[1] E. Bristol, On a new measure of interaction for multivariable process control, IEEE Trans. Autom. Control 11(1) (1966) 133-134. [2] A. Niederlinski, A heuristic approach to the design of linearmultivariable interacting control systems, Automatica 7(6) (1971) 691-701. [3] P. Grosdldler, M. Morari, B.R. Holt, Closed-loop properties from steady state gain information, Ind. Eng. Chem. Fundam. 24(2) (1985) 221-235. [4] M.F. Witcher, T.J. McAvoy, Interaction control systems:steady state and dynamic measurement of interaction, ISA Trans. 16(3) (1977) 35-41. [5] J.P. Gagnepain, D.E. Seborg, Analysis of process interactions with application to multiloop control system design, Ind. Eng. Chem. Process. Des. Dev. 21(1) (1982) 5-11. [6] F.M.Meeuse, A.E.M. Huesman, Analyzing dynamic interaction of control loops in the time domain, Ind. Eng. Chem. Res. 41(18) (2002) 4585-4590. [7] T.McAvoy, Y. Arkun, R. Chen, D. Robinson, P.D. Schnelle, A newapproach to defining a dynamic relative gain, Control. Eng. Pract. 11(8) (2003) 907-914. [8] Q. Xiong, W.J. Cai, M.J. He, A practical loop pairing criterion for multivariable processes, J. Process Control 15(7) (2005) 741-747. [9] Q. Xiong, W.J. Cai, M.J. He, Decentralized control system design for multivariable processes-a novel method based on effective relative gain array, Ind. Eng. Chem. Res. 45(8) (2006) 2769-2776. [10] Q. Xiong, W.J. Cai, Effective transfer function method for decentralized control system design for multi-input multi-output processes, J. Process Control 16(8) (2006) 773-784. [11] Q. Xiong,W.J. Cai, M.J. He, Equivalent transfer function method for PI/PID controller design of MIMO processes, J. Process Control 17(8) (2007) 665-673. [12] M.J. He, W.J. Cai,W. Ni, L.H. Xie, RNGA based control system configuration for multivariable processes, J. Process Control 19(6) (2009) 1036-1042. [13] N. Monshizadeh-Naini, A. Fatehi, A.K. Sedigh, Input-output pairing using effective relative energy array, Ind. Eng. Chem. Res. 48(15) (2009) 7137-7144. [14] M. Morari, G. Stephanopoulos, Studies in the synthesis of control structures for chemical processes:part Ⅲ:optimal selection of secondary measurements within the framework of state estimation in the presence of persistent unknown disturbances, AICHE J. 26(2) (1980) 247-260. [15] S. Treiber, Multivariable control for non-square systems, Ind. Eng. Chem. Process. Des. Dev. 23(4) (1984) 854-857. [16] M. Morari, W. Grimm, M.J. Oglesby, I.D. Prosser, Design of resilient processing plants-VⅡ. Design of energy management system for unstable reactors-new insights, Chem. Eng. Sci. 40(2) (1985) 187-198. [17] J.W. Chang, C.C. Yu, The relative gain for non-square multivariable systems, Chem. Eng. Sci. 45(5) (1990) 1309-1323. [18] D.E. Reeves, Y. Arkun, Interaction measure for nonsquare decentralized control structures, AICHE J. 35(4) (1989) 603-613. [19] X.L. Luo, L.H. Ren, P.F. Cao, Y. Zhao, F. Xu, A closed-loop evaluation for regulatory control structure of multivariable system, Proceedings of the 10th World Congress on Intelligent Control and Automation, 2012. [20] M.J. He,W.J. Cai, B.F.Wu, M. He, Simple decentralized PID controller design method based on dynamic relative interaction analysis, Ind. Eng. Chem. Res. 44(22) (2005) 8334-8344. |