3419 - 3428 |
Reliable computation of solid solubility in dense gases through homotopy continuation approach Aslam N, Sunol AK |
3429 - 3434 |
Static mixers with a gas continuous phase Couvert A, Sanchez C, Charron I, Laplanche A, Renner C |
3435 - 3451 |
Granular attrition in a rotary valve: Attrition product size and shape Yao J, Wang CH, Lim EWC, Bridgwater J |
3452 - 3462 |
Oxidation kinetics of iron(II) complexes of trans-1,2-diaminocyclohexanetetraacetate (cdta) with dissolved oxygen: Reaction mechanism, parameters of activation and kinetic salt effects Piche S, Larachi F |
3463 - 3475 |
Modeling of batch phenol biodegradation in internal loop airlift bioreactor with gas recirculation by Candida tropicalis Jia XQ, Wen JP, Jiang Y, Liu XL, Feng W |
3476 - 3495 |
Kinetic simulation of methane hydrate formation and dissociation in porous media Sun XF, Mohanty KK |
3496 - 3505 |
Spin and dip coating of light-emitting polymer solutions: Matching experiment with modelling Yimsiri P, Mackley MR |
3506 - 3518 |
Gas/liquid dispersions with a SMX static mixer in the laminar regime Fradette L, Li HZ, Choplin L, Tanguy P |
3519 - 3531 |
Generalized linear driving force approximation for adsorption of multicomponent mixtures Cruz P, Magalhaes FD, Mendes A |
3532 - 3542 |
Heat transfer of gas flow through a packed bed Wen DS, Ding YL |
3543 - 3549 |
A note on the modelling of the bouncing of spherical drops or solid spheres on a wall in viscous fluid Legendre D, Zenit R, Daniel C, Guiraud P |
3550 - 3563 |
Diffusiophoresis of a colloidal sphere in nonelectrolyte gradients in a circular cylindrical pore Keh HJ, Hsu YS |
3564 - 3576 |
Kinetics of Pd/alumina catalysed 1,2-dichloroethane gas-phase oxidation Aranzabal A, Gonzalez-Marcos JA, Ayastuy JL, Gonzalez-Velasco JR |
3577 - 3585 |
Two-dimensional modeling of the effects of insoluble surfactant on the breakup of a liquid filament Dravid V, Songsermpong S, Xue ZJ, Corvalan CA, Sojka PE |
3586 - 3592 |
Two-dimensional numerical simulations of Marangoni-Benard instabilities during liquid-liquid mass transfer in a vertical gap Grahn A |
3593 - 3601 |
Experimental investigation of dilute turbulent particulate flow inside a curved 90 degrees bend Yang W, Kuan B |
3602 - 3609 |
Treatment of industrial liquid wastes by electrocoagulation: Experimental investigations and an overall interpretation model Khemis M, Leclerc JP, Tanguy G, Valentin G, Lapicque F |
3610 - 3622 |
Effect of antifoam agents on bubble characteristics in bubble columns based on acoustic sound measurements Al-Masry WA, Ali EM, Aqeel YM |
3623 - 3631 |
Electrowinning of copper in two- and three-compartment reactive electrodialysis cells Cifuentes L, Grageda M, Crisostomo G |
3632 - 3642 |
Experimental study of the slug/churn flow transition in a single Taylor bubble Carvalho JRFG |
3643 - 3652 |
Unsteady extinction mechanism of nonpremixed flame interacting with a vortex Oh CB, Hwang CH, Lee CE, Park J |
3653 - 3662 |
The second-law optimal operation of a paper drying machine Zvolinschi A, Johannessen E, Kjelstrup S |
3663 - 3673 |
Modeling of the evolution with length of bubble size distributions in bubble columns Bordel S, Mato R, Villaverde S |
3674 - 3685 |
Mathematical modelling of solvent drying from a static particle bed Kohout M, Collier AP, Stepanek F |
3686 - 3697 |
Derivation of filtration equations incorporating the effect of pressure redistribution on the cake-medium interface: A constant pressure filtration Vorobiev E |
3698 - 3704 |
Solubility of gases in a hydroformylation solvent Still C, Salmi T, Maki-Arvela P, Eranen K, Murzin DY, Lehtonen J |
3705 - 3713 |
A stochastic model for breakage frequency of viscous drops in turbulent dispersions Das PK |
3714 - 3724 |
Numerical study on development of particle concentration profiles in a curved microchannel Ookawara S, Street D, Ogawa K |
3725 - 3735 |
An approximate method for solving gas-solid non-catalytic reactions Gomez-Barea A, Ollero P |
3736 - 3745 |
Characterization of bore pressure change effects on Matrimid (R) fiber performance in pervaporation of acetic acid and water mixtures Zhou FB, Koros WJ |
3746 - 3760 |
Modelling of comminution processes in Spex Mixer/Mill Concas A, Lai N, Pisu M, Cao G |
3761 - 3770 |
Comparison of the adsorption performance of compound adsorbent in a refrigeration cycle with and without mass recovery Wang LW, Wang RZ, Lu ZS, Chen CJ, Wu JY |
3771 - 3779 |
Volumetric power consumption in baffled shake flasks Peter CP, Suzuki Y, Rachinskiy K, Lotter S, Buchs J |
3780 - 3784 |
Concept of nano-reactor for the control of the selectivity of the free radical grafting of maleic anhydride onto polypropylene in the melt Shi D, Hu GH, Li RKY |
3785 - 3790 |
q-exponential structure of arbitrary-order reaction kinetics Niven RK |
3791 - 3791 |
Comments on "Application of a three-layer modelling approach for solids transport in horizontal and inclined channels" A. Ramadan, P. Skalle, A. Saasen [Chemical Engineering Science 2005, 60, 2557-2570] Stevenson P |
3792 - 3793 |
Response to comments on: "Application of a three-layer modeling approach for solids transportation in horizontal and inclined channels" by A. Ramadan, P. Skalle, and A. Saasen Ramadan A |