Design of Peptide Analogues with Improved Activity Using a Novel de Novo Protein Design Approach
C. A. Floudas, J. L. Klepeis
págs. 3817-3826
A Conceptual Framework for the Process System Synthesis and Design Congruent with Corporate Strategy
T. Umeda
págs. 3827-3837
Quaternary Distillation Systems with Less than N - 1 Columns
P. C. Wankat, J. K. Kim
págs. 3838-3846
An Evaluation of MIMO Input Designs for Process Identification
D. E. Seborg, J. S. Conner
págs. 3847-3854
Steady-State Rate-Based Simulation of Packed Reactive Distillation: Spatial Discretization
S. Lextrait, R. B. Eldridge
págs. 3855-3869
Real-Options-Based Planning Strategies under Uncertainty
C. D. Maranas, A. Gupta
págs. 3870-3878
Methanol-Based Industrial Cluster Design: A Study of Design Options and the Design Process
R. M. Stikkelman, P. M. Herder
págs. 3879-3885
págs. 3886-3894
Automatic Control of Simulated Moving Beds II: Nonlinear Isotherm
G. Erdem, M. Mazzotti, M. Morbidelli, M. Morari, S. Abel
págs. 3895-3907
págs. 3908-3923
On a New MILP Model for the Planning of Heat-Exchanger Network Cleaning
J. H. Lavaja, M. J. Bagajewicz
págs. 3924-3938
págs. 3939-3947
Material and Energy Flow in a Metal Evaporation System with Moving Boundaries
M. A. McClelland, K. W. Westerberg
págs. 3948-3956
Importance of Process Chemistry in Selecting the Operating Policy for Plants with Recycle
J. D. Ward, D. A. Mellichamp
págs. 3957-3971
Static and Dynamic Behavior of Autocatalytic Replicators in Reactor Networks
F. Teymour, E. Tatara, I. Birol
págs. 3972-3993
págs. 3994-3999
Simplified Design of Batch Reactive Distillation Columns
M. E. Huerta-Garrido
págs. 4000-4011
Bayesian Estimation via Sequential Monte Carlo Sampling: Unconstrained Nonlinear Dynamic Systems
W.-s. Chen, B. R. Bakshi
págs. 4012-4023
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