243 - 244 |
Reuel Shinnar at 80: An appreciation Denn M, Luss D |
246 - 269 |
A systematic methodology for the design development and scale-up of complex chemical processes. The role of control and concurrent design Shinnar R |
270 - 282 |
Bounds on operating conditions leading to melting during olefin polymerization Song H, Luss D |
283 - 287 |
Dynamic interaction measures for decentralized control of multivariable processes Lee J, Edgar TF |
288 - 303 |
Bifurcation analysis of catalytic monoliths with nonuniform catalyst loading Ramanathan K, Balakotaiah V, West DH |
304 - 308 |
On the measurement of stagnancy in continuous-flow systems Nauman EB |
309 - 314 |
Optimal feed distribution in a packed-bed membrane reactor: The case of methanol oxidative dehydrogenation Diakov V, Varma A |
315 - 326 |
Emerging coherence of oscillating chemical reactions on arrays: Experiments and simulations Zhai YM, Kiss IZ, Hudson JL |
327 - 339 |
A sensitivity approach to reachability analysis for particle size distribution in semibatch emulsion polymerization Immanuel CD, Doyle FJ |
340 - 348 |
Volterra-Laguerre models for nonlinear process identification with application to a fluid catalytic cracking unit Zheng QS, Zafiriou E |
349 - 353 |
Drop size evolution during the phase separation of liquid mixtures Califano F, Mauri R |
354 - 363 |
Surface effects on the phase separation of binary polymer blends Li XF, Denn MM |
364 - 374 |
Column profile maps. 1. Derivation and interpretation Tapp M, Holland ST, Hildebrandt D, Glasser D |
375 - 383 |
Widening the applicability of reactive distillation technology by using concurrent design Citro F, Lee JW |
384 - 396 |
Dynamic disadvantages of intensification in inherently safer process design Luyben WL, Hendershot DC |
397 - 404 |
Desorption of polychlorinated biphenyls from contaminated St. Lawrence River sediments with supercritical fluids Zhou W, Anitescu G, Tavlarides LL |
405 - 421 |
Automatic control of simulated moving beds Erdem G, Abel S, Morari M, Mazzotti M, Morbidelli M, Lee JH |
422 - 427 |
Effect of pH on the foam fractionation of Mimosa pudica L. seed proteins Jeong GT, Park ES, Wahlig VL, Burapatana V, Park DH, Tanner RD |
428 - 440 |
Feasible regions for step-growth melt polycondensation systems Nisoli A, Doherty MF, Malone MF |
441 - 448 |
On aggregating populations Ramkrishna D |
449 - 457 |
Kinetic bounds on attainability in the reactor synthesis problem Abraham TK, Feinberg M |
458 - 474 |
Fault detection using canonical variate analysis Juricek BC, Seborg DE, Larimore WE |
475 - 485 |
Synthesis of a novel magnetic resin and the study of equilibrium in cation exchange with amino acids Martin C, Cuellar J |
486 - 493 |
Kinetics of bacterial As(III) oxidation and subsequent As(V) removal by sorption onto biogenic manganese oxides during groundwater treatment Katsoyiannis IA, Zouboulis AI, Jekel M |
494 - 501 |
Novel circulating fluidized-bed membrane reformer using carbon dioxide sequestration Prasad P, Elnashaie SSEH |
502 - 508 |
Influence of the heating rate and the type of catalyst on the formation of key intermediates and on the generation of gases during hydropyrolysis of glucose in supercritical water in a batch reactor Sinag A, Kruse A, Rathert J |
509 - 514 |
Effect of carbon dioxide on the interfacial tension of polymer melts Li HB, Lee LJ, Tomasko DL |
515 - 524 |
Deposition of thin polymeric films from liquid carbon dioxide using a high-pressure free-meniscus coating process Novick BJ, DeSimone JM, Carbonell RG |
525 - 534 |
Steric stabilization of silica colloids in supercritical carbon dioxide Sirard SM, Castellanos HJ, Hwang HS, Lim KT, Johnston KP |
535 - 552 |
Systematic framework for environmentally conscious chemical process design: Early and detailed design stages Chen H, Shonnard DR |
553 - 565 |
Start-up of homogeneous azeotropic distillation columns with multiple steady states Scenna NJ, Benz SJ, Franceseoni JA, Rodriguez NH |
566 - 576 |
Manufacture of thin-film solar cells: Modeling and control of Cu(InGa)Se-2 physical vapor deposition onto a moving substrate Junker ST, Birkmire RW, Doyle FJ |
577 - 588 |
Direct method for structural observability analysis Ponzoni I, Sanchez MC, Brignole NB |
589 - 596 |
Feedforward and feedback controller performance assessment of linear time-variant processes Olaleye FB, Huang B, Tamayo E |
597 - 607 |
Industrial applications of a feedback controller performance assessment of time-variant processes Olaleye F, Huang B, Tamayo E |
608 - 613 |
Cooling system design for water and wastewater minimization Kim JK, Smith R |
614 - 622 |
Extractive desulfurization and denitrogenation of fuels using ionic liquids Zhang SG, Zhang QL, Zhang ZC |
623 - 628 |
Copper(II) removal from wastewaters by a new synthesized selective extractant and SLM viability Molinari R, Poerio T, Cassano R, Picci N, Argurio P |
629 - 637 |
Agglomeration of paracetamol during crystallization in pure and mixed solvents Alander EM, Uusi-Penttila MS, Rasmuson AC |
638 - 644 |
Prediction of the natural hydrocarbon vapor phase PVT properties Yackow A, Planche H |
645 - 654 |
High-pressure binary mass diffusion coefficients for combustion applications Harstad K, Bellan J |
655 - 661 |
Design of conical spouted beds for the handling of low-density solids Olazar M, San Jose MJ, Alvarez S, Morales A, Bilbao J |
662 - 668 |
Dew points of quaternary methane plus carbon dioxide plus water plus methanol mixtures. Measurement and correlation Jarne C, Blanco ST, Fernandez J, Rauzy E, Otin S, Velasco I |