An enhanced feedback-feedforward control scheme for process industries
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Manish Yadav
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Hirenkumar G. Patel
Abstract
In this article, a unified control scheme is proposed for dead-time compensation and disturbance rejection via feedback and feedforward controller. The objectives of this work are suggested in two folds, first tuning of fractional order feedback controller via delayed Bode’s ideal transfer function instead of conventional Bode’s ideal transfer function with the benefits of dead time compensator and second feedforward controller for disturbance rejection. An existing method is utilized for comparison with the proposed scheme. To examine the efficacy of the proposed method robustness test is also carried out via sensitivity analysis. For quantifiable evaluation of the proposed scheme Integral Absolute Error (IAE) and Integral Square Error (ISE) are utilized. For the usefulness of the proposed scheme, two practical problems are demonstrated in this paper. The limpidity and instinctive appeal of the proposed scheme make it beautiful for industrial applications.
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Author contributions: All the authors have accepted responsibility for the entire content of this submitted manuscript and approved submission.
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Research funding: None declared.
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Conflict of interest statement: The authors declare no conflicts of interest regarding this article.
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© 2021 Walter de Gruyter GmbH, Berlin/Boston
Artikel in diesem Heft
- Frontmatter
- Research Articles
- Nonlinear autoregressive-moving average-L2 (NARMA-L2) controller for multivariable ball mill plant
- An enhanced feedback-feedforward control scheme for process industries
- Appling the computational fluid dynamics studies of the thermogravitational column for N2-CO2 and He-Ar gas mixtures separation
- An enhancement in series cascade control for non-minimum phase system
- Modelling and simulation of industrial multistage flash desalination process with exergetic and thermodynamic analysis. A case study of Azzour seawater desalination plant
- Development of a CFD-based simulation model and optimization of thermal diffusion column: application on noble gas separation
- A machine-learning reduced kinetic model for H2S thermal conversion process
- Design strategies for oxy-combustion power plant captured CO2 purification
- Energy-saving investigation of vacuum reactive distillation for the production of ethyl acetate
- Reducing total annual cost and CO2 emissions in batch distillation for separating ternary wide boiling mixtures using vapor recompression heat pump
Artikel in diesem Heft
- Frontmatter
- Research Articles
- Nonlinear autoregressive-moving average-L2 (NARMA-L2) controller for multivariable ball mill plant
- An enhanced feedback-feedforward control scheme for process industries
- Appling the computational fluid dynamics studies of the thermogravitational column for N2-CO2 and He-Ar gas mixtures separation
- An enhancement in series cascade control for non-minimum phase system
- Modelling and simulation of industrial multistage flash desalination process with exergetic and thermodynamic analysis. A case study of Azzour seawater desalination plant
- Development of a CFD-based simulation model and optimization of thermal diffusion column: application on noble gas separation
- A machine-learning reduced kinetic model for H2S thermal conversion process
- Design strategies for oxy-combustion power plant captured CO2 purification
- Energy-saving investigation of vacuum reactive distillation for the production of ethyl acetate
- Reducing total annual cost and CO2 emissions in batch distillation for separating ternary wide boiling mixtures using vapor recompression heat pump
