2143 - 2150 |
Alternative designs for a catalytic converter operating under autothermal conditions Lopez E, Errazu AF, Borio DO, Bucala V |
2151 - 2160 |
Measurement of uni-axial fiber angle in non-woven fibrous media Chase GG, Beniwal V, Venkataraman C |
2161 - 2171 |
Design of novel monolith catalyst supports for gas/solid reactions with heat exchange Groppi G, Tronconi E |
2173 - 2184 |
Agglomeration of yttrium oxalate particles produced by reaction precipitation in semi-batch reactor Sung MH, Choi IS, Kim JS, Kim WS |
2185 - 2194 |
H2S gas treatment by iron bioprocess Pagella C, De Faveri DM |
2195 - 2201 |
Supercritical CO2 extraction of hiprose seed oil: experiments and mathematical modelling Reverchon E, Kaziunas A, Marrone C |
2203 - 2212 |
Measurements of solid contaminant emission rates from boiling pools Dayan A, Zalmanovich S, Ullmann A |
2213 - 2222 |
Numerical modelling of sedimentation processes White DA, Verdone N |
2223 - 2236 |
Effect of preparation conditions on morphology and release profiles of biodegradable polymeric microspheres containing protein fabricated by double-emulsion method Yang YY, Chung TS, Bai XL, Chan WK |
2237 - 2247 |
Parameter estimation of a proton-exchange membrane fuel cell using voltage-current data Suares GE, Hoo KA |
2249 - 2256 |
Transient study of the effect of residual cations in Cu/ZSM-5 for SCR of NO by hydrocarbon Mongkolsiri N, Praserthdam P, Silveston PL, Hudgins RR |
2257 - 2263 |
Comparison of the hydrodynamics and mass transfer characteristics of a modified square airlift reactor with common airlift reactors Lu XP, Ding J, Wang YR, Shi J |
2265 - 2270 |
Upon equilibrium of gas bubble in infinite liquid Mitrovic J |
2271 - 2286 |
Modelling steady state and ignition during catalytic methane oxidation in a monolith reactor Veser G, Frauhammer J |
2287 - 2294 |
A fluid-dynamic model for flow pattern on a distillation tray Liu CJ, Yuan XG, Yu KT, Zhu XJ |
2295 - 2301 |
On dissolution of a spherical gas bubble in the presence of fast reaction Long WM, Kalachev LV |
2303 - 2313 |
The no-flow problem for granular material in rotating kilns and dish granulators Spurling RJ, Davidson JF, Scott DM |
2315 - 2327 |
Model validation for industrial model predictive control systems Huang B, Tamayo EC |
2329 - 2338 |
Heat transfer in fixed bed: a model non-linearity approach Thomeo JC, Freire JT |
2339 - 2342 |
Power consumption of inner-outer helical ribbon impellers in viscous Newtonian and non-Newtonian fluids Wang JJ, Feng LF, Gu XP, Wang K, Hu CH |
2343 - 2344 |
Comments on "Dynamic simulation of dispersed gas-liquid two-phase flow using a discrete bubble model" by E. Delnoij, F. A. Lammers, J. A. M. Kuipers, and W. P. M. van Swaaij [Chemical Engineering Science 52 (1997) 1429-1458] Karamanev D |
2345 - 2346 |
Reply to comments on "Dynamic simulation of dispersed gas-liquid two-phase flow using a discrete bubble model" Delnoij E, Kuipers JAM |
2347 - 2347 |
The boiling slurry reactor: Axial dispersion model (vol 54, pg 5021, 1999) Khinast JG, Luss D, Leib TM, Harold MP |
2349 - 2349 |
Diffusion and reaction in biofilms (vol 53, pg 397, 1998) Wood BD, Whitaker S |