4385 - 4397 |
Simulation of transients in heterogeneous catalysis: a comparison of the step- and pulse-transient techniques for the study of hydrocarbon oxidation on metal oxide catalysts Hinz A, Nilsson B, Andersson A |
4399 - 4413 |
Experiments on a square planform steel silo Brown CJ, Lahlouh EH, Rotter JM |
4415 - 4421 |
Effects of inertia on the slow motion of aerosol particles Keh HJ, Shiau SC |
4423 - 4434 |
A large eddy PIV method for turbulence dissipation rate estimation Sheng J, Meng H, Fox RO |
4435 - 4450 |
Robust H-infinity control of nonlinear plants based on multi-linear models: an application to a bench-scale pH neutralization reactor Galan O, Romagnoli JA, Palazoglu A |
4451 - 4460 |
A numerical model for packed-bed combustion of char particles Cooper J, Hallett WLH |
4461 - 4479 |
Dynamics and stability analysis of solid catalyzed gas-phase polymerization of olefins in continuous stirred bed reactors Gorbach AB, Naik SD, Ray WH |
4481 - 4494 |
Flow patterns and velocity fields of granules in Dorfan Impingo filters for gas cleanup Hsiau SS, Smid J, Tsai HH, Kuo JT, Chou CS |
4495 - 4513 |
Calculation of the effective permeabilities of held-scale porous media Mukhopadhyay S, Sahimi M |
4515 - 4524 |
Quasi-equilibrium bubble formation during top-submerged gas injection Liow JL |
4525 - 4535 |
Molecular sieve sorbents for kinetic separation of propane/propylene Padin J, Rege SU, Yang RT, Cheng LS |
4537 - 4547 |
Gas chromatographic simulated moving bed separation of the enantiomers of the inhalation anesthetic enflurane Biressi G, Quattrini F, Juza M, Mazzotti M, Schurig V, Morbidelli M |
4549 - 4562 |
The influence of chemical composition on vaporisation of LNG and LPG on unconfined water surfaces Conrado C, Vesovic V |
4563 - 4570 |
The K-L reactor model for circulating fluidized beds Kunii D, Levenspiel O |
4571 - 4582 |
Effects of hydrolysis and esterification side-reactions on the kinetic resolution of enzyme-catalyzed irreversible transesterification in organic solvents Tsai SW, Cheng IC, Huang CM |
4583 - 4595 |
Multivariable model validation in the presence of time-variant disturbance dynamics Huang B |
4597 - 4609 |
Discrete-phase simulation of single bubble rise behavior at elevated pressures in a bubble column Li Y, Zhang JP, Fan LS |
4611 - 4627 |
Prediction of particle size distribution in suspension polymerization reactors: effect of turbulence nonhomogeneity Maggioris D, Goulas A, Alexopoulos AH, Chatzi EG, Kiparissides C |
4629 - 4641 |
Modeling of electrodialysis of metal ion removal from pulp and paper mill process stream Yu ZQ, Admassu W |
4643 - 4652 |
Use of limestone for SO2 removal from flue gas in the semidry FGD process with a powder-particle spouted bed Ma XX, Kaneko T, Tashimo T, Yoshida T, Kato K |
4653 - 4665 |
Bubble formation from wall orifice in liquid cross-flow under low gravity Nahra HK, Kamotani Y |
4667 - 4680 |
State estimation of batch distillation columns using an extended Kalman filter Oisiovici RM, Cruz SL |
4681 - 4697 |
Numerical modeling of wavy stratified two-phase flow in pipes Meknassi F, Benkirane R, Line A, Masbernat L |
4699 - 4708 |
Pressure drop calculation and modelling of inclined intermittent gas-liquid flow Cook M, Behnia M |
4709 - 4718 |
A fully distributed model for the simulation of a catalytic combustor Wanker R, Raupenstrauch H, Staudinger G |
4719 - 4735 |
Fine drop recovery in batch gas-agitated liquid-liquid systems Shahrokhi H, Shaw JM |
4737 - 4743 |
A combined bulk chemistry/electrochemical approach to study the precipitation, deposition and inhibition of CaCO3 Neville A, Morizot AP |
4745 - 4755 |
Application of Sn-activated carbon in pressure swing adsorption for purification of H-2 Iyuke SE, Daud WRW, Mohamad AB, Kadhum AAH, Fisal Z, Shariff AM |
4757 - 4781 |
Semibatch emulsion polymerisation reactors: polybutyl acrylate case study Sajjadi S, Brooks BW |
4783 - 4787 |
Modelling of sintering of iron particles in high-temperature gas fluidisation Knight PC, Seville JPK, Kamiya H, Horio M |