2595 - 2602 |
Metabolic engineering: a new frontier of chemical reaction engineering Stephanopoulos G, Stafford DE |
2603 - 2614 |
Simulation of heavy metal vaporization dynamics in a fluidized bed Zhou H, Abanades S, Flamant G, Gauthier D, Lu J |
2615 - 2625 |
Oxidative dehydrogenation of ethane at short contact times: species and temperature profiles within and after the catalyst Henning DA, Schmidt LD |
2627 - 2633 |
Drag force on a floc in a flow field: two-layer model Hsu JP, Hsieh YH |
2635 - 2640 |
Use of angle of repose and bulk densities for powder characterization and the prediction of minimum fluidization and minimum bubbling velocities Wong ACY |
2641 - 2652 |
The effect of a crystal size distribution on ZLC experiments Duncan WL, Moller KP |
2653 - 2661 |
Effective mass of powder beds subjected to low magnitude vibration and its application to binary systems: Part 1 -Experimental methodology Yanagida T, Matchett AJ, Coulthard JM |
2663 - 2671 |
Effective mass of powder beds subjected to low magnitude vibration and its application to binary systems: Part 2 -comparison of segregated and well-mixed binary powder mixtures Yanagida T, Matchett AJ, Coulthard JM |
2673 - 2678 |
Multi-component lattice gas diffusion Benes NE, Bouwmeester HJM, Verweij H |
2679 - 2696 |
Removal of volatile organic compounds by cryogenic condensation followed by adsorption Gupta VK, Verma N |
2697 - 2705 |
Transient operation of a catalytic liquid-liquid plug flow reactor for kinetics measurements Caravieilhes S, Schweich D, de Bellefon C |
2707 - 2718 |
The hydrodynamics of ejector-Venturi scrubbers and their modelling by an annular flow/boundary layer model Gamisans X, Sarra M, Lafuente FJ, Azzopardi BJ |
2719 - 2725 |
Enhancement of laminar mixing by optimal control methods Vikhansky A |
2727 - 2733 |
Henry's law constant of organic compounds in water from a group contribution model with multipole corrections Lin ST, Sandler SI |
2735 - 2746 |
Modelling of free radical polymerisation of ethylene using difunctional initiators Dhib R, Al-Nidawy N |
2747 - 2752 |
Water activities of florinated solid polymer electrolyte/water systems using group-contribution method Huh JY, Bae YC |
2753 - 2764 |
Process optimisation in sunflower oil extraction by supercritical CO2 Bravi M, Bubbico R, Manna F, Verdone N |
2765 - 2771 |
An analytical model for material line kinematics in steady and unsteady buoyancy driven flows in 2-d channels De Chant LJ |
2773 - 2780 |
A kinetic study on anaerobic reduction of sulphate, Part I: Effect of sulphate concentration Moosa S, Nemati M, Harrison STL |
2781 - 2789 |
Pressure drop modelling in cellular metallic foams Fourie JG, Du Plessis JP |
2791 - 2798 |
The use of two different models to describe the axial mixing of solids in fluidised beds Grasa G, Abanades JC |
2799 - 2809 |
Optimal mode of operation for biomass production Betlem BHL, Mulder P, Roffel B |
2811 - 2823 |
Modeling the impact of shrinkage on the pyrolysis of dry biomass Hagge MJ, Bryden KM |
2825 - 2835 |
Solubilization of model polycyclic aromatic hydrocarbons by nonionic surfactants Li JL, Chen BH |
2837 - 2848 |
Influence of macromixing on powder formation in a reactive coaxial jet Ablitzer C, Gruy F, Perrais C |
2849 - 2862 |
Computational fluid dynamic modelling of flow patterns in an oscillatory baffled column Ni X, Jian H, Fitch AW |
2863 - 2873 |
Contact time optimization of two-stage batch adsorber systems using the modified film-pore diffusion model Hui CW, Chen B, McKay G |
2875 - 2876 |
1(st) moment in the Colombo model used to calculate solid-liquid contacting effectiveness in trickle bed reactors Coleman LJI, Hudgins RR, Silveston PL |