2014
DOI: 10.1016/j.desal.2014.03.014
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Modeling and control of reverse osmosis desalination process using centralized and decentralized techniques

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Cited by 25 publications
(11 citation statements)
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“…The proposed method is compared with the main steam temperature model by Valsalam [18] . The MSE value for the proposed method is 1.8595e-08 and the MSE value for the Valsalam model is 7.2531.…”
Section: Resultsmentioning
confidence: 99%
See 1 more Smart Citation
“…The proposed method is compared with the main steam temperature model by Valsalam [18] . The MSE value for the proposed method is 1.8595e-08 and the MSE value for the Valsalam model is 7.2531.…”
Section: Resultsmentioning
confidence: 99%
“…Statistical model for the desalination of sea water was proposed by Sobana and Panda [18] . The regression analysis and ANOVA was performed for the developed statistical model.…”
Section: Introductionmentioning
confidence: 99%
“…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). PID-based controllers include the classical one (AlDhaifallah et al 2012;Sobana & Panda 2014), or modified PID such as auto-tuned PID (Rathore et al 2013;Chithra et al 2015).…”
Section: Introductionmentioning
confidence: 99%
“…Among those, the most common types of controllers are based on PID and MPC (Sobana & Panda 2014). PID-based controllers include the classical one (AlDhaifallah et al 2012;Sobana & Panda 2014), or modified PID such as auto-tuned PID (Rathore et al 2013;Chithra et al 2015). Those controllers can work well but with poor robustness even without uncertainty.…”
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%