Control of Single-Input-Single-Output (SISO) Processes

  • Tao LiuEmail author
  • Furong Gao
Part of the Advances in Industrial Control book series (AIC)


For control system design and engineering practice, a number of performance specifications and robust stability criteria have been developed to evaluate control system performance and stability. In industrial process control, the following widely used error criteria, time domain and frequency domain performance specifications, and robust stability criteria are introduced here for reference.


Robust Stability Disturbance Rejection Control System Design Internal Model Control Load Disturbance 
These keywords were added by machine and not by the authors. This process is experimental and the keywords may be updated as the learning algorithm improves.


  1. Åström KJ, Hägglund T (2005) Advanced PID control. ISA Society of America, Research Triangle ParkGoogle Scholar
  2. Braatz RD (1995) Internal model control: The control handbook, FL: CRC Press, Boca RatonGoogle Scholar
  3. Goodwin GC, Graebe L, Salgado ME (2001) Control system design, Prentice Hall, Upper Saddle River, NJGoogle Scholar
  4. Horn IG, Arulandu JR, Braatz RD (1996) Improved filter design in internal model control. Ind Eng Chem Res 35(10):3437–3441CrossRefGoogle Scholar
  5. Huang HP, Jeng JC, Luo KY (2005) Auto-tune system using single-run relay feedback test and model-based controller design. J Process Control 15:713–727CrossRefGoogle Scholar
  6. Hwang C, Cheng YC (2005) A note on the use of the Lambert W function in the stability analysis of time-delay systems. Automatica 41(11):1979–1985MathSciNetzbMATHCrossRefGoogle Scholar
  7. Lee Y, Park S, Lee M, Brosilow C (1998) PID controller tuning for desired closed-loop responses for SI/SO systems. AICHE J 44(1):106–115CrossRefGoogle Scholar
  8. Liu T, Gao F (2010) New insight into internal model control filter design for load disturbance rejection. IET Control Theory Appl 4(3):448–460MathSciNetCrossRefGoogle Scholar
  9. Liu T, Zhang WD, Gu DY (2005) Analytical two-degree-of-freedom tuning design for open-loop unstable processes with time delay. J Process Control 15:559–572CrossRefGoogle Scholar
  10. Morari M, Zafiriou E (1989) Robust process control. Prentice Hall, Englewood CliffGoogle Scholar
  11. Seborg DE, Edgar TF, Mellichamp DA (2004) Process dynamics and control, 2nd edn. Wiley, HobokenGoogle Scholar
  12. Shamsuzzoha M, Lee M (2007) IMC-PID controller design for improved disturbance rejection of time-delayed processes. Ind Eng Chem Res 46(7):2077–2091CrossRefGoogle Scholar
  13. Shinskey FG (1996) Process control system, 4th edn. McGraw Hill, New YorkGoogle Scholar
  14. Skogestad S (2003) Simple analytical rules for model reduction and PID controller tuning. J Process Control 13(4):291–309MathSciNetCrossRefGoogle Scholar
  15. Skogestad S, Postlethwaite I (2005) Multivariable feedback control: analysis and design, 2nd edn. Wiley, ChichesterGoogle Scholar
  16. Zhang WD, Xi YG, Yang GK, Xu XM (2002) Design PID controllers for desired time-domain or frequency-domain response. ISA Trans 41(4):511–520CrossRefGoogle Scholar
  17. Zhou KM, Doyle JC, Glover K (1996) Robust and optimal control. Prentice Hall, Englewood CliffzbMATHGoogle Scholar

Copyright information

© Springer-Verlag London Limited 2012

Authors and Affiliations

  1. 1.RWTH Aachen UniversityAachenGermany
  2. 2.Hong Kong University of Science and TechnologyKowloonHong Kong SAR

Personalised recommendations