[1] Smith, O. J. M., Closer Control of Loops with Dead-Time, Chemical Engineering Progress, 53, p. 217, (1959).
[2] Palmor, Z., “Stability Properties of Smith Dead Time Compensator Controllers”, Int. J. Control, 32 (6),
p. 212, (1980).
[3] Hang, C. C., Lim, K. W. and Chong, B. W., A Dual - Rate Adaptive Digital Smith Predictor, Automatica, 25(1), p. 1 (1989).
[4] Watanabe, K. and Ito, M., A Process Model Control for Linear Systems with Time Delay, IEEE Trans. Automat. Contr., AC-26(6), p. 1261 (1981).
[5] Mataušek, M. R., Micić, A. D., A Modified Smith Predictor for Controlling a Process with an Integrator and Long Dead Time, IEEE Trans. Automat. Control, 44(8), p. 1196 (1996).
[6] Mataušek, M. R., Micić, A. D., On the Modified Smith Predictor for Controlling a Process with an Integrator and Long Dead Time, IEEE Trans. Automat. Contr., 41(8), p. 1603 (1999). [7] Hägglund, T., A Predictive PI Controller for Processes with Long Dead Times, IEEE Contr. Syst. Mag., 12(1), p. 57 (1992).
[8] Astrom, K., Hang, C. C. and Lim, B. C., A New Smith Predictor for Controlling A Process with an Integrator and Long Dead Time, IEEE Transactions on Automatic Control, 39(2), p. 343 (1994).
[9] Kaya, I., Atherton, D. P., A New PI - PD Smith Predictor for Control of Processes with Long Dead Time, in: 14th IFAC World Congress, Vol. C, p. 283, Beijing (1999).
[10] Kaya, I., Obtaining Controller Parameters for a New PI-PD Smith Predictor Using Auto Tuning, Journal of Process Control, 13(5), p. 465 (2003).
[11] Majhi, S., Atherton, D. P., Modified Smith Predictor and Controller for Processes with Time Delay,
IEE Proc. Control Theory Appl., 146(5), p. 359 (1999).
[12] Majhi, S.¸ Atherton, D. P., Obtaining Controller Parameters for a New Smith Predictor Using Auto Tuning, Automatica, 36(11), p. 1651 (2000).
[13] Xiang Lu,Yong Sheng Yang, Qing Guo Wang, Wei Xing Zheng, A Double Two Degree of Freedom Control Scheme for Improved Controlof Unstable Delay Processes, Journal of Process Control, 15(5), p. 605 (2005).
[14] Ramanathan, S., Curl R. L. and Kravaris, C., Dynamics and Control of Quasirational Systems, AIChE J., 35(6), p. 1017 (1989).
[15] Gundepudi, P. K., Friedly, J., Velocity Control of Hyperbolic Partial Differential Equation Systems with Single Characteristic Variable, Chem. Eng. Sci., 53(24) p. 4055 (1998).
[16] Shirvani, M., Inagaki, M. and Shimizu, T., A Simplified Model Of Distributed Parameter Systems, Int. J. Eng., 6(2), p. 65 (1993).
[17] Shirvani, M., Inagaki, M. and Shimizu, T., Simplification Study on Dynamic Models of Distributed Parameter Sytems, AIChE J., 41(12), p. 2658 (1995).
[18] Shirvani, M., Doustary, M.A., Shahbaz, M., Eksiri, Z., Heuristic Process Model Simplification in Frequency Response Domain, I.J.E. Transactions B: Applications, 17(1), p. 19 (2004).
[19] Toudou, I., Flow Forced Dynamic Behaviour of Heat Exchangers, Trans.JSME, (in Japanies) 33, p. 215 (1967).
[20] Morari, M. and Zafiriou, E., “Robust Process Control”, Englewood Cliffs, NJ: Prentice-Hall, (1989).
[21] Kaya, I., IMC Based Automatic Tuning Method for PID Controllers in a Smith Predictor Configuration., Computer and Chemical Engineering, 28(3), p. 281 (2004).