213 - 218 |
A Comparison of the Sorbtive Characteristics of Leaf Mold and Activated Carbon Columns for the Removal of Hexavalent Chromium Sharma DC, Forster CF |
219 - 224 |
Anaerobic-Digestion of Wash Waters Derived from the Purification of Virgin Olive Oil Using a Hybrid Reactor Combining a Filter and a Sludge Blanket Borja R, Alba J, Banks CJ |
225 - 228 |
PH-Controlled Fermenters to Increase Production of Leuconocin-S by Leuconostoc-Paramesenteroides Baker RC, Winkowski K, Montville TJ |
229 - 234 |
Influence of the Immobilization Conditions on the Efficiency of Alpha-Amylase Production by Bacillus-Licheniformis Dobreva E, Ivanova V, Tonkova A, Radulova E |
235 - 241 |
A Temperature Profile in Batch Culture to Increase the Production of the Recombinant UDP-Glucuronosyltransferase 2B4 in Escherichia-Coli Lamotte D, Ouzzine M, Fournelgigleux S, Magdalou J, Boudrant J |
243 - 248 |
Determination of Kinetics Parameters for Free and Immobilized Beta-Galactosidase Carrara CR, Rubiolo AC |
249 - 252 |
Effect of Nonlinear Equilibrium on the Mass-Transfer Rate of Alpha-Amylase Extraction by Reversed Micelles Brandani S, Brandani V, Digiacomo G, Spera L |
253 - 263 |
Separation of Enzymes Produced by Trichoderma-Reesei with Hydrophobic Ultrafiltration Membranes Ehsani N, Nystrom M, Ojamo H, Siikaaho M |
265 - 270 |
Fed-Batch Culture for Xylitol Production by Candida-Boidinii Vandeska E, Amartey S, Kuzmanova S, Jeffries TW |
271 - 280 |
Lactic-Acid from Wood Parajo JC, Alonso JL, Santos V |
281 - 285 |
Immobilization of Beta-Glucosidase from a Commercial Preparation .1. A Comparative-Study of Natural Supports Martino A, Durante M, Pifferi PG, Spagna G, Bianchi G |
287 - 293 |
Immobilization of Beta-Glucosidase from a Commercial Preparation .2. Optimization of the Immobilization Process on Chitosan Martino A, Pifferi PG, Spagna G |
295 - 301 |
Process Model of the Oxidation of Glycerol with Gluconobacter-Oxydans Ohrem HL, Voss H |