Immunopharmacology 1991: Vol 29 Table of Contents

3 Pages·1991·0.54 MB·English

197
Author Index of Volume 29
Al-Duri, B., 133 Hanéil, V., 39 Riede, Th., 9
Hofmann, H., 65 Rod, V., 39
Bjorn, I., 185
Bradka, F., 107 Karcz, J., 165 Schliinder, E. U., 9
Kistenmacher, H., 139 Semkov, Kr., 77, 83
Chang, M.-Y., 49
Knapp, H., 155 Simon, H.-G., 139
Chhabra, R. P., 121
Kolev, N., 77, 83 Srinivas, B. K., 121
Czernicki, M., 33
Strek, F., 165
McKay, G., 133 Strom, K., 185
Demyanovich, R. J., 173, 179
Ma¢kowiak, J., 93
Ditl, P., 27
Magelli, F., 27 Tobis, J., 147
Domasch, K., 1
Marisko, V., 27
Domenech, S., 33
Morsi, B. I., 49 Vortmeyer, D., 139, 147
DrahoS, J., 107
Mihle, K., 1
Waterling, U., 155
Eiras, G., 49
Nocentini, M., 27 Wichterlova, J., 39
Fajner, D., 27 Numrich, R., 117
Farhat, S., 33 Yao, B. P., 65
Fialova, M., 107 Pasquali, G., 27
Pibouleau, L., 33 Zahradnik, J., 107
Gasche, H. E., 65 Pravsnitz, J. M., 139 Zheng, C., 65
Grén, U., 185 Punéochafr, M., 107 Zheng, D., 155
Subject Index of Volume 29
Adsorption columns Channelling
isothermal, scale-up effects due to near-wall channel- near-wall, in isothermal adsorption columns, scale-up
ling in: on limitations in use of plug flow models, 147 effects due to: on limitations in use of plug flow
Aggregates models, 147
of particles in flocculation with polymers, stability Concentration distribution
of, 1 of solids in slurry reactors stirred with multiple axial
Agitated reactors impellers, 27
mass transfer characteristics of gases in n-hexane at
elevated pressures and temperatures in, 49
Distillation
batch, optimal control of, via nonlinear programming,
Baffles 33
experimental determination of optimal geometry of, Distillation column system
heat pump, study of, 185
for heat transfer in agitated vessel, 165
Drying
Batch distillation
selective through, in fixed beds, 9
optimal control of, via nonlinear programming, 33
Dyes
Binary mixtures
commercial, production of, via impingement-sheet
containing H,, CH, and CO, with high boiling hydro-
mixing, 173, 179
carbons, vapour—liquid equilibria at high tempera-
tures and pressures in: experimental equipment and
results, 155 Electrolytes and non-electrolytes
Binary systems equation of state for systems containing, 139
extended empirical Freundlich isotherm for: modified Extraction column
procedure to obtain correlative constants, 133 prediction of performance of, from tracer experiments
Bubble columns with stationary continuous phase, 39
bubble behaviour and flow structure of, 65
effect of operating conditions on characteristics of Flocculation
pressure fluctuations in, 107 with polymers, stability of particle aggregates in, 1
Chem. Eng. Process., 29 (1991) 197-198 © Elsevier Sequoia/Printed in The Netherlands
198
Flow structure Optimal control
and bubble behaviour of bubble columns, 65 of batch distillation via nonlinear programming, 33
Fluidized beds
Packed columns
non-Newtonian fluid flow in: minimum fluidization
irrigated, pressure drop in, 93
velocity and bed expansion characteristics, 121
modelling of, accounting for axial mixing and
Freundlich isotherm
Marangoni effects, 83
extended empirical, for binary systems: modified
Plug flow models
procedure to obtain correlative constants, 133
on limitations in use of: scale-up effects due to
near-wall channelling in isothermal adsorption
Heat pump distillation column system
columns, 147
study of, 185
Polymers
Heat transfer
stability of particle aggregates in flocculation with, 1
in agitated vessel, experimental determination of
optimal geometry of baffles for, 165 Pressure drop
in irrigated packed columns, 93
in rough tubes, 117
Pressure fluctuations
in bubble column, effect of operating conditions on
Impellers
multiple axial, solids concentration distribution in characteristics of, 107
slurry reactors stirred with, 27
Slurry reactors
Impingement-sheet mixing
stirred with multiple axial impellers, solids concentra-
production of commercial dyes via, 173, 179
tion distribution in, 27
Solids concentration distribution
Marangoni effect
in slurry reactors stirred with multiple axial impellers,
(interfacial turbulence) in gas(vapour)—liquid mass
27
transfer, evaluation of, 77, 83
Mass transfer characteristics Through-drying
of gases in n-hexane at elevated pressures and tempera- selective, in fixed beds, 9
tures in agitated reactors, 49 Tubes
Mixing rough, heat transfer in, 117
axial, and Marangoni effects, modelling of packed Turbulence
columns accounting for, 83 interfacial (Marangoni effect) in gas(vapour)—liquid
impingement-sheet ,p roduction of commercial dyes
mass transfer, evaluation of, 77, 83
via, 173,179
Vapour—liquid equilibria
Non-Newtonian fluid flow at high temperatures and pressures in binary mixtures
in fluidized beds: minimum fluidization velocity and containing H,, CH, and CO, with high boiling hydro-
bed expansion characteristics, 121 carbons: experimental equipment and results, 155