717 - 730 |
Optimising the quality of safe food: Computational modelling of a continuous sterilisation process Jung A, Fryer PJ |
731 - 739 |
Measurement and modeling of particle-liquid heat transfer in liquid-solid and gas-liquid-solid fluidized beds Briens CL, Del Pozo M, Trudell C, Wild G |
741 - 764 |
On the concept and application of 'partial coherence' in non-linear wave propagation Hankins NP, Helfferich FG |
765 - 773 |
Analysis of a catalytic annular reactor for very short contact times Beretta A, Baiardi P, Prina D, Forzatti P |
775 - 783 |
On convection driven by surface tension caused by transient heat conduction Tan KK, Thorpe RB |
785 - 802 |
Modelling of the hydrodynamics of the cocurrent gas-liquid trickle flow through a trickle-bed reactor Attou A, Boyer C, Ferschneider G |
803 - 806 |
The effect of bulk concentration gradient on fluid-solid reaction rate Perez-Tello R, Sohn HY, Rajamani RK |
807 - 818 |
Numerical simulation of non-isothermal gas-liquid absorption with chemical reaction on a spherical laminar film -Application to phosgene absorption into aqueous sodium hydroxide solutions Taghizadeh M, Jallut C, Tayakout-Fayolle M, Lieto J |
819 - 828 |
Steady recirculating flow near static contact lines Gaskell PH, Thompson HM, Savage MD, Ikin JB |
829 - 839 |
A new correlation for the wall-to-fluid mass transfer in liquid-solid fluidized beds Schmidt S, Buchs J, Born C, Biselli P |
841 - 850 |
Correlation of polymer particle size with droplet size in suspension polymerisation of methylmethacrylate in a batch oscillatory-baffled reactor Ni X, Zhang Y, Mustafa I |