2SKOGESTAD S.Dynamics and control of distillation columns—a critical survey[J].Model Ident Control,1997,18(3):177-217.
3SKOGESTAD S.Dynamics and control of distillation columns:a tutorial introduction[J].Chem Eng Res Des,1997,75(6):538-562.
4LUYBEN W L.Design and control of a fully heat-integrated pressure-swing azeotropic distillation system[J].Ind Eng Chem Res,2008,47(8):2681-2695.
5YU Baoru,WANG Qiaoyi,XU Chunjian.Design and control of distillation system for methylal/methanol separation.Part 2:pressure swing distillation with full heat integration[J].Ind Eng Chem Res,2012,51(3):1293-1310.
6SEADA J D,HENLEY E J.Separation process principles[M].Hoboken,NJ:John Wiley&Sons Inc,1998:612.
7LUYBEN W L.Distillation design and control using aspenTMsimulation[M].New York:John Wiley&Sons Inc,2006.
8LUYBEN W L.Evaluation of criteria for selecting temperature control trays in distillation columns[J].Process Control,2006,16(2):115-134.
9YU C C,LUYBEN W L.Use of multiple temperatures for the control of multicomponent distillation columns[J].Ind Eng Chem Process Des Dev,1984,23(3):590-597.
10XIA Ming,XIN Yanping,LUO Junwen,et al.Temperature control for extractive dividing-wall column with an adjustable vapor split:methylal/methanol azeotrope separation[J].Ind Eng Chem Res,2013,52(50):17996-18013.