Identification and control of a pilot scale binary distillation column

Logist, Filip; Huyck, Bart; Fabre, M.; Verwerft, M.; Pluymers, Bert; Brabanter, Jos De; Moor, Bart De; Impe, Jan Van

doi:10.23919/ecc.2009.7075136

Search citation statements

Order By: Relevance

Paper Sections

Select...

Methods1

Citation Types

Supporting

Mentioning

Contrasting

Year Published

2011

2014

Publication Types

Select...

Article2

Other1

Relationship

Self Cite1

Independent2

Authors

Journals

Cited by 3 publications

(1 citation statement)

References 2 publications

Supporting

Mentioning

Contrasting

Order By: Relevance

“…The reboiler duty Qr is a repeated periodic signal of 6000 s. The clock period, i.e. the minimum time before the signal is allowed to switch, is 300 s. From former experiments (Logist et al, 2009), it is known that the dynamics of the system are faster at the top of the column. Therefore, the clock period of the other inputs is slightly smaller.…”

Section: Methodsmentioning

confidence: 99%

Identification of a Pilot Scale Distillation Column: A Kernel Based Approach

Huyck

Brabanter

Logist

et al. 2011

IFAC Proceedings Volumes

Self Cite

View full text Add to dashboard Cite

Section: Methodsmentioning

confidence: 99%

Identification of a Pilot Scale Distillation Column: A Kernel Based Approach

Huyck

Brabanter

Logist

et al. 2011

IFAC Proceedings Volumes

Self Cite

View full text Add to dashboard Cite

Online model predictive control of industrial processes using low level control hardware: A pilot-scale distillation column case study

Huyck

Brabanter

Moor

et al. 2014

Control Engineering Practice

View full text Add to dashboard Cite

Simplified Discrete Binary PSO tuned Multivariable PID Controller for Binary Distillation Column plant

Queen

Auxillia

2013

2013 International Conference on Circuits, Power and Computing Technologies (ICCPCT)

View full text Add to dashboard Cite

In this paper a Multivariable PID Controller is designed for a Binary Distillation column plant. The Binary Distillation Column is mainly used for the separation of liquid mixtures containing volatile and non-volatile components. To maintain the mole fraction of the distillate the PID Controller regulates the vapour tlow rate and liquid tlow rate. Decoupler is used to avoid loop interactions as it may cause instability. The PID controller is tuned using the Particle Swarm Optimization (PSO) algorithm and the Discrete Binary Particle Swarm Optimization (DBPSO) algorithm and Simplitied Discrete Binary Particle Swarm Optimization (SDBPSO) algorithm to obtain reduced settling time. Simulations are carried out to minimize Integral of Absolute Error (IAE). Transient response analysis shows the better performance of SDBPSO algorithm over PSO and DBPSO algorithm. Stability analysis is done using pole-zero map and Nyquist plot.

show abstract

Identification and control of a pilot scale binary distillation column

Cited by 3 publications

References 2 publications

Identification of a Pilot Scale Distillation Column: A Kernel Based Approach

Identification of a Pilot Scale Distillation Column: A Kernel Based Approach

Online model predictive control of industrial processes using low level control hardware: A pilot-scale distillation column case study

Simplified Discrete Binary PSO tuned Multivariable PID Controller for Binary Distillation Column plant

Contact Info

Product

Resources

About