| 701 - 714 |
A Model for Light-Distribution and Average Solar Irradiance Inside Outdoor Tubular Photobioreactors for the Microalgal Mass-Culture
Fernandez FG, Camacho FG, Perez JA, Sevilla JM, Grima EM |
| 715 - 726 |
Effect of Agitation Intensities on Fungal Morphology of Submerged Fermentation
Cui YQ, Vanderlans RG, Luyben KC |
| 727 - 736 |
Toxicity and Biodegradation of Formaldehyde in Anaerobic Methanogenic Culture
Qu MB, Bhattacharya SK |
| 737 - 746 |
Linear Scale Ultrafiltration
Vanreis R, Goodrich EM, Yson CL, Frautschy LN, Dzengeleski S, Lutz H |
| 747 - 757 |
New Patterns of Mixed-Substrate Utilization During Batch Growth of Escherichia-Coli K12
Narang A, Konopka A, Ramkrishna D |
| 758 - 772 |
An Indirect Optimization Method for Biochemical Systems - Description of Method and Application to the Maximization of the Rate of Ethanol, Glycerol, and Carbohydrate Production in Saccharomyces-Cerevisiae
Torres NV, Voit EO, Glezalcon C, Rodriguez F |
| 773 - 782 |
Kinetic Modeling of Poly(Beta-Hydroxybutyrate) Production and Consumption by Paracoccus-Pantotrophus Under Dynamic Substrate Supply
Vanaalastvanleeuwen MA, Pot MA, Vanloosdrecht MC, Heijnen JJ |
| 783 - 792 |
Fed-Batch Culture of Recombinant Ns0 Myeloma Cells with High Monoclonal-Antibody Production
Zhou WC, Chen CC, Buckland B, Aunins J |
| 793 - 797 |
Cell-Size Distribution as a Parameter for the Predetermination of Exponential-Growth During Repeated Batch Cultivation of CHO Cells
Seewoster T, Lehmann J |
| 798 - 806 |
Water Activity and Substrate Concentration Effects on Lipase Activity
Wehtje E, Adlercreutz P |
| 807 - 814 |
Thermophilic Sulfate and Sulfite Reduction in Lab-Scale Gas-Lift Reactors Using H-2 and CO2 as Energy and Carbon Source
Vanhouten RT, Yun SY, Lettinga G |
| 815 - 820 |
Application of Self-Cycling Fermentation Technique to the Production of Poly-Beta-Hydroxybutyrate
Marchessault P, Sheppard JD |
