| 1 - 21 |
Calculating distillation efficiencies of multicomponent i-butane/n-butane column
Ilme J, Klemola K, Aittamaa J, Nystrom L |
| 23 - 33 |
Vapor-liquid equilibria of toluene plus n-butanol and toluene plus n-butanol plus calcium chloride at 94.0 kPa
Darwish NA, Al-Khateib AA |
| 35 - 47 |
A new internal model control scheme with simplified design and implementation
Wang QG, Zhang Y, Zhang Y |
| 49 - 69 |
A fixed bed barrier reactor with separate feed of reactants
Neomagus HWJP, Saracco G, Versteeg GF |
| 71 - 88 |
Turbulent resistance of complex bed structures
Tobis J |
| 89 - 103 |
A fuzzy decision-making computer aided system for the preliminary selection of agitator
Wang JJ, Feng LF, Gu XP, Wang K |
| 105 - 124 |
Droplet size-velocity characteristics of sprays generated by two-phase feed nozzles
Copan J, Balachandar R, Berruti F |
| 125 - 138 |
Pore scale model for flow regime transition in a trickle bed reactor
Revankar ST |
| 139 - 155 |
Visualizing the entrapment of air pockets in the shell of a hemodialyzer during wet-out
Frank A, Lipscomb GG, Dennis M |
| 157 - 174 |
Ozonation kinetics of phenolic compounds present in table olive wastewaters: p-hydroxybenzoic acid, tyrosol and p-coumaric acid
Beltran J, Torregrosa J, Dominguez JR, Peres JA |
| 175 - 192 |
A thermodynamic model for gas hydrates in the presence of salts and methanol
Zuo JY, Zhang D, Stenby EH |
| 193 - 220 |
Cooling and solidification in the presence of reciprocating non-Newtonian shear flow: The live feed injection moulding process
Pittman JFT, Aguirre P, Ding D |
| 221 - 228 |
Estimation of heat of vaporization of pure liquid at its normal boiling temperature
Liu ZY |
| 229 - 257 |
The laminar flow tubular reactor with homogeneous and heterogeneous reactions - I. Integral equations for diverse reaction rate regimes
Grau RJ, Cabrera MI, Cassano AE |
