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The minimum utility cost is shown to not necessarily be the maximum of the single component minimum utility costs.
This paper addresses minimum utility cost mass-exchange network design by considering the special case of water minimisation.
This model returns a near-to-optimal network configuration with minimum utility cost while allows to select geographically closest matches.
Next, a novel problem, namely the pinch-based calculation of Minimum Utility Cost for a separable heat and mass exchange network, is solved.
The minimum utility cost problem is investigated for a single mass exchanger which is required to meet composition targets in multiple components.
This work aims at quantifying the minimum utility cost necessary to complete a given separation task using vapor liquid equilibrium (distillation) operations.
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Rigorous process simulations are used to build the surrogate model, while pinch analysis is employed to determine the maximum heat recovery and minimum utility costs.
In the second stage, a mixed-integer linear program is solved to yield minimum-utility cost networks in which the number of mass-exchanger units is minimized.
The HEN formulation is presented and solved to attain minimum heating and cooling utility cost and for selecting the optimum utilities.
Until now, minimum utility targets have existed, but not capital cost targets.
Utility Cost of Formal Privacy for Releasing National Employer-Employee Statistics.
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Justyna Jupowicz-Kozak
CEO of Professional Science Editing for Scientists @ prosciediting.com