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Pumping cost.
The pumping cost is assumed to be zero.
Other LCOE elements such as pumping cost of PSHPP and fuel costs of SCGT were calculated under different scenarios.
The viscosity of the emulsion desired to reduce the pumping cost is around 400 cP at ambient temperature.
This is only valid provided that the PSHPP's capital cost should not exceed 4180 $/kW at zero pumping cost.
According to this relationship, the decision maker can work out the groundwater management considering both pumping rate and pumping cost.
Each point in this figure represents a possible solution for the problem, which contains pumping rate versus operation pumping cost.
The fuel cost is observed to be highly sensitive, while pumping cost has been found to be least sensitive.
From a baseline run, it was observed that the pumping cost was hardly 1%% of the total revenue.
A groundwater management problem is presented involving pumping cost minimization with both well discharges and well locations as decision variables.
Sensitivity analysis on the storage-reliability constraint, its influence on pumping cost, water quality, and tank sizing are explored.
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