2013
DOI: 10.1016/j.jprocont.2013.09.023
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Nonlinear model predictive control of biodiesel production via transesterification of used vegetable oils

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Cited by 26 publications
(17 citation statements)
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“…The interested reader can refer to excellent review articles in this area [155][156][157][158][159]. The operation and control of biomass-based processes pose unique challenges such as variable (type and concentration) feed [160], distributed nature of raw material availability [161], nonlinear dynamics [162][163][164] and fewer online measurements [165].…”
Section: Renewable Fuelsmentioning
confidence: 99%
See 1 more Smart Citation
“…The interested reader can refer to excellent review articles in this area [155][156][157][158][159]. The operation and control of biomass-based processes pose unique challenges such as variable (type and concentration) feed [160], distributed nature of raw material availability [161], nonlinear dynamics [162][163][164] and fewer online measurements [165].…”
Section: Renewable Fuelsmentioning
confidence: 99%
“…In the context of bio-diesel production, most of the control studies have focused on the control of the transesterification reactor which is the heart of the bio-diesel production process. Optimal control (deterministic and stochastic) [160,174] and MPC [162,164,[175][176][177] seem to be the popular choices for this reactor control problem. Operation and control of reactive separation systems have also been pursued for biodiesel production systems, however, most of these contributions use simple PID controllers [178,179].…”
Section: Renewable Fuelsmentioning
confidence: 99%
“…An appropriated mathematical model can be used to predict the effect of disturbances in biodiesel reactors, including these caused by oil change, and help to reduce the negative effects by the design of a control system [3,4,[12][13][14][15]. Nonetheless, the continuous reactor model previously reported does not consider the dynamics of feed oil changes.…”
Section: Introductionmentioning
confidence: 99%
“…Literature shows burgeoning interest in advanced model based control of a transesterification reactor [5,[8][9][10][11][12][13][14][15][16]]. An approach to determine an optimal temperature trajectory for a batch reactor was presented in [5].…”
Section: Introductionmentioning
confidence: 99%
“…Consequently, deviations between the desired and actual states occurring during the process cannot be corrected and disturbances cannot be compensated. A method to overcome these drawbacks of open-loop control was presented by [14]. In this work, the economic performance of a semi-batch reactor for the production of biodiesel was optimized by using a nonlinear model predictive control (NMPC) strategy.…”
Section: Introductionmentioning
confidence: 99%