MPC of distillation column with side reactors for methyl acetate

doi:10.1016/j.cjche.2017.08.012

Chinese Journal of Chemical Engineering ›› 2017, Vol. 25 ›› Issue (12): 1798-1804.DOI: 10.1016/j.cjche.2017.08.012

• 第25届中国过程控制会议专栏 • 上一篇下一篇

MPC of distillation column with side reactors for methyl acetate

Cuimei Bo¹, Jun Li¹, Lei Yang¹, Hui Yi¹, Jihai Tang², Xu Qiao²

1. College of Automation and Electrical Engineering, Nanjing Tech University, Nanjing 210009, China;
2. State Key Laboratory of Materials-oriented Chemical Engineering, Nanjing Tech University, Nanjing 210009, China

收稿日期:2016-11-19 修回日期:2017-04-18 出版日期:2017-12-28 发布日期:2018-01-18
通讯作者: Jun Li,E-mail addresses:Lijun_ee@njtech.edu.cn,j262402@163.com.
基金资助:
Supported by the National Natural Science Foundation of China (61673205, 61503181, 21727818), National Key R&D Program of China (2017YFB0307304), the Natural Science Foundation of Jiangsu Province (BK20141461, BK20140953), the State Key Laboratory of Materials-Oriented Chemical Engineering Open Subject (kl16-07).

MPC of distillation column with side reactors for methyl acetate

Cuimei Bo¹, Jun Li¹, Lei Yang¹, Hui Yi¹, Jihai Tang², Xu Qiao²

1. College of Automation and Electrical Engineering, Nanjing Tech University, Nanjing 210009, China;
2. State Key Laboratory of Materials-oriented Chemical Engineering, Nanjing Tech University, Nanjing 210009, China

Received:2016-11-19 Revised:2017-04-18 Online:2017-12-28 Published:2018-01-18
Contact: Jun Li,E-mail addresses:Lijun_ee@njtech.edu.cn,j262402@163.com.
Supported by:
Supported by the National Natural Science Foundation of China (61673205, 61503181, 21727818), National Key R&D Program of China (2017YFB0307304), the Natural Science Foundation of Jiangsu Province (BK20141461, BK20140953), the State Key Laboratory of Materials-Oriented Chemical Engineering Open Subject (kl16-07).

摘要/Abstract

摘要： This paper focuses on the dynamic control of distillation columnwith side reactors (SRC) formethyl acetate production. To obtain the optimumintegrated structure and steady state simulation, the systematic design approach based on the concept of independent reaction amount is applied to the process of SRC formethyl acetate production. In addition to the basic control loops, multi-variable model predictive control modular with methyl acetate concentration and temperature of sensitive plate is designed. Then, based on process simulation software Aspen Plus, dynamic simulation of SRC for methyl acetate production is used to verify the effectiveness of the control scheme.

关键词: Distillation column with side reactors (SRC), Multi-variable model predictive control (MPC), Methyl acetate, Steady-state optimization, Dynamic simulation

Abstract: This paper focuses on the dynamic control of distillation columnwith side reactors (SRC) formethyl acetate production. To obtain the optimumintegrated structure and steady state simulation, the systematic design approach based on the concept of independent reaction amount is applied to the process of SRC formethyl acetate production. In addition to the basic control loops, multi-variable model predictive control modular with methyl acetate concentration and temperature of sensitive plate is designed. Then, based on process simulation software Aspen Plus, dynamic simulation of SRC for methyl acetate production is used to verify the effectiveness of the control scheme.

Key words: Distillation column with side reactors (SRC), Multi-variable model predictive control (MPC), Methyl acetate, Steady-state optimization, Dynamic simulation

Cuimei Bo, Jun Li, Lei Yang, Hui Yi, Jihai Tang, Xu Qiao. MPC of distillation column with side reactors for methyl acetate[J]. Chinese Journal of Chemical Engineering, 2017, 25(12): 1798-1804.

Cuimei Bo, Jun Li, Lei Yang, Hui Yi, Jihai Tang, Xu Qiao. MPC of distillation column with side reactors for methyl acetate[J]. Chin.J.Chem.Eng., 2017, 25(12): 1798-1804.

参考文献

[1] M.F. Malone, M.F. Doherty, Reactive distillation, Ind. Eng. Chem. Res. 39 (11) (2000) 3953-3957.

[2] A. Stankiewicz, Reactive separations for process intensification: an industrial perspective, Chem. Eng. Process. 42 (3) (2003) 137-144.

[3] Z.Y. Qiu, L.N. Zhao, L.Weatherley, Process intensification technologies in continuous biodiesel production, Chem. Eng. Process. 49 (4) (2010) 323-330.

[4] D.B. Kaymak,W.L. Luyben, Design of distillation columnswith external side reactors, Ind. Eng. Chem. Res. 43 (25) (2004) 8049-8056.

[5] M.A. Al-Arfaj,W.L. Luyben, Comparison of alternative control structures for an ideal two-product reactive distillation column, Ind. Eng. Chem. Res. 39 (9) (2000) 3298-3307.

[6] M.A. Al-Arfaj, W.L. Luyben, Comparative control study of ideal and methyl acetate reactive distillation, Chem. Eng. Sci. 57 (24) (2002) 5039-5050.

[7] D.B. Kaymak, W.L. Luyben, Quantitative comparison of reactive distillation with conventional multiunit reactor/column/recycle systems for different chemical equilibrium constants, Ind. Eng. Chem. Res. 43 (10) (2004) 2493-2507.

[8] D.B. Kaymak, W.L. Luyben, Comparison of two types of two-temperature control structures for reactive distillation columns, Ind. Eng. Chem. Res. 44 (13) (2005) 4625-4640.

[9] D.B. Kaymak, W.L. Luyben, Dynamic control of a column/side-reactor process, Ind. Eng. Chem. Res. 47 (22) (2008) 8704-8712.

[10] Lalitha S. Balasubramhanya, Francis J. Doyle Ⅲ, Nonlinear model-based control of a batch reactive distillation column, J. Process Control 10 (2) (2012) 209-218.

[11] Sudibyo, I.M. Iqbal, M.N. Murat, N. Aziz, Comparison of MIMO MPC and PI decoupling in controlling methyl tert-butyl ether process, Comput. Aided Chem. Eng. 31 (2012) 345-349.

[12] Neha Sharma, Kailash Singh, Model predictive control and neural network predictive control of TAME reactive distillation column, Chem. Eng. Process. Process Intensif. 59 (9) (2012) 9-21.

[13] B.O. Cuimei, The design and control of distillation column with side reactors for chlorobenzene production, Chin. J. Chem. Eng. 20 (6) (2012) 1113-1120.

[14] Z.H.O.U. Jiao, Simulation of reactive distillation process coupled with side reactors for preparation of methyl acetate, J. Nanjing Univ. Technol. Nat. Sci. Ed. 28 (5) (2006) 51-56.

[15] T. Safinski, A.A. Adesina, Development of a novel basket impeller dualflow tray catalytic distillation reactor, Ind. Eng. Chem. Res. 44 (16) (2005) 6212-6221.

[16] Bo Cuimei, Tang Jihai, Qiao Xu, Ding Lianghui, Cui Mifen, The optimization method and simulating systemof distillation column with side reactors for benzene chloride production, J. Shanghai Jiaotong Univ. 45 (8) (2011) 1157-1162.

[17] Lianghui Ding, Jihai Tang, Mifen Cui, Cuimei Bo, Xian Chen, Qiao Xu, Optimum design and analysis based on independent reaction amount for distillation column with side reactors: production of benzyl chloride, Ind. Eng. Chem. Res. 50 (19) (2011) 11143-11152.

[18] B. Friedland, Control system design: an introduction to state-space methods, Optimal Control Appl. Methods 9 (1) (2012) 107-107.

MPC of distillation column with side reactors for methyl acetate

MPC of distillation column with side reactors for methyl acetate

PDF (PC)

可视化

摘要/Abstract

引用本文

使用本文

参考文献

相关文章 15

编辑推荐

Metrics

本文评价

[1]	Jindong Dai, Chi Zhai, Jiali Ai, Guangren Yu, Haichao Lv, Wei Sun, Yongzhong Liu. A cellular automata framework for porous electrode reconstruction and reaction-diffusion simulation[J]. 中国化学工程学报, 2023, 60(8): 262-274.
[2]	Jianglong Du, Haolan Tao, Jie Yang, Cheng Lian, Sen Lin, Honglai Liu. Understanding electrokinetic thermodynamics in nanochannels[J]. 中国化学工程学报, 2021, 29(3): 33-41.
[3]	Mingyuan Hu, Hui Tian. Design of process and control scheme for cyclohexanol production from cyclohexene using reactive distillation[J]. 中国化学工程学报, 2021, 40(12): 96-105.
[4]	Zhiheng Ren, Muhammad Naeem Younis, Hui Zhao, Chunshan Li, Xiangui Yang, Erqiang Wang, Gongying Wang. Silver modified Cu/SiO₂ catalyst for the hydrogenation of methyl acetate to ethanol[J]. 中国化学工程学报, 2020, 28(6): 1612-1622.
[5]	Mohammad El Wali, Saeed Rahimpour Golroudbary, Andrzej Kraslawski. Impact of recycling improvement on the life cycle of phosphorus[J]. 中国化学工程学报, 2019, 27(5): 1219-1229.
[6]	Xiaohui Wang, Jiachen Li, Li Zhang. Understanding self-accelerated water diffusion within poly-lactic acid via molecular dynamics simulation[J]. 中国化学工程学报, 2019, 27(4): 759-764.
[7]	Zhixian Huang, Yixiong Lin, Xiaoda Wang, Changshen Ye, Ling Li. Optimization and control of a reactive distillation process for the synthesis of dimethyl carbonate[J]. , 2017, 25(8): 1079-1090.
[8]	Yunhu Gao, Zhihong Xu, Kejing Wu, Xiaolu Wang, Zhaojun Yu, Weiyang Fei. The steady-state and dynamic simulation of cascade distillation system for the production of oxygen-18 isotope from water[J]. , 2016, 24(8): 979-988.
[9]	Zhishan Zhang, Qingjun Zhang, Guijie Li, Meiling Liu, Jun Gao. Design and control of methyl acetate-methanol separation via heat-integrated pressure-swing distillation[J]. Chinese Journal of Chemical Engineering, 2016, 24(11): 1584-1599.
[10]	Lumin Li, Lanyi Sun, Delian Yang, Wang Zhong, Yi Zhu, Yuanyu Tian. Reactive dividing wall column for hydrolysis of methyl acetate: Design and control[J]. , 2016, 24(10): 1360-1368.
[11]	Lili Tao, ZhihuaHu, Feng Qian. Design and control of a p-xylene oxidation process[J]. Chinese Journal of Chemical Engineering, 2015, 23(12): 1935-1944.
[12]	黄秀辉, 钟伟民, 彭昌军, 钱锋. Isobaric Vapor-Liquid Equilibrium of Binary Systems: p-Xylene+ (Acetic Acid, Methyl Acetate and n-Propyl Acetate) and Methyl Acetate+n-Propyl Acetate in an Acetic Acid Dehydration Process[J]. Chinese Journal of Chemical Engineering, 2013, 21(2): 171-176.
[13]	周平, 向波, 柴天佑. Improved Disturbance Observer (DOB) Based Advanced Feedback Control for Optimal Operation of a Mineral Grinding Process^*[J]. Chinese Journal of Chemical Engineering, 2012, 20(6): 1206-1212.
[14]	薄翠梅, 汤吉海, 柏杨进, 乔旭, 丁良辉, 张湜. The Design and Control of Distillation Column with Side Reactors for Chlorobenzene Production^*[J]. Chinese Journal of Chemical Engineering, 2012, 20(6): 1113-1120.
[15]	李澄非. Dynamic Simulation and Analysis of Industrial Purified Terephthalic Acid Solvent Dehydration Process[J]. , 2011, 19(1): 89-96.