2006
DOI: 10.2166/wst.2006.125
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Total cost minimization control scheme for biological wastewater treatment process and its evaluation based on the COST benchmark process

Abstract: This paper proposes a new cost minimisation control scheme for a predenitrification type of biological wastewater treatment process and evaluates the validity of the control scheme based on the benchmark process presented by Copp. The control scheme adopting a hierarchical control structure incorporates lower-level controllers that consist of a set of local dynamic controllers and a higher-level static optimiser that provides the set points of the lower-level controllers based on the total cost index of Vanrol… Show more

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Cited by 17 publications
(4 citation statements)
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“…This definition assumes that lower electricity consumption would linearly lead to reductions in operational costs and/or in greenhouse gas (GHG) emissions related to the electricity production. Other studies considered effluent quality/cost by introducing weights on concentrations and electricity consumption (Yamanaka et al 2006). However, the current development in electricity supply, going towards a higher penetration of renewable energy sources (Ren21, 2020), undermines this assumption of a direct correlation between electricity consumption and costs/emissions.…”
Section: )mentioning
confidence: 99%
“…This definition assumes that lower electricity consumption would linearly lead to reductions in operational costs and/or in greenhouse gas (GHG) emissions related to the electricity production. Other studies considered effluent quality/cost by introducing weights on concentrations and electricity consumption (Yamanaka et al 2006). However, the current development in electricity supply, going towards a higher penetration of renewable energy sources (Ren21, 2020), undermines this assumption of a direct correlation between electricity consumption and costs/emissions.…”
Section: )mentioning
confidence: 99%
“…en Yamanaka et al (2006) se utiliza el BSM1 y una estructura jerárquica en la que un controlador de alto nivel proporciona los set-point en base a una optimización mediante GA. Los GA son utilizados también en Beraud et al (2009) para la optimización de los set-point en las diferentes zonas aeróbicas, obteniendo un cierto ahorro energético a la vez que se mantienen los niveles de tratamiento deseados. En Åmand y Carlsson (2012) se aplica optimización para minimizar la variable manipulada K L a con la restricción de que el amonio en el efluente no supere un valor prefijado.…”
Section: Aplicación De Técnicas De Optimizaciónunclassified
“…[15] used a hierarchical structure of two PI layers for optimizing the operation of a nutrient removal WWTP. In [16], a PI controller in the lower level follows an ammonia setpoint determined by GA optimization in the higher level. The method in [17] proposes a unique approach that divides the control structure into three layers: the supervisory control layer, the optimizing control layer and, and the low-level control layer.…”
Section: Introductionmentioning
confidence: 99%