723 - 732 |
Inverse size-exclusion chromatography for distributed pore and solute sizes Goto M, McCoy BJ |
733 - 747 |
Particle morphology of calcium carbonate precipitated by gas-liquid reaction in a Couette-Taylor reactor Jung WM, Kang SH, Kim WS, Choi CK |
749 - 758 |
Ethylene epoxidation in a catalytic packed-bed membrane reactor: effects of reactor configuration and 1,2-dichloroethane addition Lafarga D, Varma A |
759 - 765 |
Evaluation of hydrogen transfer in FCC catalysts. A new approach for cyclohexene as a test reactant de la Puente G, Sedran U |
767 - 771 |
Numerical tracking and circulation time distribution in an infinite Taylor system Khellaf K, Lauriat G, Legrand J |
773 - 781 |
Material coordinates and solute movement in consolidating clay Smiles DE |
783 - 795 |
Bioleaching of a pyrrhotite ore by a sulfooxidans strain: kinetic analysis Veglio F, Beolchini F, Nardini A, Toro L |
797 - 805 |
Investigation on fouling behaviors of low-energy surface and fouling fractal characteristics Yang QF, Ding J, Shen ZQ |
807 - 816 |
A nonlinear profile observer using tray temperatures for high-purity binary distillation column control Shin J, Seo H, Han M, Park S |
817 - 825 |
Correlative biosorption equilibria model for a binary batch system Ho YS, McKay G |
827 - 837 |
Selection of optimal sensor position in a tubular reactor using robust degree of observability criteria van den Berg FWJ, Hoefsloot HCJ, Boelens HFM, Smilde AK |
839 - 847 |
Turbulence structure of the solid phase in transition region of a circulating fluidized bed Zhou HS, Lu JD, Lin LA |
849 - 855 |
Asymptotic solutions for laminar dispersion in circular tubes Vrentas JS, Vrentas CM |
857 - 866 |
Numerical simulation of fluid dynamics in fluidized beds with horizontal heat exchanger tubes Gustavsson M, Almstedt AE |
867 - 879 |
Two-fluid modelling of cooling-tube erosion in a fluidized bed Gustavsson M, Almstedt AE |