2009
DOI: 10.1016/j.jprocont.2008.06.016
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Model-predictive control of feed flow reversal in a reverse osmosis desalination process

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Cited by 63 publications
(11 citation statements)
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“…In general, a RO desalination plant is a multi-input multi-output (MIMO) nonlinear system where the nonlinearity is caused by the nonlinear behavior of each unit and practical challenges such as fouling, fault and model mismatch. In some works, the model of a RO system is considered nonlinear and time-invariant with respect to the membrane, and valves fouling, membrane deformations and faults (Bartman et al, 2009). If the actuator fault is regarded as a nonlinear behavior of the system, the nonlinear dynamics of the system will become very complicated.…”
Section: Plant Descriptionmentioning
confidence: 99%
See 1 more Smart Citation
“…In general, a RO desalination plant is a multi-input multi-output (MIMO) nonlinear system where the nonlinearity is caused by the nonlinear behavior of each unit and practical challenges such as fouling, fault and model mismatch. In some works, the model of a RO system is considered nonlinear and time-invariant with respect to the membrane, and valves fouling, membrane deformations and faults (Bartman et al, 2009). If the actuator fault is regarded as a nonlinear behavior of the system, the nonlinear dynamics of the system will become very complicated.…”
Section: Plant Descriptionmentioning
confidence: 99%
“…Additionally, based on the parity space method, (Wu et al, 2018) investigated the problem of fault detection for the linear discrete time-varying system with multiplicative noise. On the other hand, MPCs are powerful tools to control RO desalination plants (Abbas, 2006), (Bartman et al, 2009). The AFTC –based model predictive controllers seemed to be the most functional approach to control RO desalination plants according to literature (Mcfall et al, no date), (Gambier et al, 2009, 2010).…”
Section: Introductionmentioning
confidence: 99%
“…Many studies have made great contributions to the desalination literature to control RO systems. The control schemes include conventional (Alatiqi et al 1989;AlDhaifallah et al 2012;Sobana & Panda 2014;Ashagre et al 2020), feedforward (McFall et al 2008, optimal (Gambier et al 2009;Ghobeity & Mitsos 2010), adaptive (Gu et al 2013), model predictive control (MPC) (Robertson et al 1996;Abbas 2006;Bartman et al 2009aBartman et al , 2009bYang et al 2012), neural networks (Madaeni et al 2015), fractional order (Feliu-Batlle et al 2017), androbust control (Al-haj et al 2010;Phuc et al 2015Phuc et al , 2016Zebbar et al 2019). Among those, the most common types of controllers are based on PID and MPC (Sobana & Panda 2014).…”
Section: Introductionmentioning
confidence: 99%
“…For the critical variables' control of the seawater RO desalination plants, diverse controllers have been developed. These controllers are mainly: conventional [41][42][43], feedforward [37], optimal [28,44], adaptive [35], model predictive [45][46][47][48], fractional order [49], or robust [32,[50][51][52]. In these plants, the most implemented controller is the proportional integral derivative (PID), owing to the fact that many process engineers are much more familiar with this class of controller than with sophisticated advanced controllers, due their functional simplicity, which allows them to operate in a straightforward mode [53,54].…”
Section: Introductionmentioning
confidence: 99%