Abstract
Conventional and advanced exergy and exergoeconomic analyses are investigated on a coupled LiBr/H2O cycle/ORC system, which recovers low-grade residual heat to generate electricity. Exergy destruction rates, exergy destruction cost rates, and investment cost rates are calculated based on the exergy balance, cost balance, and auxiliary equations. The results indicate that 32.02% of the irreversibility rates, 37.66% of the irreversibility cost rates, and 25.83% of the investment cost rates can be eliminated. The ORC evaporator contributes to the highest irreversibility rate, and the LiBr absorber has the supreme investment cost rate. 83.17% of the exergy destruction rates are endogenous, which means that each component itself has a critical effect on system performance. In the advanced exergoeconomic analyses, 77.30% of the investment cost is generated by the components themselves. Except for LiBr pumps, other components reduce their exergy destruction cost rates preferentially. Optimizing methods to decrease the irreversibility of the system are also provided by this analysis.
| Original language | English |
|---|---|
| Pages (from-to) | 5825–5837 |
| Number of pages | 13 |
| Journal | ACS Sustainable Chemistry and Engineering |
| Volume | 10 |
| Issue number | 18 |
| DOIs | |
| Publication status | Published - 9 May 2022 |
UN SDGs
This output contributes to the following UN Sustainable Development Goals (SDGs)
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SDG 7 Affordable and Clean Energy
Keywords
- absorption refrigeration cycle
- advanced exergy
- cascade utilization
- exergoeconomic analysis
- exergy destruction rate
- organic Rankine cycle
ASJC Scopus subject areas
- General Chemistry
- Environmental Chemistry
- General Chemical Engineering
- Renewable Energy, Sustainability and the Environment
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