Modeling, dynamics and control of process networks with high energy throughput

Computers and Chemical Engineering

Volumn 32, Issue 9, 2008, Pages 1964-1983

  Baldea, Michael ^a   Daoutidis, Prodromos ^a  

^a University of Minnesota   (United States)

Author keywords

High purity distillation; Model reduction; Plant wide control; Reactor heat exchanger networks; Singular perturbations

Indexed keywords

ARCHITECTURAL DESIGN; COMPUTER NETWORKS; DISTILLATION; DISTILLATION COLUMNS; DYNAMICS; MECHANICS; METROPOLITAN AREA NETWORKS; MODEL STRUCTURES; NETWORK PROTOCOLS; STRUCTURAL DESIGN; VARIATIONAL TECHNIQUES;

BALANCE (WEIGHTING); CASE STUDIES; ELSEVIER (CO); ENERGY DYNAMICS; ENERGY INPUTS; GENERIC MODELLING; HIGH ENERGIES; HIGH-PURITY; MATERIAL BALANCING; MODEL BASED CONTROLLERS; PROCESS NETWORKS; REDUCED-ORDER-MODELS (REM); SHORT TIME; SINGULAR PERTURBATION (SP); SLOW DYNAMICS (SD);

PROCESS CONTROL;

EID: 45949102042     PISSN: 00981354     EISSN: None     Source Type: Journal    
DOI: 10.1016/j.compchemeng.2008.02.012     Document Type: Article

References (11)

1. Baldea M., and Daoutidis P. Model reduction and control of reactor-heat exchanger networks. Journal of Process Control 16 (2006) 265-274
2. Baldea M., Daoutidis P., and Kumar A. Dynamics and control of integrated networks with purge streams. AIChE Journal 52 (2006) 1460-1472
3. Daoutidis P., and Kravaris C. Dynamic output feedback control of minimum-phase multivariable nonlinear processes. Chemical Engineering Science 49 (1994) 433-447
4. Hangos K.M., Alonso A.A., Perkins J.D., and Ydstie B.E. Thermodynamic approach to the structural stability of process plants. AIChE Journal 45 4 (1999) 802-816
5. Kiss A.A., Bildea C.S., Dimian A.C., and Iedema P.D. State multiplicity in CSTR-separator-recycle polymerization systems. Chemical Engineering Science 57 (2002) 535-546
6. Kumar A., and Daoutidis P. Dynamics and control of process networks with recycle. Journal of Process Control 12 (2002) 475-484
7. Kumar A., and Daoutidis P. Nonlinear model reduction and control for high-purity distillation columns. Industrial & Engineering Chemistry Research 42 (2003) 4495-4505
8. Marroquin G., and Luyben W.L. Practical control studies of batch reactors using realistic mathematical models. Chemical Engineering Science 28 (1973) 993-1003
9. Morud J., and Skogestad S. Dynamic behavior of integrated plants. Journal of Process Control 6 2-3 (1996) 145-156
10. Pushpavanam S., and Kienle A. Nonlinear behavior of an ideal reactor separator network with mass recycle. Chemical Engineering Science 57 (2001) 2837-2849
11. Seider W.D., Seader J.D., and Lewin D.R. Process design principles (1999), John Wiley and Sons, Inc, New York