Abstract
In Chap. 2, we presented the DFDM framework for the design of Networked Manufacturing Systems (NMS).
Access this chapter
Tax calculation will be finalised at checkout
Purchases are for personal use only
Abbreviations
- \( t_{f}^{d} \) :
-
Desired response time
- \( t_{f} \) :
-
Response time
- \( t_{f}^{*} \) :
-
Shortest desired response time
- \( y_{sp} \) :
-
Change in the requirements
- d :
-
Change in disturbance
- u :
-
Input points of AOS
- y :
-
Output points of DOS
- \( F_{i - 1} \) :
-
Feed flow rate
- \( F_{i} \) :
-
Flow rate
- \( V_{i} \) :
-
Volume
- t:
-
Time
- \( C_{Ai} \) :
-
Concertation of A
- \( C_{Ai - 1} \) :
-
Feed concertation of A
- \( k_{i} \) :
-
Reaction rate constant
- \( \rho \) :
-
Density of A
- \( c_{p} \) :
-
Heat capacity of A
- \( T_{i} \) :
-
Reactor temperature
- \( T_{i - 1} \) :
-
Feed temperature
- \( \Delta H \) :
-
Heat of reaction
- U :
-
Overall heat-transfer coefficient
- \( T_{Ci} \) :
-
Jacket temperature
- \( T_{C0} \) :
-
Coolant feed temperature
- \( A_{i} \) :
-
Heat-transfer area
- \( \rho_{C} \) :
-
Density of coolant
- \( c_{pC} \) :
-
Heat capacity of coolant
- \( V_{Ci} \) :
-
Volume of the jacket
- \( F_{Ci} \) :
-
Coolant flow rate
- E :
-
Activation energy
- R :
-
Reference or nominal value
- \( A_{si} \) :
-
Side heat-transfer area
- \( A_{bi} \) :
-
Bottom heat-transfer area
- \( A_{si}^{R} \) :
-
Reference side heat-transfer area
- \( V_{i}^{R} \) :
-
Reference volume
- \( x_{1i} \) :
-
Normalized reactor holdup
- \( x_{2i} \) :
-
Concentration of reactor A
- \( x_{3i} \) :
-
Reactor temperature
- \( x_{4i} \) :
-
Coolant temperature
- \( x_{4i} \) :
-
Coolant temperature
- \( q_{i} \) :
-
Normalized flow rate
- \( q_{Ci} \) :
-
Normalized coolant flow rate
- \( \alpha_{i} \) :
-
Ratio of coolant flow rate and flow rate and
- \( \mu_{i} \) :
-
Ratio of flow rate and coolant flow rate
- \( \delta_{si} \) :
-
Thickness of side heat-transfer area
- \( \delta_{bi} \) :
-
Thickness of bottom heat-transfer area
- \( k_{0} \) :
-
Arrhenius constant
- \( \Delta H \) :
-
Heat of reaction
- ODF = 1:
-
Overdesign factor in the reactor volume obtain DIS
- \( T_{i} \) :
-
Strong constraint
- \( F_{Ci} \) :
-
Assumption
- \( k \) :
-
Reactor rate constant at reactor temperature
- \( Q_{\hbox{max} } /Q \) :
-
Controllability index of Luyben
- \( \Delta T \) :
-
Temperature difference between jacket and reactor
- \( \uplambda_{\text{ij}} \) :
-
The jth eigenvalue of ith reactor (i is omitted for single reactors)
- i:
-
Reactor number
References
Arkun, Y. (1988). Relative Sensitivity: A Dynamic Closed-Loop Interaction Measure and Design Tool. AIChE Journal, 34(4), 672–675.
Bahri, P. A., Bandoni, J. A., & Romagnoli, J. A. (1996). Effect of disturbances in optimizing control: Steady-state open-loop backoff problem. AIChE Journal, 42(4), 983–994.
Cao, Y., Biss, D., & Perkins, J. (1996). Assessment of input-output controllability in the presence of control constraints. Computers & Chemical Engineering, 20(4), 337–346.
Chenery, S. D. (1997). Process controllability analysis using linear and nonlinear optimization. In Ph.D. Monograph. London, UK: Imperial College of Science, Technology, and Medicine.
Dimitriadis, V. D., & Pistikopoulos, E. N. (1995). Flexibility analysis of dynamic systems. Industrial and Engineering Chemistry Research, 34(12), 4451–4462.
Fisher, W. R., Doherty, M. F., & Douglas, J. M. (1988). The interface between design and control. 1. Process controllability. Industrial and Engineering Chemistry Research, 27(4), 597–605.
Georgakis, C., Uztürk, D., Subramanian, S., & Vinson, D. R. (2003). On the operability of continuous processes. Control Engineering Practice, 11(8), 859–869.
Grosdidier, P., Morari, M., & Holt, B. R. (1985). Closed-loop properties from steady-state gain information. Industrial and Engineering Chemistry Fundamentals, 24(2), 221–235.
Grosdidier, P., & Morari, M. (1986). Analysis of interactions using structured singular values. In IEEE American Control Conference.
Grossmann, I. E., & Floudas, C. A. (1987). Active constraint strategy for flexibility analysis in chemical processes. Computers & Chemical Engineering, 11, 675–693.
Hovd, M., & Skogestad, S. (1992). Simple frequency-dependent tools for control system analysis, structure selection and design. Automatica, 28(5), 989–996.
Lewin, D. (1996). A simple tool for disturbance resiliency diagnosis and feedforward control design. Computers & Chemical Engineering, 20(1), 13–25.
Lyman, P. R., Luyben, W. L., & Tyreus, B. D. (1996). Method for assessing the effect of design parameters on controllability. Industrial and Engineering Chemistry Research, 35(10), 3484–3497.
Manousiouthakis, V., Savage, R., & Arkun, Y. (1986). Synthesis of decentralized process control structures using the concept of block relative gain. AIChE Journal, 32(6), 991–1003.
McAvoy, T. J. (1983). Interaction analysis: Principles and applications. NC: Instrument Society of America Research Triangle Park.
Milisavljevic, J. (2018). Architecting networked engineering systems. Doctoral Dissertation, The School of Aerospace and Mechanical Engineering. University of Oklahoma, Norman, Oklahoma.
Milisavljevic, J., Commuri, S., Allen, J. K., & Mistree, F. (2018). Steady-state operability in design for dynamic management in realization of networked engineering systems. In ASME Design for Manufacturing and Assembly Conference. Quebec City, Quebec, Canada. Paper Number DETC2018–85864.
Milisavljevic-Syed, J., Commuri, S., Allen, J. K., & Mistree, F. (2019b). Concurrent design exploration method for realizing networked manufacturing systems for industry 4.0. In 52nd CIRP Annual Conference, PROC-D-18-00262.
Mohideen, M. J., Perkins, J. D., & Pistikopoulos, E. N. (1996). Optimal design of dynamic systems under uncertainty. AIChE Journal, 42(8), 2251–2272.
Morari, M. (1983). Design of resilient processing plants—III: A general framework for the assessment of dynamic resilience. Chemical Engineering Science, 38(11), 1881–1891.
Moore, C. (1986). Application of singular value decomposition to the design, analysis, and control of industrial processes. In American Control Conference, IEEE.
Russo, L. P., & Bequette, B. W. (1995). Impact of process design on the multiplicity behavior of a jacketed exothermic CSTR. AIChE Journal, 41(1), 135–147.
Russo, L. P., & Bequette, B. W. (1998). Operability of chemical reactors: Multiplicity behavior of a jacketed styrene polymerization reactor. Chemical Engineering Science, 53(1), 27–45.
Stanley, G., Marino-Galarraga, M., & McAvoy, T. J. (1985). Shortcut operability analysis 1: The relative disturbance gain. Industrial Engineering Chemistry Process Design and Development, 24, 1181–1188.
Subramanian, S., & Georgakis, C. (2000). Steady-state operability characteristics of reactors. Computers & Chemical Engineering, 24(2–7), 1563–1568.
Subramanian, S., Uztürk, D., & Georgakis, C. (2001). An optimization-based approach for the operability analysis of continuously stirred tank reactors. Industrial and Engineering Chemistry Research, 40(20), 4238–4252.
Swaney, R. E., & Grossmann, I. E. (1985a). An Index for operational flexibility in chemical process design. Part I: Formulation and theory. AIChE Journal, 31(4), 621–630.
Swaney, R. E., & Grossmann, I. E. (1985b). An index for operational flexibility in chemical process design. Part II: Computational algorithms. AIChE Journal, 31(4), 631–641.
Swartz, C. (1996). A computational framework for dynamic operability assessment. Computers & Chemical Engineering, 20(4), 365–371.
Uztiirk, D., & Georgakis, C. (1998). An optimal control perspective on the inherent dynamic operability of processes. In Annual AIChE Meeting. Miami, FL. Paper 217a.
Uztürk, D., & Georgakis, C. (2001). Inherent dynamic operability of processes I: Definitions and analysis in the SISO case. Industrial and Engineering Chemistry Research, 41(3), 421–432.
Vinson, D. R., & Georgakis, C. (1998). A new measure of process output controllability. IFAC Proceedings Volumes, 31(11), 663–672.
Vinson, D. R., & Georgakis, C. (2000). A new measure of process output controllability. Journal of Process Control, 10(2–3), 185–194.
Zhu, Z. X., Lee, J., & Edgar, T. F. (1997). Steady state structural analysis and interaction characterization for multivariable control systems. Industrial and Engineering Chemistry Research, 36(9), 3718–3726.
Ziegler, J., & Nichols, N. (1943). Process lags in automatic control circuits. Trans. ASME, 65(5), 433–443.
Author information
Authors and Affiliations
Corresponding author
Glossary
- ACRONES
-
Adaptable Concurrent Realization of Networked Engineering System
- AIS
-
Achieved Input Space
- AOS
-
Achieved Output Space
- cDSP
-
Compromise Decision Support Problem
- CSTR
-
Continuous single tank reactor
- DAIS
-
Dynamic Available Input Space
- DAOS
-
Dynamic Achieved Output Space
- DDOS
-
Dynamic Desired Output Space
- DFDM
-
Design for Dynamic Management
- DIS
-
Desired Input Space
- Disturbance Space
-
Space where system can be functional in the presence of disturbance
- DOI
-
Dynamic Operability Index
- DOM
-
Dynamic Operability Model
- DOS
-
Desired Output Space
- EDS
-
Excepted Disturbance Space
- FI
-
Flexibility index
- Functional System
-
System that is operable
- MIMO
-
Multiple input multiple output
- MTCP
-
Minimum Time Control Problem
- NMS
-
Networked Manufacturing Systems
- Operability Space
-
Space where system can be functional
- Original System Design
-
New system design without existing specifications
- RGA
-
Relative Gain Array
- RHP
-
Right-half-plane
- SISO
-
Single input single output
- SSOM
-
Steady-State Operability Model
- Variant System Design
-
System design with existing specifications
Rights and permissions
Copyright information
© 2020 Springer Nature Switzerland AG
About this chapter
Cite this chapter
Milisavljevic-Syed, J., Allen, J.K., Commuri, S., Mistree, F. (2020). Dynamic Operability Analysis. In: Architecting Networked Engineered Systems . Springer, Cham. https://doi.org/10.1007/978-3-030-38610-8_5
Download citation
DOI: https://doi.org/10.1007/978-3-030-38610-8_5
Published:
Publisher Name: Springer, Cham
Print ISBN: 978-3-030-38609-2
Online ISBN: 978-3-030-38610-8
eBook Packages: EngineeringEngineering (R0)