5649 - 5662 |
Methanol as a direct fuel in intermediate temperature (500-600 degrees C) solid oxide fuel cells with copper based anodes Brett DJL, Atkinson A, Cumming D, Ramirez-Cabrera E, Rudkin R, Brandon NP |
5663 - 5681 |
A generalized framework for solving dynamic optimization problems using the artificial chemical process paradigm: Applications to particulate processes and discrete dynamic systems Irizarry R |
5682 - 5695 |
Support effects in hydrogenation of cinnamaldehyde over carbon nanofiber-supported platinum catalysts: Kinetic modeling Toebes ML, Nijhuis TA, Hajek J, Bitter JH, van Dillen AJ, Murzin DY, de Jong KP |
5696 - 5704 |
A general correlation for pressure drop in a Kenics static mixer Song HS, Han SP |
5705 - 5717 |
The influence of natural convection on the temporal development of the temperature and concentration fields for Sal'nikov's reaction, P -> A -> B, occurring batchwise in the gas phase in a closed vessel Campbell AN, Cardoso SSS, Hayhurst AN |
5718 - 5728 |
Effect of flow configuration on the operation of coupled combustor/reformer microdevices for hydrogen production Deshmukh SR, Vlachos DG |
5729 - 5737 |
Measurement of residence time distribution in microfluidic systems Trachsel F, Gunther A, Khan S, Jensen KF |
5738 - 5750 |
Modeling the mixing of a gas-liquid spray jet injected in a gas-solid fluidized bed: The effect of the draft tube Ariyapadi S, McMillan J, Zhou D, Berruti F, Briens C, Chan E |
5751 - 5758 |
Experimental determination of methane hydrate dissociation curve up to 55 MPa by using a small amount of surfactant as hydrate promoter Gayet P, Dicharry C, Marion G, Graciaa A, Lachaise J, Nesterov A |
5759 - 5769 |
Photocatalytic reduction of selenium ions using different TiO2 photocatalysts Nguyen VNH, Amal R, Beydoun D |
5770 - 5780 |
Refolding of proteins in a CSTR Schlegl R, Tscheliessnig A, Necina R, Wandl R, Jungbauer A |
5781 - 5791 |
Global and local mixing determinations for steel converter analysis Martin M, Rendueles M, Diaz M |
5792 - 5802 |
Optimization of the active component distribution through the catalyst bed for the case of adiabatic reactor Khanaev VM, Borisova ES, Noskov AS |
5803 - 5808 |
Inward release polymer matrix covered by a permeable membrane: a possible zero-order controlled release device Liu BT, Hsu JP |
5809 - 5818 |
Validation of the Danckwerts-plot technique by simultaneous chemical absorption of CO2 and physical desorption of O-2 Cents AHG, de Bruijn FT, Brilman DWF, Versteeg GF |
5819 - 5829 |
Reaction mechanism of a single calcium hydroxide particle with humidified HCl Koch M, Zhang XH, Deng J, Kavouras A, Krammer G, Xu JC, Ge LM |
5830 - 5835 |
CO2 absorption in carbonate/bicarbonate solutions: The Danckwerts-criterion revisited Cents AHG, Brilman DWF, Versteeg GF |
5836 - 5844 |
Model for the determination of diffusion coefficients of heterovalent ions in macroporous ion exchange resins by the zero-length column method Valverde JL, De Lucas A, Carmona M, Gonzalez M, Rodriguez JF |
5845 - 5851 |
Cyclic total reflux batch distillation with two reflux drums Bai P, Hua C, Li XG, Yu KT |
5852 - 5861 |
Direct (one-step) synthesis of TiO2 and Pt/TiO2 nanoparticles for photocatalytic mineralisation of sucrose Teoh WY, Madler L, Beydoun D, Pratsinis SE, Amal R |
5862 - 5877 |
Computer modelling and numerical analysis of hydrodynamics and heat transfer in non-porous catalytic reactor for the decomposition of ammonia Waghode AN, Hanspal NS, Shigidi IMTA, Nassehi V, Hellgardt K |
5878 - 5878 |
Deep desulfurization of diesel oil: kinetic studies and process-improvement by the use of a two-phase reactor with pre-saturator (vol 59, pg 2821, 2004) Schmitz C, Datsevich LB, Jess A |