5 - 11 |
Testing a mathematical model for initial chemical reaction fouling using a dilute protein solution Rose IC, Watkinson AP, Epstein N |
12 - 20 |
The effect of surface properties on CaSO4 scale formation during convective heat transfer and subcooled flow boiling Muller-Steinhagen H, Zhao Q, Helali-Zadeh A, Ren XG |
21 - 31 |
Coprecipitation of CaCO3 and CaSO4 Sudmalis M, Sheikholeslami R |
32 - 39 |
Correlations for the particle deposition rate accounting for lift forces and hydrodynamic mobility reduction Adomeit P, Renz U |
40 - 52 |
The fouling of alloy-800 heat exchange surfaces by magnetite particles Basset M, McInerney J, Arbeau N, Lister DH |
53 - 60 |
Thermal resistance of steam-generator tube deposits under single-phase forced convection and flow-boiling heat transfer Turner CW, Klimas SJ, Brideau MG |
61 - 64 |
The control of biofilms in tubes using wire-wound inserts Wills A, Bott TR, Gibbard IJ |
65 - 74 |
Gas mixing in a turbulent fluidized bed reactor Sotudeh-Gharebaagh R, Chaouki J |
75 - 81 |
Microstructural aspects of the flow behaviour in a liquid-solids circulating fluidized bed Zheng Y, Zhu JX |
82 - 94 |
(Gas-) liquid-solid circulating fluidized beds and their potential applications to bioreactor engineering Zhu JX, Zheng Y, Karamanev DG, Bassi AS |
95 - 101 |
Effects of oxygen supply condition and specific biofilm interfacial area on phenol removal rate in a three-phase fluidized bed bioreactor Hirata A, Meutia AA, Osawa M, Arai M, Tsuneda S |
102 - 110 |
Fluidized state gelation of ceramic microspheres: Feasibility study of a continuous process and analysis of the chemical dehydration phenomena Rovero G, Vanni M |
111 - 123 |
Modelling FCC units under steady and unsteady state conditions Arandes JM, Azkoiti MJ, Bilbao J, de Lasa HI |
124 - 131 |
A model for the evaporation of water from large glass particles in pneumatic transport Littman H, Day JY, Morgan MH |
132 - 142 |
Voidage and particle velocity profiles in a spout-fluid bed Pianarosa DL, Freitas LAP, Lim CJ, Grace JR, Dogan OM |
143 - 155 |
Three-stage well-mixed reactor model for a pressurized coal gasifier Song BH, Watkinson AP |
156 - 160 |
Gas spouting hydrodynamics of fine particles Wang SN, Xu J, Wei WS, Shi G, Bao XJ, Bi HT, Lim CJ |
161 - 167 |
Pressure gradients, voidage and gas flow in the annulus of spouted beds He YL, Lim CJ, Grace JR |
168 - 174 |
Mechanism of selenium sorption by activated carbon Jadhav RA, Agnihotri R, Gupta H, Fan LS |
175 - 181 |
Measurement and correlation of the individual ionic activity coefficients of aqueous electrolyte solutions of KF, NaF and KBr Taghikhani V, Modarress H, Vera JH |
182 - 193 |
Kinetic modelling of oxygen dependence in oxidative dehydrogenation of propane Creaser DC, Andersson B, Hudgins RR, Silveston PL |
194 - 204 |
Fractionation of nylon fibres using a vertical settler Chen JX, Masliyah JH |
205 - 210 |
Lateral mixing of shallow liquid pools by air bubbling Baird MHI, Rao NVR |
211 - 220 |
Flow patterns and oil-water dispersion in a 0.38 m diameter oscillatory baffled column Ni XW, Nelson G, Mustafa I |
221 - 225 |
Enhancement of the interfacial transfer of iodine by chemical reaction Evans GJ, Ling JR |
226 - 231 |
Degradation of solvolysis lignin using Lewis acid catalysts Hepditch MM, Thring RW |
232 - 236 |
Physical solubility of hydrogen sulfide in several aqueous solvents Rinker EB, Sandall OC |
237 - 247 |
Nonlinear control of competitive mixed-culture bioreactors via specific cell adhesion Kurtz MJ, Henson MA, Hjortso MA |
248 - 260 |
Comparison of two types of flows (crossflow and swirling flow) in ultrafiltration modules - Influence of the wall constraint Morineau-Thomas O, Lelievre C, Rossignol N, Jaouen P, Legentilhomme P |
261 - 264 |
Axial mixing and gas holdup with reciprocating doughnut plates Rao NVR, Baird MHI |
265 - 270 |
Mixing of a lignin-based slurry fuel Posarac D, Watkinson AP |
271 - 272 |
Interaction between Art & Science Tamir A |