3571 - 3578 |
On the modelling and simulation of sour gas absorption by aqueous amine solutions Kucka L, Muller I, Kenig EY, Gorak A |
3579 - 3587 |
CFD simulation of mixing and reaction: the relevance of the micro-mixing model Marchisio DL, Barresi AA |
3589 - 3600 |
Rate-based modelling of SO2 absorption into aqueous NaHCO3/Na2CO3. solutions accompanied by the desorption of CO2 Ebrahimi S, Picioreanu C, Kleerebezem R, Heijnen JJ, van Loosdrecht MCM |
3601 - 3610 |
A new method of processing the time-concentration data of reaction kinetics Yeow YL, Wickramasinghe SR, Han BB, Leong YK |
3611 - 3620 |
Multicomponent phase equilibria of thin liquid films and their vapour Stephan K |
3621 - 3628 |
Diffusion coefficient of a charged porous sphere Natraj V, Chen SB |
3629 - 3641 |
Flammability characteristics of pure hydrocarbons Albhari TA |
3643 - 3658 |
Optimal grade transition and selection of closed-loop controllers in a gas-phase olefin polymerization fluidized bed reactor Chatzidoukas C, Perkins JD, Pistikopoulos EN, Kiparissides C |
3659 - 3668 |
Characteristics and reactivities of Ca(OH)(2)/silica fume sorbents for low-temperature flue gas desulfurization Lin RB, Shih SM, Liu CF |
3669 - 3680 |
The influence of the riser exit on the particle residence time distribution in a circulating fluidised bed riser Harris AT, Davidson JF, Thorpe RB |
3681 - 3698 |
Computationally efficient solution of population balance models incorporating nucleation, growth and coagulation: application to emulsion polymerization Immanuel CD, Doyle FJ |
3699 - 3713 |
Knowledge-based hybrid modelling of a batch crystallisation when accounting for nucleation, growth and agglomeration phenomena Georgieva P, Meireles MJ, de Azevedo SF |
3715 - 3727 |
Simulation and analysis of industrial crystallization processes through multidimensional population balance equations. Part 1: a resolution algorithm based on the method of classes Puel F, Fevotte G, Klein JP |
3729 - 3740 |
Simulation and analysis of industrial crystallization processes through multidimensional population balance equations. Part 2: a study of semi-batch crystallization Puel F, Fevotte G, Klein JP |
3741 - 3752 |
A nonlinear inverse problem in simultaneously estimating the heat and mass production rates for a chemically reacting fluid Huang CH, Yeh CY, Orlande HRB |
3753 - 3763 |
Performance analysis and fuzzy optimization of a two-stage fermentation process with cell recycling including an extractor for lactic acid production Wang FS, Lin KJ |
3765 - 3776 |
Analytical and numerical evaluation of two-fluid model solutions for laminar fully developed bubbly two-phase flows Azpitarte OE, Buscaglia GC |
3777 - 3792 |
Hydrodynamics of binary fluidization in a riser: CFD simulation using two granular temperatures Lu HL, Gidaspow D |
3793 - 3806 |
Effects of surface-active agents on mass transfer of a solute into single buoyancy driven drops in solvent extraction systems Li XJ, Mao ZS, Fei WY |
3807 - 3816 |
Assessment of the effect of velocity and residence time in CaSO4 precipitating flow reaction Walker P, Sheikholeslami R |
3817 - 3828 |
Continuous optimization using a dynamic simplex method Xiong Q, Jutan A |
3829 - 3835 |
A new characteristic of liquid-liquid systems-inversion holdup of intensely agitated dispersions Deshpande KB, Kumar S |