657 - 660 |
Thermal degradation of polystyrene by Lewis acids in solution Karmore V, Madras G |
661 - 665 |
Saccharification of cellulose using a hot-compressed water-flow reactor Sakaki T, Shibata M, Sumi T, Yasuda S |
666 - 671 |
Supported transition-metal oxide catalysts for catalytic reduction of SO2 with CO as a reducing agent Wang CH, Lin SS, Hwang WU, Weng HS |
672 - 679 |
A role of sodium hydroxide in the process of hydrogen sulfide adsorption/oxidation on caustic-impregnated activated carbons Bagreev A, Bandosz TJ |
680 - 690 |
Kinetics of the total oxidation of methane over a La0.9Ce0.1CoO3 perovskite catalyst Auer R, Thyrion FC |
691 - 696 |
Kinetics of aqueous-phase hydrogenation of lactic acid to propylene glycol Zhang ZG, Jackson JE, Miller DJ |
697 - 709 |
Kinetics, gas-liquid mass transfer, and modeling of the soybean oil hydrogenation process Fillion B, Morsi BI, Heier KR, Machado RM |
710 - 719 |
Silver-catalyzed oxidation of ethylene to ethylene oxide in a microreaction system Kestenbaum H, de Oliveira AL, Schmidt W, Schuth F, Ehrfeld W, Gebauer K, Lowe H, Richter T, Lebiedz D, Untiedt I, Zuchner H |
720 - 725 |
Phase relations and heat-induced chemical processes in sludges of hot-dip galvanization Kazinczy B, Kotai L, Sajo IE, Holly S, Lazar K, Jakab E, Gacs I, Szentmihalyi K |
726 - 731 |
Development of photocatalytic coating agents with indicator dyes Zhi JF, Wang HB, Fujishima A |
732 - 743 |
High-volume single-wafer reactors for silicon epitaxy Kommu S, Khomami B |
744 - 750 |
Experimental application of partitioned model-based control to pH neutralization Maksumov A, Mulder DJ, Harris KR, Palazoglu A |
751 - 759 |
A fast and efficient algorithm for training radial basis function neural networks based on a fuzzy partition of the input space Sarimveis H, Alexandridis A, Tsekouras G, Bafas G |
760 - 778 |
A case study in simultaneous design and control using rigorous, mixed-integer dynamic optimization models Bansal V, Perkins JD, Pistikopoulos EN |
779 - 789 |
Scheduling parallel production lines with resource constraints. 1. Model formulation Lamba N, Karimi IA |
790 - 800 |
Scheduling parallel production lines with resource constraints. 2. Decomposition algorithm Lamba N, Karimi IA |
801 - 816 |
Model predictive control of interconnected linear and nonlinear processes Zhu GY, Henson MA |
817 - 824 |
Proposal to speed up the implementation of an abnormal situation management in the chemical process industry Ruiz D, Benqlilou C, Nougues JM, Puigjaner L, Ruiz C |
825 - 841 |
Combine molecular modeling with optimization to stretch refinery operation Hu SY, Towler G, Zhu XX |
842 - 852 |
Estimation of the dynamic matrix and noise model for model predictive control using closed-loop data Kadali R, Huang B |
853 - 861 |
Kinetic modeling of simultaneous recovery of metallic cations and anions with a mixture of extractants in hollow-fiber modules Lin SH, Juang RS |
862 - 870 |
Modeling comblike polymer solutions using an equation of state: Application to vapor-liquid equilibria Peng CJ, Liu HL, Hu Y |
871 - 881 |
Mixing molar volume of liquid n- and i-alkanes based on the law of corresponding states with potential between functional groups Tada Y, Hiraoka S, Nishida N, Tanuma N, Lee YS |
882 - 884 |
Heat- and mass-transfer analogy in a bubble column Verma AK |