| 71 - 79 |
Interfacial area in a reactor with helicoidal flow for the two-phase gas-liquid system
Wronski S, Hubacz R, Ryszczuk T |
| 81 - 89 |
Fluidized bed combustion and desulfurization of a heavy liquid fuel
Miccio F, Okasha FA |
| 91 - 98 |
Optimal growth conditions and the cultivation of Chaetoceros calcitrans in airlift photobioreactor
Krichnavaruk S, Loataweesup W, Powtongsook S, Pavasant P |
| 99 - 109 |
Nonlinear phenomena and qualitative evaluation of risk of clogging in a capillary microreactor under, imposed electric field
Pribyl M, Snita D, Marek M |
| 111 - 115 |
Study of the operational parameters involved in designing a particle bed reactor for the removal of lead from industrial wastewater -central composite design methodology
Kaminari NMS, Ponte MJJS, Ponte HA, Neto AC |
| 117 - 130 |
Numerical experiments on variants and parameters of the simulated annealing method
Pibouleau L, Domenech S, Davin A, Azzaro-Pantel C |
| 131 - 138 |
Optimization of batch process parameters using response surface methodology for dye removal by a novel adsorbent
Ravikumar K, Pakshirajan K, Swaminathan T, Balu K |
| 139 - 145 |
Process analysis for treatment of industrial plating wastewater: simulation and control approach
Aguilar R, Martinez SA, Rodriguez MG, Soto G |
| 147 - 152 |
Supercritical CO2 extraction of gamma-linolenic acid (GLA) from the cyanobacterium Arthrospira (Spirulina)maxima: experiments and modeling
Mendes RL, Reis AD, Pereira AR, Cardoso MT, Palavra AF, Coelho JP |
