2589 - 2604 |
Application of life cycle assessment to chemical processes Burgess AA, Brennan DJ |
2605 - 2614 |
The induction of pulses in trickle-bed reactors by cycling the liquid feed Boelhouwer JG, Piepers HW, Drinkenburg AAH |
2615 - 2628 |
Magnetic resonance imaging as a quantitative probe of gas-liquid distribution and wetting efficiency in trickle-bed reactors Sederman AJ, Gladden LF |
2629 - 2639 |
A Lagrangian description of flows in stirred tanks via computer-automated radioactive particle tracking (CARPT) Rammohan AR, Kemoun A, Al-Dahhan MH, Dudukovic MP |
2641 - 2658 |
Reversing flow catalytic converter for a natural gas/diesel dual fuel engine Liu B, Hayes RE, Checkel MD, Zheng M, Mirosh E |
2659 - 2670 |
Experiments and simulations of methane oxidation on a platinum surface Dupont V, Zhang SH, Williams A |
2671 - 2683 |
Modelling of a catalytic plate reactor for dehydrogenation-combustion coupling Zanfir M, Gavriilidis A |
2685 - 2693 |
Preparation of silicon-carbide-coated activated carbon using a high-temperature fluidized bed reactor Atwater JE, Akse JR, Wang TC, Kimura S, Johnson DC |
2695 - 2702 |
Effectiveness factors in an electrochemical reactor with rotating cylinder electrode for the acid-cupric/copper cathode interface process de Oca JLNM, Sosa E, de Leon CP, Oropeza MT |
2703 - 2713 |
Characterization of the residence time distribution in loop reactors Melo PA, Pinto JC, Biscaia EC |
2715 - 2720 |
Time-dependent finite-volume simulation of the turbulent flow in a free-surface CSTR Serra A, Campolo M, Soldati A |
2721 - 2732 |
Airlift-driven external-loop tubular photobioreactors for outdoor production of microalgae: assessment of design and performance Fernandez FGA, Sevilla JMF, Perez JAS, Grima EM, Chisti Y |
2733 - 2744 |
A novel fountain photocatalytic reactor: model development and experimental validation Puma GL, Yue PL |
2745 - 2759 |
Air-prepurification by pressure swing adsorption using single/layered beds Rege SU, Yang RT, Qian KY, Buzanowski MA |
2761 - 2766 |
Correlating laminar burning velocities using perfectly stirred reactor theory Barat RB |
2767 - 2774 |
Minimum time constrained control of acid strength on a sulfuric acid alkylation unit Petit N, Creff Y, Lemaire L, Rouchon P |
2775 - 2787 |
Robust stabilization of jacketed chemical reactors by PID controllers Alvarez-Ramirez J, Morales A |
2789 - 2801 |
Diffusion of small molecules in disordered media: study of the effect of kinetic and spatial heterogeneities Karayiannis NC, Mavrantzas VG, Theodorou DN |
2803 - 2819 |
Pore network model of deactivation of immobilized glucose isomerase in packed-bed reactors - I: Two-dimensional simulations at the particle level Dadvar M, Sohrabi M, Sahimi M |
2821 - 2830 |
Analysis of the pulse response in a CSTR for diffusion measurement in bi-porous adsorbent pellets Schwan P, Moller KP |
2831 - 2836 |
Discrete and continuous models for polymerization and depolymerization McCoy BJ, Madras G |
2837 - 2849 |
Nonlinear behavior of an ideal reactor separator network with mass recycle Pushpavanam S, Kienle A |
2851 - 2857 |
Rectification of flow measurements in continuous processes subject to fluctuations Dovi VG, Del Borghi A |
2859 - 2866 |
Study of mixing in gas-fluidized beds using a DEM model Rhodes MJ, Wang XS, Nguyen M, Stewart P, Liffman K |
2867 - 2878 |
The effect of surfactants on expanding free surfaces Breward CJW, Darton RC, Howell PD, Ockendon JR |
2879 - 2888 |
Surface tension of aqueous electrolyte solutions at high concentrations - representation and prediction Li ZB, Lu BCY |
2889 - 2895 |
Thermal diffusion in a countercurrent-flow Frazier scheme inclined for improved performance Yeh HM |
2897 - 2897 |
Unsteady state operation of catalytic particles with constant and periodically changing degree of external wetting (vol 53, pg 3129, 1998) Kouris C, Neophytides S, Vayenas CG, Tsamopoulos JA |