Optimization and discrete fractional-order PID controller applied to a pressure swing adsorption plant for the production and recovery of bioethanol

被引：5

作者：

Valdez-Resendiz, Jesus E. ^{[1
]}

Rumbo-Morales, Jesse Y. ^{[2
]}

Sorcia-Vazquez, Felipe D. J. ^{[2
]}

Ortiz-Torres, Gerardo ^{[2
]}

Gomez-Aguilar, J. F. ^{[3
]}

Cantero, Carlos Alberto Torres ^{[4
,5
]}

Ramos-Martinez, Moises ^{[2
]}

机构：

[1] Tecnol Monterrey, Ave Eugenio Garza Sada 2501 Sur, Monterrey 64700, Nuevo Leon, Mexico

[2] Univ Guadalajara, Ctr Univ Los Valles, Carretera Guadalajara Ameca Km 45-5, Ameca 46600, Jalisco, Mexico

[3] CONACyT Tecnol Nacl Mexico CENIDET, Interior Internado Palmira S-N, Cuernavaca 62490, Morelos, Mexico

[4] Tecnol Nacl Mex Campus Colima, Ave Tecnol 1, Colima 28976, Mexico

[5] Univ Colima, Fac Ingn Mecan & Electr, Carretera Colima Coquimatlan Km 9, Colima 28400, Mexico

来源：

JOURNAL OF CLEANER PRODUCTION | 2024年 / 476卷

关键词：

Bioethanol; Fractional controllers; Pressure swing adsorption; Optimization; PREDICTIVE CONTROL; SEPARATION; SIMULATION; DERIVATIVES; ETHANOL; SYSTEMS; DESIGN;

D O I：

10.1016/j.jclepro.2024.143618

中图分类号：

X [环境科学、安全科学];

学科分类号：

08 ; 0830 ;

摘要：

The results obtained demonstrate significant scientific and technological contributions. The DFOPID controller achieved a purity of 99.50% wt, a recovery of 74.53%, and an energy efficiency of 69.52%, effectively handling disturbances and trajectory changes. In comparison, the discrete PID controller reached a purity of 99.42% wt, a recovery of 74.19%, and an energy efficiency of 61.10%. While the DFOPID exhibited superior performance and faster response to trajectory changes and disturbances, the discrete PID showed better energy efficiency. Both controllers are viable for industrial applications and PSA processes, as they meet the required purity standards for biofuel production.

引用

页数：20

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