
Hydrodynamic and Mass Transfer Properties in a Three Phase External Loop Airlift Compared with a Three Phase Internal Loop Airlift and a Slurry Bubble Column

K. Muroyama, E. Shibutani, T. Tsuji, and M. Shimizu
Performance Evaluation of a Full-Scale Deep U-Tube Utilizing Ozonated Oxygen as the Process Gas for Treating Drinking Water

S. Yonsel, G. BŘlbŘl-ăaliskan, M. K÷ni, and L. Dagasan
Monitoring of Yeast Metabolism with Calorimetry

M. Bo╣njak and K. MihaljeviŠ
Oxygen Solubility and Oxygen Transfer and Uptake Rates as Functions of Water Activity

G. Maria
Modelling Bistable Genetic Regulatory Circuits Under Variable Volume Framework

M. K. PopoviŠ, C. Wulfes, and R. K. Bajpai
Drift Flux Distribution Parameter in Three-Phase Air-Lift Reactor