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Further, two exergy destruction ratios were used: (y_k) and (y^*_k), Eqs.
Exergy analysis of each sub-system leads to the choice of the optimum physical parameters for minimum local exergy destruction ratios.
The indirect gasifier and the gas combustor are identified as the main sources of irreversibility within the three process configurations, with exergy destruction ratios of 21%and5 7%7%, respectively.
The exergy destruction rates, exergy destruction ratios and exergetic performance values of presented integrated system and its subsystems are determined by using the balance equations for mass, energy, entropy, energy and exergy and evaluated their performances by means of energetic and exergetic efficiencies.
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Exergy destruction ratio.
As shown in Fig. 6c, the E. coli destruction ratio increases with time.
Additionally, the exergy destruction ratio and exergy efficiency of each subsystem are researched.
Exergetic efficiency and exergy destruction ratio are calculated for the whole system according to the second law of thermodynamics.
With an increase in the steam conditions, the exergy destruction ratio of the boiler is significantly reduced, contributing mainly to the system improvement.
Results show the exergy destruction ratio of the oil shale process integrated with hydrogen production from retorting gas is the least, 41.6%, followed by the oil shale process integrated with hydrogen production and oil hydrogenation, 45.9%.
The main factors considered in the model are the ratio of green deconstruction (i.e., building deconstruction) managers vs. conventional demolition (i.e. building destruction) managers, the ratio of green design managers (i.e. design for deconstruction) vs. conventional design managers, and the interaction behavior of heterogeneous stakeholders following the herd theory.
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