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Publications by David Liñan Romero

Peer reviewed

Articles

[1]
Liñan Romero, D. A., McCormick-Mantilla, J. A. & Ricardez-Sandoval, L. A. (2025). Economic Nonlinear Model Predictive Control and Scheduling of Multiple Fed-Batch Fermenters in a Lignocellulosic Biorefinery. Computers and Chemical Engineering, 201, 109223.
[2]
Ovalle, D., Liñan, D. A., Lee, A., Gómez, J. M., Ricardez-Sandoval, L., Grossmann, I. E. & Neira, D. E. B. (2025). Logic-Based Discrete-Steepest Descent : A Solution Method for Process Synthesis Generalized Disjunctive Programs. Computers and Chemical Engineering, 195.
[4]
Liñan, D. A., Contreras-Zarazúa, G., Sánchez-Ramírez, E., Segovia-Hernández, J. G. & Ricardez-Sandoval, L. A. (2024). A hybrid deterministic-stochastic algorithm for the optimal design of process flowsheets with ordered discrete decisions. Computers and Chemical Engineering, 180.
[5]
Liñan, D. A. & Ricardez-Sandoval, L. A. (2024). Discrete-Time Network Scheduling and Dynamic Optimization of Batch Processes with Variable Processing Times through Discrete-Steepest Descent Optimization. Industrial & Engineering Chemistry Research, 63(10), 4478-4495.
[8]
Liñan, D. A. & Ricardez-Sandoval, L. A. (2022). Optimal design and dynamic transitions of multitask catalytic distillation columns : A Discrete-Steepest Descend Framework. Chemical Engineering and Processing, 180.
[9]
Iftakher, A., Liñan, D. A., Mansouri, S. S., Nahid, A., Hasan, M. F., Choudhury, M. S. ... Lee, J. H. (2022). RD-toolbox : A computer aided toolbox for integrated design and control of reactive distillation processes. Computers and Chemical Engineering, 164.
[10]
Liñan Romero, D. A., Bernal, D. E., Gomez, J. M. & Ricardez-Sandoval, L. A. (2021). Optimal synthesis and design of catalytic distillation columns : A rate-based modeling approach. Chemical Engineering Science, 231.
[11]
Liñan, D. A., Bernal, D. E., Ricardez-Sandoval, L. A. & Gómez, J. M. (2020). Optimal design of superstructures for placing units and streams with multiple and ordered available locations : Part II: Rigorous design of catalytic distillation columns. Computers and Chemical Engineering, 139.
[12]
Liñan, D. A., Bernal, D. E., Ricardez-Sandoval, L. A. & Gómez, J. M. (2020). Optimal design of superstructures for placing units and streams with multiple and ordered available locations. Part I : A new mathematical framework. Computers and Chemical Engineering, 137.

Conference papers

[13]
Liñan, D. A., Reynoso-Donzelli, S., Ricardez-Sandoval, L. A. (2024). Optimal scheduling and open-loop control of network batch processes under variable processing times using Generalized Benders Decomposition. In 2024 American Control Conference (ACC). (pp. 4466-4471). Institute of Electrical and Electronics Engineers (IEEE).
[14]
Liñan, D. A., Ricardez-Sandoval, L. A. (2022). A discrete-steepest descent framework for the simultaneous process and control design of multigrade reactive distillation columns. In IFAC-PapersOnLine. (pp. 370-375). Elsevier BV.
[15]
Bernal, D. E., Ovalle, D., Liñan, D. A., Ricardez-Sandoval, L. A., Gómez, J. M., Grossmann, I. E. (2022). Process superstructure optimization through discrete steepest descent optimization : a GDP analysis and applications in process intensification. In Computer Aided Chemical Engineering. (pp. 1279-1284). Elsevier BV.
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2025-10-05 00:05:00 UTC