3627 - 3639 |
Chemical engineering and the postmodern world Prausnitz JM |
3641 - 3658 |
Cooling water system design Kim JK, Smith R |
3659 - 3669 |
Using molecular weight distributions to determine the kinetics of peroxide-induced degradation of polypropylene Iedema PD, Willems C, van Vliet G, Bunge W, Mutsers SMP, Hoefsloot HCJ |
3671 - 3681 |
An analytical model of the dynamic lift experienced by a bubble moving off-angle to an inviscid flow field with vorticity Schrage DS, Feke DL, Kamotani Y |
3683 - 3697 |
A generalised dynamic model for char particle gasification with structure evolution and peripheral fragmentation Wang FY, Bhatia SK |
3699 - 3717 |
Sound speed and attenuation in dense, non-cohesive air-granular systems Weir GJ |
3719 - 3726 |
Dynamic bifurcations and features of a cooled countercurrent flow reactor Garg R, Luss D |
3727 - 3735 |
Application of Petrov-Galerkin methods to transient boundary value problems in chemical engineering: adsorption with steep gradients in bidisperse solids Liu F, Bhatia SK |
3737 - 3750 |
Scaling relationships for rotating drums Ding YL, Forster RN, Seville JPK, Parker DJ |
3751 - 3770 |
Numerical simulations of the dependency of flow pattern on impeller clearance in stirred vessels Montante G, Lee KC, Brucato A, Yianneskis M |
3771 - 3779 |
Calculation of sedimentation equilibrium using a modified flash algorithm Castier M, Esposito RO, Tavares FW, Pecanha RP |
3781 - 3796 |
A novel FTIR method for studying mixed gas adsorption at low concentrations: H2O and CO2 on NaX zeolite and gamma-alumina Rege SU, Yang RT |
3797 - 3802 |
Micromixing efficiency in static mixer Fang JZ, Lee DJ |
3803 - 3813 |
On viscous momentum transfer by solids in gas-solids flow through risers Bussing W, Reh L |
3815 - 3827 |
Triphase catalysis: a correlation for Sherwood number using the rotating disk contactor (RDC) developed earlier Glatzer HJ, Doraiswamy LK |
3829 - 3843 |
Prediction of flammability limits at reduced pressures Arnaldos J, Casal J, Planas-Cuchi E |
3845 - 3853 |
Vibrational flow of non-Newtonian fluids Deshpande NS, Barigou M |
3855 - 3878 |
Impinging round jet studies in a cylindrical enclosure with and without a porous layer: Part I - Flow visualisations and simulations Prakesh M, Turan OF, Li YG, Mahoney J, Thorpe GR |
3879 - 3892 |
Impinging round jet studies in a cylindrical enclosure with and without a porous layer: Part II - LDV measurements and simulations Prakash M, Turan OF, Li YG, Mahoney J, Thorpe GR |
3893 - 3897 |
Novel sub-micron highly multi-layered polymer films formed by continuous flow chaotic mixing Zumbrunnen DA, Inamdar S |
3899 - 3901 |
Mass transfer coefficient in vacuum fluidized bed drying Kozanoglu BU, Vilchez JA, Casal J, Arnaldos J |
3903 - 3906 |
An analytical solution of mass diffusion in a long cylindrical microporous adsorbent with fluid film heat and mass transfer resistances San JY, Ni CC, Hong F |
3907 - 3913 |
Internally staged permeator for gas/vapour separation: effect of pressure drop in annuli of annular hollow fibres Lim SP, Li K |
3915 - 3922 |
Application of reductive perturbation method to branching of stationary solutions Inamdar SR, Karimi IA |
3923 - 3925 |
Comments on the modeling of a fore void volume in a TAP reactor Wang DZ |
3927 - 3927 |
Formal reply to letter to the editor 'Comments on the modeling of a fore void volume in a TAP reactor' Nijhuis TA, Kapteijn F, Moulijn JA |