Temperature inferential control of a reactive distillation column with double reactive sections

doi:10.1016/j.cjche.2018.11.023

中国化学工程学报 ›› 2019, Vol. 27 ›› Issue (4): 896-904.DOI: 10.1016/j.cjche.2018.11.023

• Process Systems Engineering and Process Safety • 上一篇下一篇

Temperature inferential control of a reactive distillation column with double reactive sections

Lijing Zang, Kejin Huang, Ting Guo, Yang Yuan, Haisheng Chen, Liang Zhang, Xing Qian, Shaofeng Wang

College of Information Science and Technology, Beijing University of Chemical Technology, Beijing 100029, China

收稿日期:2018-09-18 修回日期:2018-11-18 出版日期:2019-04-28 发布日期:2019-06-14
通讯作者: Kejin Huang
基金资助:
Supported by the National Natural Science Foundation of China (21376018, 21576014, 21676011, 21808007, and 21878011), the Fundamental Research Funds for the Central Universities (ZY1837) and China Postdoctoral Science Foundation (2017M620587).

Temperature inferential control of a reactive distillation column with double reactive sections

Lijing Zang, Kejin Huang, Ting Guo, Yang Yuan, Haisheng Chen, Liang Zhang, Xing Qian, Shaofeng Wang

College of Information Science and Technology, Beijing University of Chemical Technology, Beijing 100029, China

Received:2018-09-18 Revised:2018-11-18 Online:2019-04-28 Published:2019-06-14
Contact: Kejin Huang
Supported by:
Supported by the National Natural Science Foundation of China (21376018, 21576014, 21676011, 21808007, and 21878011), the Fundamental Research Funds for the Central Universities (ZY1837) and China Postdoctoral Science Foundation (2017M620587).

摘要/Abstract

摘要： Temperature inferential control (TIC) is studied for a reactive distillation column with double reactive sections (RDC-DRSs) processing a hypothetical two-stage consecutive reversible reaction (A + B ⇌ C + D, C + B ⇌ E + D with α_D > α_B > α_C > α_A > α_E). Because of the complicated dynamic behaviors, the controlled stages by sensitivity analysis lead to great steady-state deviations (SSDs) in top and bottom product purities. Since TIC involves considerably reduced settling times in comparison with direct composition control, small SSDs in product qualities correspond generally to small transient deviations (TDs) in product qualities. An objective function that measures SSDs in product qualities is formulated to represent the performance of a TIC system and an iterative procedure is devised to search for the best control configuration. The application of the procedure to the RDC-DRS gives considerably suppressed TDs and SSDs in top and bottom product qualities as compared with the one by sensitivity analysis. The method is simpler in principle and less computationally intensive than the current practice. These striking outcomes show the effectiveness of the proposed principle for the development of TIC systems for complicated reactive distillation columns.

关键词: Reactive distillation column, Temperature inferential control, Sensitivity analysis, Transient deviation, Steady-state deviation

Abstract: Temperature inferential control (TIC) is studied for a reactive distillation column with double reactive sections (RDC-DRSs) processing a hypothetical two-stage consecutive reversible reaction (A + B ⇌ C + D, C + B ⇌ E + D with α_D > α_B > α_C > α_A > α_E). Because of the complicated dynamic behaviors, the controlled stages by sensitivity analysis lead to great steady-state deviations (SSDs) in top and bottom product purities. Since TIC involves considerably reduced settling times in comparison with direct composition control, small SSDs in product qualities correspond generally to small transient deviations (TDs) in product qualities. An objective function that measures SSDs in product qualities is formulated to represent the performance of a TIC system and an iterative procedure is devised to search for the best control configuration. The application of the procedure to the RDC-DRS gives considerably suppressed TDs and SSDs in top and bottom product qualities as compared with the one by sensitivity analysis. The method is simpler in principle and less computationally intensive than the current practice. These striking outcomes show the effectiveness of the proposed principle for the development of TIC systems for complicated reactive distillation columns.

Key words: Reactive distillation column, Temperature inferential control, Sensitivity analysis, Transient deviation, Steady-state deviation

Lijing Zang, Kejin Huang, Ting Guo, Yang Yuan, Haisheng Chen, Liang Zhang, Xing Qian, Shaofeng Wang. Temperature inferential control of a reactive distillation column with double reactive sections[J]. 中国化学工程学报, 2019, 27(4): 896-904.

参考文献

[1] G. Sephanopoulos, Chemical Process Control:An Introduction to Theory and Practice, Frentice-Hall, Inc., Englewood Cliffs, NJ, 1984.
[2] P.B. Deshpande, Multivariable Process Control, Instrument Society of America, Research Triangle Park, NC, 1989.
[3] W.L. Luyben, C.C. Yu, Reactive Distillation Design and Control, John Wiley & Sons, Inc., Hoboken, NJ, 2008.
[4] O. Rademaker, J.E. Rijnsdorp, A. Maarleveld, Dynamics and Control of Continuous Distillation Units, Elsevier, Amsterdam, 1975.
[5] F.G. Shinskey, Distillation control, McGraw-Hill, NY, 1977.
[6] W.L. Luyben, Evaluation of criteria for selecting temperature control trays in distillation columns, J. Process Control 16(2006) 115-134.
[7] J.A. Heath, I.K. Kookos, J.D. Perkins, Process control structure selection based on economics, AICHE J. 23(2000) 1998-2016.
[8] I.K. Kookos, Real-time regulatory control structure selection based on economics, Ind. Eng. Chem. Res. 44(2005) 3993-4000.
[9] S.J. Wang, D.S.H. Wong, Controllability and energy efficiency of a high-purity divided wall column, Chem. Eng. Sci. 62(2007) 1010-1025.
[10] W.L. Luyben, Control of an azeotropic DWC with vapor recompression, Chem. Eng. Process. 109(2016) 114-124.
[11] C. Yu, X. Yao, K. Huang, L. Zhang, S. Wang, H. Chen, A reactive distillation column with double reactive sections for the separations of two-stage consecutive reversible reactions, Chem. Eng. Process. 79(2014) 56-68.
[12] D.B. Kaymak, H. Unlu, T. Ofkeli, Control of a reactive distillation column with double reactive sections for two-stage consecutive reactions, Chem. Eng. Process. 113(2016) 86-93.
[13] I.N. Oksal, D.B. Kaymak, Dynamic controllability comparison of reactive distillation columns with single and double reactive sections for two-stage consecutive reactions, Chem. Eng. Res. Des. 129(2018) 391-402.
[14] X. Zang, K. Huang, Y. Yuan, H. Chen, L. Zhang, S. Wang, K. Wang, Reactive distillation columns with multiple reactive sections:a case study on the disproportionation of trichlorosilane to silane, Ind. Eng. Chem. Res. 56(2017) 717-727.
[15] Y. Cao, K. Huang, Y. Yuan, H. Chen, L. Zhang, S. Wang, Dynamics and control of reactive distillation columns with double reactive sections:feed splitting influences, Ind. Eng. Chem. Res. 56(2017) 8029-8040.
[16] K. Huang, Y. Yuan, L. Zhang, H. Chen, X. Qian, S. Wang, Controllability evaluation for reactive distillation columns with multiple reactive sections disproportionating trichlorosilane to silane, Ind. Eng. Chem. Res. 57(2018) 1102-1108.
[17] B.D. Tyreus, Dominant variables for partial control. 1. A thermodynamic method for their applications, Ind. Eng. Chem. Res. 38(1999) 1432-1443.
[18] E.S. Hori, S. Skogestad, Selection of control structure and temperature location for two-product distillation columns, Chem. Eng. Res. Des. 85(2007) 293-306.

Temperature inferential control of a reactive distillation column with double reactive sections

Temperature inferential control of a reactive distillation column with double reactive sections

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