| 239 - 246 |
Heat-Recovery in Supercritical-Fluid Extraction Process with Separation at Subcritical Pressure
Sievers U, Eggers R |
| 247 - 253 |
Influence of Pressure on the Gas/Liquid Interfacial Area a and the Coefficient K(L)A in a Countercurrent Packed-Column
Benadda B, Otterbein M, Kafoufi K, Prost M |
| 255 - 263 |
A Method for Online Determination of Residual Water-Content and Sublimation End-Point During Freeze-Drying
Genin N, Rene F, Corrieu G |
| 265 - 270 |
Variation of Quality Attributes in Serially Connected Independent Food Reactor Units .2.
Kormendy I |
| 271 - 282 |
Design of a Supercritical-Fluid Extraction Process for Separating Mixtures Incurred in Enzyme-Catalyzed Reactions
Chrisochoou A, Schaber K |
| 283 - 286 |
Kinetics of the Esterification of Phthalic-Anhydride with 2-Ethylhexanol .3. Tetrabutyl Titanate as a Catalyst
Skrzypek J, Sadlowski JZ, Lachowska M, Jaroszynski M |
| 287 - 293 |
Failure Modes of Pressure-Vessel Components and Their Consideration in Analyses
Lietzmann A, Rudolph J, Weiss E |
| 295 - 300 |
Absorption of No in Aqueous-Solutions of Fe(II)NTA - Determination of the Equilibrium-Constant
Hofele J, Vanvelzen D, Langenkamp H, Schaber K |
| 301 - 310 |
A Theoretical Approach to Predict the Performance of Chevron-Type Plate Heat-Exchangers
Martin H |
| 311 - 317 |
Production of Anhydrous, Crystalline Boron-Oxide in Fluidized-Bed Reactor
Kocakusak S, Akcay K, Ayok T, Koroglu HJ, Koral M, Savasci OT, Tolun R |
