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This paper introduces a new approach for the design of water utilization networks featuring minimum freshwater usage and minimum utility consumption in process plants.
An ensuing graphical method is developed for targeting the pinch point and minimum utility consumption of the hydrogen system with purification reuse.
Therefore, the entropy change which indicates the thermodynamic irreversibility of the satisfying process is minimized for each sink to obtain the minimum utility consumption.
A multi-criteria synthesis strategy for heat-exchanger networks (HENs) simultaneously considering minimum utility consumption, maximum source-stream temperature flexibility, and even minimum number of matches is proposed.
The proposed method is based on the principle that minimizing thermodynamic irreversibility of the satisfying process will result in minimum utility consumption of the hydrogen network.
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Earlier work showed how to discover minimum utility use for these restricted match problems.
Then, the quantitative relationship between the hydrogen utility adjustment and the hydrogen surplus is deduced, and a numerical method for identifying the pinch point and the minimum hydrogen utility consumption target is developed.
The minimum utility cost is shown to not necessarily be the maximum of the single component minimum utility costs.
We normalize minimum utility to zero adding a constant.
Protocol 6 (KAQ) deStepbes a greedy algoridentifiescomputhe a suboptimized -anonymous quantization mapping funcells from thatdata.
Hydrogen utility consumption minimization is one of the key strategies for reducing refinery operating costs.
More suggestions(15)
minimum utility value
minimum power consumption
minimum sample consumption
minimum utility score
minimum utility threshold
minimum fuel consumption
minimum heat consumption
minimum utility use
minimum utility cost
minimum propellant consumption
minimum energy consumption
minimum hydrogen consumption
minimum exergy consumption
minimum resource consumption
minimum solvent consumption
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