PID Control pp 297-337 | Cite as
Process Reaction Curve and Relay Methods Identification and PID Tuning
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References
- Åström, K.J. and Hägglund, T. (1988) Automatic Tuning of PID Controllers. Instrument Society of America, Research Triangle Park, NC.Google Scholar
- Åström, K.J. and Hägglund, T. (1995) PID Controllers: Theory, Design and Tuning. Instrument Society of America, Research Triangle Park, NC.Google Scholar
- Chien, I.L. and Fruehauf, P.S. (1990) Consider IMC tuning to improve controller performance. Chemical Engineering Progress, October, 33–41.Google Scholar
- Hang, C.C., Åström, K.J. and Wang, Q.G. (2002) Relay feedback auto-tuning of process controllers — a tutorial review. J. Proc. Cont., 12, 143–162.Google Scholar
- Hang, C.C., Åström, K.J. and Ho, W.K. (1991) Refinement of the Ziegler-Nichols tuning formula. IEE Proceedings-D, 138, 111–118.Google Scholar
- Hang, C.C., Lee, T.H. and Ho, W.K. (1993) Adaptive Control. Instrument Society of America, Research Triangle Park, NC.Google Scholar
- Harriott, P. (1964) Process Control. McGraw-Hill, New York.Google Scholar
- Huang, C.T. and Chou, C.J. (1994) Estimation of the underdamped second-order parameters from the system transient. Ind. Eng. Chem. Res., 33, 174–176.Google Scholar
- Huang, C.T. and Huang, M.F. (1993) Estimating of the second-order parameters from process transient by simple calculation. Ind. Eng. Chem. Res., 32, 228–230.Google Scholar
- Huang, C.T. and Clements Jr, W.C. (1982) Parameter estimation for the second-order-plus-dead-time model. Ind. Eng. Chem. Process Des. Dev., 21, 601–603.CrossRefGoogle Scholar
- Huang, H.P. and Jeng, J.C. (2002) Monitoring and assessment of control performance for single loop systems. Ind. Eng. Chem. Res., 41, 1297–1309.Google Scholar
- Huang, H.P. and Jeng, J.C. (2003) Identification for monitoring and autotuning of PID controllers. J. Chem. Eng. Japan, 36, 284–296.Google Scholar
- Huang, H.P., Lee, M.W. and Chen, C.L. (2001) A systemof procedures for identification of simple models using transient step response. Ind. Eng. Chem. Res., 40, 1903–1915.Google Scholar
- Huang, H.P., Lee, M.W. and Chien, I.L. (2000) Identification of transfer-function models from the relay feedback tests. Chem. Eng. Commun., 180, 231–253.Google Scholar
- Li, W., Eskinat, E. and Luyben, W.L. (1991) An improved autotune identification method. Ind. Eng. Chem. Res., 30, 1530–1541.Google Scholar
- Luyben, W.L. (2001) Getting more information from relay-feedback tests. Ind. Eng. Chem. Res., 40, 4391–4402.Google Scholar
- McMillan, G.K. (1994) Tuning and Control Loop Performance, A Practitioner Guide, 3rd edn. Instrument Society of America, Research Triangle Park, NC.Google Scholar
- Oldenbourg, R.C. and Sartorius, H. (1948) The dynamics of automatic control. Trans. ASME, 77, 75–79.Google Scholar
- Shinskey, F. (1990) How good are our controllers in absolute performance and robustness? Measurement and. Control, 23, 114–121.Google Scholar
- Sundareesan, K.R., Chandra Prasad, C. and Krishnaswamy, C. (1978) Evaluating parameters for process transients. Ind. Eng. Chem. Process Des. Dev., 17, 237–241.Google Scholar
- Sung, S.W., Jungmin, O., Lee, I.B., Lee, J. and Yi, S.H. (1996) Automatic tuning of PID controller using second-order plus time delay model. J. Chem. Eng. Japan, 6, 990–999.Google Scholar
- Wang, Q.G., Guo, X. and Zhang, Y. (2001) Direct identification of continuous time delay systems from step response. J. Proc. Contr., 11, 531–542.Google Scholar
- Yu, C.C. (1999) Autotuning of PID Controllers. Springer-Verlag, London.Google Scholar
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