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多模型預(yù)測(cè)控制在苯乙烯聚合反應(yīng)中的應(yīng)用

作者: 時(shí)間:2011-08-08 來(lái)源:網(wǎng)絡(luò) 收藏



了基于性能指標(biāo)切換的多算法,這種方法通過(guò)在多個(gè)操作點(diǎn)附近獲取的多個(gè)線性來(lái)設(shè)計(jì)多個(gè)線性器,同時(shí)根據(jù)所提的器選擇方法來(lái)達(dá)到非線性控制。將所提基于性能指標(biāo)切換的多控制算法施加到仿真系統(tǒng)中,分別進(jìn)行了設(shè)定點(diǎn)跟蹤和有干擾兩種不同情況的仿真。結(jié)果表明,所提算法多模型非線性控制算法與普通的DMC相比具有更加良好的穩(wěn)定性和收斂性,并能做到無(wú)偏跟蹤。
參考文獻(xiàn)
[1] QIN S J, BADGWELL T A. An overview of nonlinear model predictive control applications. In: Algower F, Zheng A, eds. Proceedings of Nonlinear model predictive control workshop—assessment and future directions.Ascona, Switzerland, 1998.
[2] QIN S J, BADGWELL T A. A survey of industrial model predictive control technology[J]. Control Engineering Practice,2003,11(7):733-764.
[3] JOHANSEN T S. Operating regime based process modeling and identification[D]. Norway: University of Trondheim, 1994.
[4] Zhou Chaojun, Jiang Weisun. Two methods of multiple models control for nonlinear process[J]. Signal and Control (China), 1994,23(6):356-330.
[5] BALAKRISHNAN J. Control system design using multiple models, switching, and tuning [D].American: Yale University, 1996.
[6] PISHVAIE M R, SHAHROKHI M. pH control using the nonlinear multiple models, switching, and tunning approach [J]. Ind. Eng. Chem. Res., 2000,39(5):1311-1319.
[7] GALAN O, ROMAGNOLI J A, PALAZOGLU A. Real-time implementation of multi-linear model-based control strategies—an application to a bench-scale pH neutralization reactor[J]. Journal of Process Control,2004,14(5):571-579.
[8] AUFDERHEIDE B, BEQUETTE B W. Extension of dynamic matrix control to multiple models[J]. Computers and Chemical Engineering, 2003,27(8-9):1079-1096.
[9] PORFIRIO C R, NETO E A, ODLOAK D, Multi-model predictive control of an industrial C3/C4 Splitter[J]. Control Engineering Practice, 2003,11(7):765-779.

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