Shen Jingzhu(沈静珠).Process System Optimization(过程系统优化)[M].Beijing:China Machine Press, 1990
[2]
Kuhlmann A, Bogle I.Controllability evaluation for nonminimum phase-processes with multiplicity[J].AIChE J., 2001,47(11):2627-2631
[3]
Figueroa J L, Bahri P A, Bandoni J A, Romagnoli J A.Economic impact of disturbance and uncertain parameters in chemical processes—a dynamic back-off analysis[J].Computers and Chemical Engineering, 1996,20(4):453-461
[4]
Soliman M, Swartz C, Baker R.A mixed-integer formulation for back-off under constrained predictive control[J].Computers and Chemical Engineering, 2008,32(10):2409-2419
[5]
Li Zhihong(李志红), Hua Ben(华贲).Flexible synthesis of heat exchanger networks for multi-period operation[J].Journal of Chemical Engineering of Chinese Universities(高校化学工程学报), 1999,13(3):252-258
[6]
Xu Qiang(徐强), Chen Bingzhen(陈丙珍), He Xiaorong(何小荣).Flexible synthesis in chemical processing systems[J].Journal of Tsinghua University(清华大学学报), 2001,41(6):44-47
[7]
Karafyllis I, Kokossis A.On a new measure for the integration of process design and control:the disturbance resiliency index[J].Chemical Engineering Science, 2002,57(5):873-886
[8]
Ulasa S, Diwekar U M.Integrating product and process design with optimal control:a case study of solvent recycling[J].Chemical Engineering Science, 2006,61(6):2001-2009
[9]
Miranda M, Reneaume J M, Meyer X,et al.Integrating process design and control:an application of optimal control to chemical processes[J].Chemical Engineering and Processing, 2008,47(11):2004-2018
[10]
Sakizlis V, Perkins J D, Pistikopoulos E N.Parametric controllers in simultaneous process and control design optimization[J].Industrial & Engineering Chemistry Research, 2003,42(20):4545-4563 target="_blank">
[11]
Chawankul N, Budman1 H, Douglas P L.The integration of design and control:IMC control and robustness[J].Computers and Chemical Engineering, 2005,29(2):261-271
[12]
Ricardez-Sandoval L A, Budman H M, Douglas P L.Simultaneous design and control of processes under uncertainty:a robust modelling approach[J].Journal of Process Control, 2008,18(7/8):735-752
[13]
Lu X J, Li H, Yuan X.PSO-based intelligent integration of design and control for one kind of curing process[J].Journal of Process Control, 2010,20(10):1116-1125
[14]
Ricardez-Sandoval L A, Douglas P L, Budman H M.A methodology for the simultaneous design and control of large-scale systems under process parameter uncertainty[J].Computers and Chemical Engineering, 2011,35(2):307-318
[15]
Pajula E, Ritala R.Measurement uncertainty in integrated control and process design:a case study[J].Chemical Engineering and Processing, 2006,45(4):312-322
[16]
Bansal V, Perkins J D, Pistikopoulos E N.A case study in simultaneous design and control using rigorous, mixed-integer dynamic optimization models[J].Industrial & Engineering Chemistry Research, 2002,41(4):760-778 target="_blank">
[17]
Sakizlis V, Perkins J D, Pistikopoulos E N.Recent advances in optimization based simultaneous process and control design[J].Computers and Chemical Engineering, 2004,28(10):2069-2086
[18]
Asteasuain M, Brandolin A, Sarmoria C,et al. Simultaneous design and control of a semibatch styrene polymerization reactor[J].Industrial & Engineering Chemistry Research, 2004,43(17):5233-5247 target="_blank">
[19]
Asteasuain M, Sarmoria C, Brandolin A,et al.Integration of control aspects and uncertainty in the process design of polymerization reactors[J].Chemical Engineering Journal, 2007,131(1/2/3):135-144
[20]
Flores-Tlacuahuac A, Biegler L T.Integrated control and process design during optimal polymer grade transition operations[J].Computers and Chemical Engineering, 2008,32(11):2823-2837
[21]
Grosch R, Monnigmann M, Marquardt W.Integrated design and control for robust performance:application to an MSMPR crystallizer[J].Journal of Process Control, 2008,18(2):173-188
[22]
Altimari P, Bildea C S.Integrated design and control of plantwide systems coupling exothermic and endothermic reactions[J].Computers and Chemical Engineering, 2009,33(4):911-923
[23]
Xu Feng(许锋), Luo Xionglin(罗雄麟).Analysis of air rate margin in FCCU regenerator based on dynamic model[J].Journal of Chemical Industry and Engineering(China)(化工学报), 2008,59(1):126-134
[24]
Xu Feng(许锋), Luo Xionglin(罗雄麟).Manipulation margin and control performance analysis of chemical process under advanced process control[J].CIESC Journal(化工学报), 2012,63(3):881-886
[25]
Xu Feng(许锋), Luo Xionglin(罗雄麟).Margin analysis and control design of FCCU regenerator based on dynamic optimization(Ⅰ):Mathematical description of dynamic optimization[J].CIESC Journal(化工学报), 2009,60(3):675-682
[26]
Xu Feng(许锋), Luo Xionglin(罗雄麟).Margin analysis and control design of FCCU regenerator based on dynamic optimization(Ⅱ):Solution and result analysis[J].CIESC Journal(化工学报), 2009,60(3):683-690
