| 1111 - 1119 |
Use of asymmetric hollow fibre modules for elimination of H2S from gas streams via a membrane absorption method
Li K, Wang DL, Koe CC, Teo WK |
| 1121 - 1130 |
Steady-state analysis of simulated moving-bed chromatography using the linear, ideal model
Zhong GM, Guiochon G |
| 1131 - 1144 |
The rheology and processing of a concentrated cellulose acetate solution
Wee WK, Mackley MR |
| 1145 - 1151 |
Robust multivariable control using an SVD-based controller
Zhu ZX, Jutan A |
| 1153 - 1162 |
Scale and variance of radial liquid maldistribution in trickle beds
Wang YF, Mao ZS, Chen JY |
| 1163 - 1173 |
A sulphur capture model for circulating fluidized-bed boilers
Mattisson T, Lyngfelt A |
| 1175 - 1201 |
On non-Newtonian fluid flow in ducts and porous media
Liu SJ, Masliyah JH |
| 1203 - 1208 |
Permeability of sheets of nonwoven fibrous media
Termonia Y |
| 1209 - 1221 |
High-order approximations for noncyclic and cyclic adsorption in a particle
Lee JT, Kim DH |
| 1223 - 1231 |
Direct forward gravure coating on unsupported web
Benkreira H, Cohu O |
| 1233 - 1238 |
The speed, direction and stability of concentration shocks in a fluidised bed
Sergeev YA, Gibilaro LG, Foscolo PU, Brandani S |
| 1239 - 1252 |
Maxwell-Stefan analysis of multicomponent transient diffusion in a capillary and adsorption of hydrocarbons in activated carbon particle
Do HD, Do DD |
| 1253 - 1265 |
Modelling of combined Navier-Stokes and Darcy flows in crossflow membrane filtration
Nassehi V |
| 1267 - 1276 |
Relationship between bubble size distributions and chord-length distribution in heterogeneously bubbling systems
Liu WD, Clark NN, Karamavruc AI |
| 1277 - 1293 |
An on-line monitoring procedure for 2x2 and 3x3 full multivariable control systems
Ju J, Chiu MS |
| 1295 - 1305 |
Equilibrium theory for binary solvent vapor recovery by pressure swing adsorption : conceptual process design for separation of the lighter component
Subramanian D, Ritter JA |
| 1307 - 1310 |
Modelling of heat transfer in fluidized-bed coating of thin plates
Leong KC, Lu GQM, Bhatia SK, Rudolph V |
| 1311 - 1315 |
Parabolic intraparticle concentration profile assumption in modeling and simulation of nonlinear simulated moving-bed separation processes
Ching CB, Lu ZP |
| 1317 - 1318 |
Some comments on "Deposition in narrow channels"
Hogarth WL, Parlange JY, Wallach R |
| 1319 - 1320 |
Reply to comments on "Deposition in narrow channels"
Philip JR |
