603 - 615 |
Gas-inducing impeller design and performance characteristics Forrester SE, Rielly CD, Carpenter KJ |
617 - 627 |
Liquid mixing and phase hold-ups in gas producing fluidized bed bioreactors Buffiere P, Fonade C, Moletta R |
629 - 638 |
Integral sorption in glassy polymers Vrentas JS, Vrentas CM |
639 - 649 |
Modelling and simulation of hydrocarbon mobility in soil-water and soil-supercritical carbon dioxide systems Barna L, Bayard R, Blanchard JM, Gourdon R |
651 - 655 |
Detecting powder mixture segregation for multicomponent mixtures Walker JJ, Rollins DK |
657 - 669 |
Selective catalytic reduction of NO over commercial DeNO(x)-catalysts : experimental determination of kinetic and thermodynamic parameters Koebel M, Elsener M |
671 - 677 |
Multiplicity of the solutions of the flash equations Tiscareno F, Gomez A, Jimenez A, Chavez R |
679 - 689 |
Reaction-bonded silicon nitride synthesis : experiments and model Maalmi M, Varma A, Strieder WC |
691 - 696 |
Conversion-temperature trajectories for well-mixed adsorptive reactors Yongsunthon I, Alpay E |
697 - 708 |
A non-isothermal, non-equimolar transient kinetic model for gas-solid reactions Patisson F, Francois MG, Ablitzer D |
709 - 719 |
Studies of mixing in a concentric tube airlift bioreactor with different spargers Merchuk JC, Contreras A, Garcia F, Molina E |
721 - 726 |
Asymptotic approach for mass transfer in a steady laminar Newtonian flow for estimating the aqueous layer permeability Flores AF |
727 - 734 |
Numerical simulation of a reverse-flow NOx-SCR reactor with side-stream ammonia addition Snyder JD, Subramaniam B |
735 - 741 |
Three-phase foam equation of state Gaporaud BMM, Sajet P, Antonini G |
743 - 751 |
Application of cubic equations of state to the fit of vapor pressures of pure components Wisniak J, Apelblat A, Segura H |
753 - 759 |
Appropriately defined dimensionless groups for the description of flow phenomena in disperse systems Molerus O |
761 - 772 |
The mechanical behaviour of vibrated, aerated beds of glass and starch powder Janssen LPBM, Marring E, Hoogerbrugge JC, Hoffmann AC |
773 - 786 |
Non-linear tracking of glass transition temperatures for free radical emulsion copolymers Fevotte G, McKenna TF, Othman S, Hammouri H |
787 - 805 |
A trickle-bed reactor model for hydrogenation of 2,4 dinitrotoluene : experimental verification Rajashekharam MV, Jaganathan R, Chaudhari RV |
807 - 817 |
Prediction of heat transfer in prototype fluidized reactors from scale-model data Overmann SP, Brown RC, Grewal NS |
819 - 832 |
Frequency response of an adsorber with modulation of the inlet molar flow-rate - I. A semi-batch adsorber Park IS, Petkovska M, Do DD |
833 - 843 |
Frequency response of an adsorber with modulation of the inlet molar flow-rate - II. A continuous flow adsorber Park IS, Petkovska M, Do DD |
845 - 846 |
Conduction heat transfer from confined spheres Kubie J |
847 - 851 |
The linear driving force model for cyclic adsorption and desorption : the effect of external fluid-film mass transfer Choong TSY, Scott DM |
853 - 856 |
The Wong-Sandler mixing rules and EOS which are thermodynamically consistent at infinite pressure Brandani F, Brandani S, Brandani V |