Sliding mode control of vertical double wall dividing-wall columns

被引:2
|
作者
Wang, Honghai [1 ,2 ]
Zhang, He [1 ,2 ]
Wang, Zhongbiao [3 ]
Zhou, Qi [4 ]
Su, Weiyi [1 ,2 ]
Li, Chunli [1 ,2 ]
Hu, Yuqi [1 ,2 ]
机构
[1] Hebei Univ Technol, Sch Chem Engn & Technol, Tianjin 300130, Peoples R China
[2] Hebei Univ Technol, Sch Chem Engn & Technol, Natl Local Joint Engn Lab Energy Conservat Chem Pr, Tianjin 300130, Peoples R China
[3] Purificat Equipment Res Inst CSIC, Handan 056004, Peoples R China
[4] Tianjin Univ, Sch Chem Engn & Technol, Tianjin 300072, Peoples R China
基金
中国国家自然科学基金;
关键词
VDWDWC; Separation; Dynamic simulation; Sliding mode control; PREDICTIVE CONTROL; EXTRACTIVE DISTILLATION; DESIGN; OPTIMIZATION;
D O I
10.1016/j.cep.2022.109200
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Since a multi-component distillation system has more complex process nonlinearities and time delays than a traditional three-column system, sliding mode control (SMC) is often adopted for multi-component systems. In this paper, a new type of dividing-wall column, called the vertical double-wall dividing-wall column (VDWDWC), is proposed for the separation of quaternary systems. This column has the potential for both higher separation efficiencies and lower equipment costs than the traditional three-column sequence. Therefore, SMC was adopted for the multivariable VDWDWC system and the Smith hysteresis compensation is added to reduce the impact of chattering. The results revealed that the settling time, the oscillations, and steady-state errors of the SMC controller were less than those of the PID controller. Finally, optimal parameters of the SMC controller were obtained by response surface methodology. These parameters reduced the overshoot of the controller, further indicating that SMC could control the VDWDWC system better.
引用
收藏
页数:11
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