6499 - 6515 |
On predicting self-diffusion coefficients from viscosity in gases and liquids Suarez-Iglesias O, Medina I, Pizarro C, Bueno JL |
6516 - 6523 |
Equilibrium liquidus temperatures of binary mixtures from differential scanning calorimetry Kousksou T, Jamil A, Zeraouli Y, Dumas JP |
6524 - 6533 |
Macroscopic investigation of hydrate film growth at the hydrocarbon/water interface Taylor CJ, Miller KT, Koh CA, Sloan ED |
6534 - 6547 |
Characterization of potassium glycinate for carbon dioxide absorption purposes Portugal AF, Derks PWJ, Versteeg GE, Magalhaes FD, Mendes A |
6548 - 6555 |
Cationic starches as gas hydrate kinetic inhibitors Lee JD, Wu HJ, Englezos P |
6556 - 6567 |
Reduction and oxidation kinetics of Mn3O4/Mg-ZrO2 oxygen carrier particles for chemical-looping combustion Zafar Q, Abad A, Mattisson T, Gevert B, Strand M |
6568 - 6581 |
Modelling and optimization of catalytic-dielectric barrier discharge plasma reactor for methane and carbon dioxide conversion using hybrid artificial neural network - genetic algorithm technique Istadi I, Amin NAS |
6582 - 6594 |
Kinetic studies of the partial oxidation of gasoline (POXG) over a Ni-CeO2 catalyst in a fixed-bed flow reactor Ibrahim HH, Idem RO |
6595 - 6603 |
Influence of structured packing on gas holdup in a three-phase bubble column Monsalvo M, Bohm U |
6604 - 6614 |
Dynamic modeling of a batch crystallization process: A stochastic approach for agglomeration and attrition process Laloue N, Couenne F, Gorrec Y, Kohl M, Tanguy D, Tayakout-Fayolle M |
6615 - 6630 |
CFD simulation of large-scale bubble plumes: Comparisons against experiments Dhotre MT, Smith BL |
6631 - 6640 |
Drying air-induced disturbances in multi-layer coating systems Ikin JB, Thompson HM |
6641 - 6648 |
Chemotherapeutic engineering: Vitamin E TPGS-emulsified nanoparticles of biodegradable polymers realized sustainable paclitaxel chemotherapy for 168 h in vivo Feng SS, Zhao LY, Zhang ZP, Bhakta G, Win KY, Dong YC, Chien S |
6649 - 6658 |
A method to predict solubility of hydrogen in hydrocarbons and their mixtures Riazi MR, Roomi YA |
6659 - 6676 |
The effect of gas injection on the hydraulic transport of slurries in horizontal pipes Orell A |
6677 - 6686 |
Chaotic advection using passive and externally actuated particles in a serpentine channel flow Kang TG, Hulsen MA, Anderson PD, den Toonder JMJ, Meijer HEH |
6687 - 6695 |
Shape optimization of a micromixer with staggered herringbone groove Ansari MA, Kim KY |
6696 - 6708 |
Modelling and simulation of the nonlinear behaviour of paper: A cellular materials approach Ribeiro HA, Costa CAV |
6709 - 6715 |
Stability of water/toluene interfaces saturated with adsorbed naphthenic acids - A molecular dynamics study Li CL, Li ZY, Choi P |
6716 - 6725 |
Electro-ultrafiltration of amylase enzymes: Process design and economy Enevoldsen AD, Hansen EB, Jonsson G |
6726 - 6746 |
Near field characteristics of swirling flow past a sudden expansion Mak H, Balabani S |
6747 - 6753 |
Rise velocities and gas-liquid mass transfer of bubbles in organic solutions Maceiras R, Santana R, Alves SS |
6754 - 6767 |
The Y-procedure: How to extract the chemical transformation rate from reaction-diffusion data with no assumption on the kinetic model Yablonsky GS, Constales D, Shekhtmanc SO, Gleaves JT |
6768 - 6776 |
Propyne hydrogenation in a continuous polymeric catalytic membrane reactor Brandao L, Madeira LM, Mendes AM |
6777 - 6783 |
Jacobi galerkin spectral method for cylindrical and spherical geometries Fernandino M, Dorao CA, Jakobsen HA |
6784 - 6793 |
Modeling of a packed-bed electrochemical reactor for producing glyoxylic acid from oxalic acid Li J, Hu XH, Su YZ, Li QB |
6794 - 6805 |
Nano-fluidization under high gravity - A perspective view from simulation Hou CF, Ge W |
6806 - 6815 |
Estimation of rheological parameters using velocity measurements Park HM, Hong SM, Lim JY |
6816 - 6826 |
Batch extractive distillation as a hybrid process: separation of minimum boiling azeotropes Kotai B, Lang P, Modla G |
6827 - 6835 |
Sulfate decomposition from circulating fluidized bed combustors bottom ash Hoteit A, Bouquet E, Schonnenbeck C, Gilot P |
6836 - 6842 |
The importance of finite adsorption kinetics in the sorption of hydrocarbon gases onto a nutshell-derived activated carbon Wang K, Li C, San H, Do DD |
6843 - 6850 |
Transmission probabilities and particle-wall contact for Knudsen diffusion in pores of variable diameter Albo SE, Broadbelt LJ, Snurr RQ |
6851 - 6864 |
A dynamic optimization procedure for non-catalytic nitric oxide reduction in waste incineration plants Zanoelo EF, Meleiro LAC |
6865 - 6878 |
PDF method for population balance in turbulent reactive flow Rigopoulos S |
6879 - 6884 |
Interaction between two single-walled carbon nanotubes revisited: Structural stability of nanotube bundles Cao DP, Wang WC |
6885 - 6896 |
Dispersion of high-viscosity liquid-liquid systems by flow through SMX static mixer elements Rao NVR, Baird MHI, Hrymak AN, Wood PE |
6897 - 6907 |
Performance of stress-transport models in the prediction of particle-to-fluid heat transfer in packed beds Coussirat M, Guardo A, Mateos B, Egusquiza E |
6908 - 6913 |
Gravity draining of a yield-stress fluid through an orifice Toplak T, Tabuteau H, de Bruyn JR, Coussot P |
6914 - 6926 |
An analytical solution of different configurations of the linear viscoelastic normal and frictional-elastic tangential contact model Kruggel-Emden H, Wirtz S, Scherer V |
6927 - 6938 |
Numerical and experimental investigations on thermal debinding of polymeric binder of powder injection molding compact Khoong LE, Lam YC, Chai JC, Jiang L, Ma J |
6939 - 6946 |
Application of the Maxwell-Stefan approach to ion exchange in microporous materials. Batch process modelling Silva CM, Lito PF |
6947 - 6956 |
Fluidization, bubbling and jamming of nanoparticle agglomerates Valverde JM, Castellanos A |