An operating model for dead-end membrane filtration is proposed based on the well-known blocking laws. The resulting model contains three parameters representing, the operating strategy, the fouling mechanism and the fouling potential of the feed. The optimal control strategy is determined by minimizing the energy consumption for a fixed final time and produced volume. It was found that constant power filtration leads to minimal energy consumption. Constant flux and constant pressure filtration have equal energy costs. However, compared to strategies with a non-decreasing pressure and non-increasing flux, the relative savings are small. Only if the fouling mechanism resembles standard blocking and the fouling resistance is large compared to...
In filling lines equipped with membrane separation devices in the form of filters energy, consumptio...
Organic fouling on the membrane can be minimised through powdered activated carbon (PAC) usage in th...
Concentration polarization (CP) and membrane fouling are two major drawbacks for pressure-driven mem...
An operating model for dead-end membrane filtration is proposed based on the well-known blocking law...
An operating model for dead-end membrane filtration is proposed based on the well-known blocking law...
An operating model for dead-end membrane filtration is proposed based on the well-known blocking law...
A control strategy aimed at minimizing energy consumption is formulated for non-ideal dead-end cake ...
A control strategy aimed at minimizing energy consumption is formulated for non-ideal dead-end cake ...
A control strategy aimed at minimizing energy consumption is formulated for non-ideal dead-end cake ...
In this paper a control strategy is formulated that minimizes the costs for a single chemical cleani...
International audienceThis paper presents an optimal control strategy allowing the maximization of t...
Journée organisée conjointement par l'objet thématique SAMI (Système, Analyse, Modélisation, Informa...
In filling lines equipped with membrane separation devices in the form of filters energy, consumptio...
Organic fouling on the membrane can be minimised through powdered activated carbon (PAC) usage in th...
Concentration polarization (CP) and membrane fouling are two major drawbacks for pressure-driven mem...
An operating model for dead-end membrane filtration is proposed based on the well-known blocking law...
An operating model for dead-end membrane filtration is proposed based on the well-known blocking law...
An operating model for dead-end membrane filtration is proposed based on the well-known blocking law...
A control strategy aimed at minimizing energy consumption is formulated for non-ideal dead-end cake ...
A control strategy aimed at minimizing energy consumption is formulated for non-ideal dead-end cake ...
A control strategy aimed at minimizing energy consumption is formulated for non-ideal dead-end cake ...
In this paper a control strategy is formulated that minimizes the costs for a single chemical cleani...
International audienceThis paper presents an optimal control strategy allowing the maximization of t...
Journée organisée conjointement par l'objet thématique SAMI (Système, Analyse, Modélisation, Informa...
In filling lines equipped with membrane separation devices in the form of filters energy, consumptio...
Organic fouling on the membrane can be minimised through powdered activated carbon (PAC) usage in th...
Concentration polarization (CP) and membrane fouling are two major drawbacks for pressure-driven mem...