| 3957 - 3966 |
Electrically heated converters for automotive emission control: determination of the best size regime for the heated element
Bissett EJ, Oh SH |
| 3967 - 3976 |
Uncatalysed oxidation of cyclohexene
Mahajani SM, Sharma MM, Sridhar T |
| 3977 - 3993 |
Nonequilibrium effects in fixed-bed interstitial fluid dispersion
Kronberg AE, Westerterp KR |
| 3995 - 4006 |
Bubble recirculation regimes in an internal-loop airlift reactor
van Benthum WAJ, van der Lans RGJM, van Loosdrecht MCM, Heijnen JJ |
| 4007 - 4022 |
Bubble size distribution and coarsening of aqueous foams
Magrabi SA, Dlugogorski BZ, Jameson GJ |
| 4023 - 4030 |
Experimental investigations of cake characteristics in crossflow microfiltration
Hamachi M, Mietton-Peuchot M |
| 4031 - 4040 |
Estimation of overall effective coefficient of heat transfer for nonisothermal fixed-bed adsorption
Lin WC, Farooq S, Tien C |
| 4041 - 4051 |
Dynamic behaviour of the mixer-settler cascade. Extractive separation of the rare earths
Wichterlova J, Rod V |
| 4053 - 4060 |
A model for bubble-to-jet transition at a submerged orifice
Sundar R, Tan RBH |
| 4061 - 4063 |
Mass transfer kinetics for interfacially perturbed vertical liquid films
Floarea O, Dobre T, Dinu SV |
| 4065 - 4087 |
Screening models for batch process development: Part II. Case studies
Allgor RJ, Barton PI |
| 4089 - 4098 |
Maxwell-Stefan theory for macropore molecular-diffusion-controlled fixed-bed adsorption
Wang R, Farooq S, Tien C |
| 4099 - 4109 |
Residence time, mass transfer and back-mixing of the liquid in trickle flow reactors containing porous particles
Iliuta I, Larachi F, Grandjean BPA |
| 4111 - 4121 |
Analysis of a tubular zeolite membrane process
Karimi IA, Farooq S |
