| 2551 - 2554 |
The influence of phase behavior on reactions at supercritical conditions: The hydrogenation of alpha-pinene
Chouchi D, Gourgouillon D, Courel M, Vital J, da Ponte MN |
| 2555 - 2562 |
Microfabricated multiphase packed-bed reactors: Characterization of mass transfer and reactions
Losey MW, Schmidt MA, Jensen KF |
| 2563 - 2572 |
Simulation of hydrolytic polymerization of nylon-6 in industrial reactors: Part I. Mono-acid-stabilized systems in VK tube reactors
Agrawal AK, Devika K, Manabe T |
| 2573 - 2579 |
Aggregation and peptization behavior of zeolite crystals in sols and suspensions
Maurer T, Muller SP, Kraushaar-Czarnetzki B |
| 2580 - 2585 |
Effect of the particle size of starting materials on the synthesis of crystallin layered sodium silicate for use in detergents
de Lucas A, Rodriguez L, Lobato J, Sanchez P |
| 2586 - 2596 |
Codeposition of SiC and C from mixtures of methyltrichlorosilane and ethylene in hydrogen
Kostjuhin IM, Sotirchos SV |
| 2597 - 2605 |
Model of the wet limestone flue gas desulfurization process for cost optimization
Warych J, Szymanowski M |
| 2606 - 2617 |
Temperature gradient operation of a simulated moving bed unit
Migliorini C, Wendlinger M, Mazzotti M, Morbidelli M |
| 2618 - 2627 |
Use of simulation to optimize NOx abatement by absorption and selective catalytic reduction
Sweeney AJ, Liu YA |
| 2628 - 2639 |
Inferential control of high-purity multicomponent batch distillation columns using an extended Kalman filter
Oisiovici RM, Cruz SL |
| 2640 - 2653 |
A simultaneous optimization strategy for overall integration in refinery planning
Zhang J, Zhu XX, Towler GP |
| 2654 - 2659 |
Tuning smith predictors using simple formulas derived from optimal responses
Kaya I |
| 2660 - 2667 |
PID-based sliding mode controller for nonlinear processes
Li MZ, Wang FL, Gao FR |
| 2668 - 2678 |
Poly(amino acid)-functionalized cellulosic membranes: Metal sorption mechanisms and results
Hestekin JA, Bachas LG, Bhattacharyya D |
| 2679 - 2684 |
Membrane crystallizers
Curcio E, Criscuoli A, Drioli E |
| 2685 - 2692 |
Selective removal of methanol from humid air streams using a water-vapor-purged membrane separator
Klug A, Pfromm PH, Rezac ME, Czermak P |
| 2693 - 2701 |
The kinetics and thermodynamics of sorption of chromium(VI) onto the iron(III) complex of a carboxylated polyacrylamide-grafted sawdust
Unnithan MR, Anirudhan TS |
| 2702 - 2713 |
The effects of a readily adsorbed trace component (water) in a bulk separation PSA process: The case of oxygen VSA
Wilson SJ, Beh CCK, Webley PA, Todd RS |
| 2714 - 2728 |
Feasibility of a reactive distillation column with ternary mixtures
Lee JW, Hauan S, Westerberg AW |
| 2729 - 2741 |
Entrainer selection rules for the separation of azeotropic and close-boiling-temperature mixtures by homogeneous batch distillation process
Rodriguez-Donis I, Gerbaud V, Joulia X |
| 2742 - 2747 |
Classification of homogeneous binary azeotropes
Shulgin I, Fischer K, Noll O, Gmehling J |
| 2748 - 2756 |
Prediction of asphaltene precipitation for Kuwaiti crude using thermodynamic micellization model
Fahim MA, Al-Sahhaf TA, Elkilani AS |
| 2757 - 2766 |
A fuzzy ARTMAP-based quantitative structure-property relationship (QSPR) for predicting physical properties of organic compounds
Espinosa G, Yaffe D, Arenas A, Cohen Y, Giralt F |
