Proceedings of ESCAPE 35ISSN: 2818-4734
Volume: 4 (2025)
Table of Contents
LAPSE:2025.0324
Published Article
LAPSE:2025.0324
Analysis of Control Properties as a Sustainability Indicator in Intensified Processes for Levulinic Acid Purification
Tadeo E. Velázquez-Sámano, Heriberto Alcocer-García, Eduardo Sánchez-Ramírez, Carlos R. Caceres-Barrera, Juan G. Segovia-Hernández
June 27, 2025
Abstract
The evaluation of control properties in industrial processes is essential to achieve sustainability, a very relevant topic today. This study emphasizes the importance of control studies to ensure that processes are efficient, operable and safe. While strategies such as process intensification can reduce the size, cost, and consumption of energy, it can present challenges in control and operability. This work focuses on the evaluation of the control properties of schemes with different degrees of intensification for the purification of levulinic acid, with the aim of identifying designs with the best control properties and the best economic and environmental indicators. The schemes were designed under a systematic synthesis strategy and optimized using the hybrid method of differential evolution with a tabu list, considering the total annual cost and Eco-indicator 99. An open-loop study analyzed the relationship between manipulable variables and output variables using total condition number, sensitivity index, and relative gain matrix analysis. The dynamic behavior in a closed loop was subsequently analyzed using the minimization of the absolute error integral as a criterion. The results showed that the design, which includes a liquid-liquid extraction column, three distillation columns, and thermal coupling, presented the best dynamic performance. This design had a low total condition number, a below-average sensitivity index, a stable control structure, and low values of the absolute error integral. In addition, it stood out for its excellent cost and environmental impact indicators, which makes it the most favorable option among the proposed designs.
Keywords
Bioproducts, Control, Distillation, Stochastic Optimization
Suggested Citation
Velázquez-Sámano TE, Alcocer-García H, Sánchez-Ramírez E, Caceres-Barrera CR, Segovia-Hernández JG. Analysis of Control Properties as a Sustainability Indicator in Intensified Processes for Levulinic Acid Purification. Systems and Control Transactions 4:1071-1076 (2025) https://doi.org/10.69997/sct.104729
Author Affiliations
Velázquez-Sámano TE: Guanajuato University, Chemical Engineering Department, Guanajuato, Guanajuato, México
Alcocer-García H: Guanajuato University, Civil and Ambiental Engineering Department, Guanajuato, Guanajuato, México
Sánchez-Ramírez E: Guanajuato University, Chemical Engineering Department, Guanajuato, Guanajuato, México
Caceres-Barrera CR: Guanajuato University, Chemical Engineering Department, Guanajuato, Guanajuato, México
Segovia-Hernández JG: Guanajuato University, Chemical Engineering Department, Guanajuato, Guanajuato, México
Journal Name
Systems and Control Transactions
Volume
4
First Page
1071
Last Page
1076
Year
2025
Publication Date
2025-07-01
Version Comments
Original Submission
Other Meta
PII: 1071-1076-1304-SCT-4-2025, Publication Type: Journal Article
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LAPSE:2025.0324
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References Cited
  1. Ukawa-Sato R, Hirano N, Fushimi C. Design and techno-economic analysis of levulinic acid production process from biomass by using co-product formic acid as a catalyst with minimal waste generation. Chem. Eng. Res. Des 192:389-401 (2023) https://doi.org/10.1016/j.cherd.2023.02.046
  2. Olujic Ž, Jödecke M, Shilkin A, Kaibel, B. Equipment improvement trends in distillation. Chem. Eng. Process.: Process Intensif 48:1089-1104 (2009) https://doi.org/10.1016/j.cep.2009.03.004
  3. Tian Y, Demirel SE, Hasan MMF, Pistikopoulos EN. An overview of process systems engineering approaches for process intensification: State of the art. Chem. Eng. Process.: Process Intensif 133:160-210 (2018) https://doi.org/10.1016/j.cep.2018.07.014
  4. Villegas-Uribe CA, Medina-Herrera N, Hernández-Magallanes JA, Tututi-Avila S. Optimal design and control of three simplified sargent four-product dividing-wall columns. Chem. Eng. Process.: Process Intensif 174:108860 (2022) https://doi.org/10.1016/j.cep.2022.108860
  5. Arenas-Grimaldo C, Avendaño-Guerrero JG, Molina-Guerrero CE, Segovia-Hernández JG. Design and control of a distillation sequence for the purification of bioethanol obtained from sotol bagasse (Dasylirium sp.). Chem. Eng. Res. Des 203:11-17 (2024) https://doi.org/10.1016/j.cherd.2023.12.039
  6. Li M, Peng J, Cheng Y, Zhu X, Ma Y, Zhang Z, Gao J. Dynamic control of an energy-saving process with two extractive dividing-wall columns for separation of acetone/methanol/butanone/tert-butyl alcohol mixtures. Chem. Eng. Res. Des 200:281-291 (2023) https://doi.org/10.1016/j.cherd.2023.10.045
  7. Pushkala SP, Panda RC. Design and analysis of reactive distillation for the production of isopropyl myristate. Clean. Chem. Eng 5:100090 (2023) https://doi.org/10.1016/j.clce.2022.100090
  8. Alcocer-García H, Segovia-Hernández JG, Prado-Rubio OA, Sánchez-Ramírez E, Quiroz-Ramírez JJ. Multi-objective optimization of intensified processes for the purification of levulinic acid involving economic and environmental objectives. Part II: A comparative study of dynamic properties. Chem. Eng. Process.: Process Intensif 147:107745 (2020) https://doi.org/10.1016/j.cep.2019.107745
  9. Schmidt LM, Mthembu LD, Reddy P, Deenadayalu N, Kaltschmitt M, Smirnova I. Levulinic acid production integrated into a sugarcane bagasse based biorefinery using thermal-enzymatic pretreatment. Ind Crops Prod 99:172-178 (2017) https://doi.org/10.1016/j.indcrop.2017.02.010
  10. Alcocer-García H, Segovia-Hernández JG, Sánchez-Ramírez E, Caceres-Barrera CR, Hernández S. Sequential Synthesis Methodology in the Design and Optimization of Sustainable Distillation Sequences for Levulinic Acid Purification. Bioenergy Res 1-15 (2024) https://doi.org/10.1007/s12155-024-10765-0
  11. Santaella MA, Jiménez LE, Orjuela A, Segovia-Hernández JG. Design of thermally coupled reactive distillation schemes for triethyl citrate production using economic and controllability criteria. Chem. Eng. J 328:368-381 (2017) https://doi.org/10.1016/j.cej.2017.07.015
  12. Prado-Rubio OA, Jørgensen SB, Jonsson G. Control System Development for Integrated Bioreactor and Membrane Separation Process. Comput. Aided Chem. Eng 28:289-294 (2010) https://doi.org/10.1016/S1570-7946(10)28049-5