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The parameter values were estimated by direct adapting from literature (e.g., the Km value of SERCA) or indirect fitting (e.g., for maximum pump rate of SERCA based on the decay of Ca2+ transient); see Table 3 for a complete list of modified parameters.
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MOGA model is applied to the MAIWF to develop maximum pumping rate and minimum operation cost.
The maximum pumping rate of the developed micro-pump is 28 μL/min at an air pressure of 10 psi and a driving frequency of 10 Hz.
MOGA model applied in Wadi El-Farigh, Egypt, to develop the maximum pumping rate and minimum operation cost as well as to predict the future changes in both pumping rate and pumping operation cost.
In phase one, the current pumping rate (Q_i^{ k)}) of the (i{mathrm{th}}) well, obtained in (6), is being rectified in case it violates the local maximum, the local minimum or the global maximum pumping rate constraints.
When L* < 0.87W* + 0.62, by contrast, the impact from inland exceeds that from lateral and hence, resulting in a smaller maximum interface toe location and a higher maximum pumping rate.
It is found that the impact from both inland and lateral boundaries could play a significant role on the interface toe location and maximum pumping rate (defined as the maximum allowable pumping rate that will not lead to pumping saltwater), depending on sizes of domain length and width.
When L* > 0.87W* + 0.62, the impact from lateral overcomes that from inland, producing a larger maximum interface toe location and a lower maximum pumping rate than those in SS.
We compare the interface toe location and maximum pumping rate among three scenarios that assume (S1) an infinite domain width and a finite domain length, (S2) a finite domain width and length, and (SS) an infinite domain width and length.
By inspection only of the reported results one may easily verify that this is an untroubled case in the sense that the active pumping locations may perform at maximum pumping rates without any threat from saltwater intrusion.
Constraints capture mechanical or physical process limitations (such as maximum pumping rates, and treatment train capacities) or interim and final values of state variables at discrete or continuous regions of the modeled domain.
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