| 2879 - 2884 |
Investigation of the filtration rate of silica in aluminum fluoride production from silicic acid
Bayat M, Taeb A, Rastegar S |
| 2885 - 2899 |
Diffusiophoresis of a colloidal sphere in nonelectrolyte gradients parallel to one or two plane walls
Chen PY, Keh HJ |
| 2901 - 2905 |
Evaporation-induced pattern formation in polymer films via secondary phase separation
Yamamura M, Nishio T, Kajiwara T, Adachi K |
| 2907 - 2920 |
On the validity of thermogravimetric determination of carbon gasification kinetics
Feng B, Bhatia SK |
| 2921 - 2931 |
Electrolyte transport through amphoteric nanofiltration membranes
Fievet P, Labbez C, Szymczyk A, Vidonne A, Foissy A, Pagetti J |
| 2933 - 2944 |
On the apparent permeability of a porous layer backed by a perforated plate
Dufreche J, Prat M, Schmitz P, Sherwood JD |
| 2945 - 2953 |
A study by in situ techniques of the thermal evolution of the structure of a Mg-Al-CO3 layered double hydroxide
Yang WS, Kim Y, Liu PKT, Sahimi M, Tsotsis TT |
| 2955 - 2969 |
Operation of semi-batch emulsion polymerisation reactors: Modelling, validation and effect of operating conditions
Zeaiter J, Romagnoli JA, Barton GW, Gomes VG, Hawkett BS, Gilbert RG |
| 2971 - 2985 |
A fuzzy diagnosis approach using dynamic fault trees
Chang SY, Lin CR, Chang CT |
| 2987 - 2994 |
Influence of viscosity and surface tension on performance of gas-liquid contactors with ejector type gas distributor
Elgozali A, Linek V, Fialova M, Wein O, Zahradnik J |
| 2995 - 3004 |
Methanol synthesis in a forced unsteady-state reactor network
Velardi SA, Barresi AA |
| 3005 - 3011 |
Closed-loop automatic tuning of PID controller for nonlinear systems
Tan KK, Ferdous R, Huang S |
| 3013 - 3024 |
Study on diffusion and flow of benzene, n-hexane and CCl4 in activated carbon by a differential permeation method
Bae JS, Do DD |
| 3025 - 3032 |
Dynamic wetting in metering and pre-metered forward roll coating
Benkreira H |
| 3033 - 3045 |
Modelling diffusion and reaction accompanied by capillary condensation using three-dimensional pore networks. Part 1. Fickian diffusion and pseudo-first-order reaction kinetics
Wood J, Gladden LF |
| 3047 - 3059 |
Modelling diffusion and reaction accompanied by capillary condensation using three-dimensional pore networks. Part 2. Dusty gas model and general reaction kinetics
Wood J, Gladden LF, Keil FJ |
| 3061 - 3071 |
Modeling of supercritical water oxidation of phenol catalyzed by activated carbon
Nunoura T, Lee GH, Matsumura Y, Yamamoto K |
| 3073 - 3084 |
Modelling of micro-particle agglomeration in turbulent flows
Ho CA, Sommerfeld M |
| 3085 - 3093 |
The combined use of in-bed monitoring and an adsorption model to anticipate breakthrough during expanded bed adsorption
Bruce LJ, Chase HA |
| 3095 - 3106 |
IDEAS approach to process network synthesis: minimum utility cost for complex distillation networks
Drake JE, Manousiouthakis V |
| 3107 - 3117 |
Particle flow, mixing, and chemical reaction in circulating fluidized bed absorbers
Mao D, Edwards JR, Kuznetsov AV, Srivastava R |
| 3119 - 3131 |
Stress effects on the conductivity of particulate beds
Vargas WL, McCarthy JJ |
| 3133 - 3140 |
Effects of crystal growth rate and heat and mass transfer on solute distribution
Fukui K, Maeda K |
| 3141 - 3147 |
Removal of aerosols by bubbling through porous media submerged in organic liquid
Agranovski IE, Myojo T, Braddock RD |
| 3149 - 3153 |
Prediction of the inversion velocity in the binary-solid liquid fluidized bed
Hu XH |
