Abstract

This study focused on investigating the bottoming power cycles operating with CO2-based binary mixture, taking into account exergetic, economic and exergo-environmental impact indices. The main intent is to assess the benefits of employing a CO2-based mixture working fluid in closed Brayton bottoming power cycles in comparison with pure CO2 working fluid. Firstly, selection criteria for the choice of suitable additive compound for CO2-based binary mixture is delineated and the composition of the binary mixture is decided based on required cycle minimum temperature. The decided CO2-C7H8 binary mixture with a 0.9 mole fraction of CO2 is analyzed in two cycle configurations: Simple regenerative cycle (SRC) and Partial heating cycle (PHC). Comparative analysis among two configurations with selected working fluid are carried out. Thermodynamic analyses at varying cycle pressure ratio shows that cycle with CO2-C7H8 mixture shows maximum power output and exergy efficiency at rather higher cycle pressure ratio compared to pure CO2 power cycles. PHC with CO2-C7H8 mixture shows 28.68% increment in exergy efficiency with the levelized cost of electricity (LCOE) 21.62% higher than pure CO2 PHC. Whereas, SRC with CO2-C7H8 mixture shows 25.17% increment in exergy efficiency with LCOE 57.14% higher than pure CO2 SRC. Besides showing lower economic value, cycles with a CO2-C7H8 mixture saves larger CO2 emissions and also shows greater exergo-environmental impact improvement and plant sustainability index.

Highlights

  • Efficiency in heat to power conversion systems is a global concern

  • This study investigates the exergetic, economic, and exergo-environmental performance of two different configurations of bottoming power cycles powered by carbon dioxide-based binary mixture for warm climatic conditions

  • It can be observed that maximum power output occurs at the pressure ratio of 4.4 for 0.9CO2/0.1C7H8 Partial heating cycle (PHC) as in the case of exergy efficiency

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Summary

Introduction

Efficiency in heat to power conversion systems is a global concern. Power-generating systems possessing improved thermodynamic, economic, and environmental performances are a top priority of researchers and manufacturers [1]. The performance enhancement of S-CO2 Brayton power cycles in high ambient temperature zones can be achievable by relocating the CO2 critical point to higher temperatures by adding the second working fluid in CO2 ; this can be done by designing a CO2- based binary mixture [17]. The research on power cycles powered by CO2 -based binary mixtures has been growing in the selection of working fluids and performance optimization of power cycles for both low and high-temperature heat sources [21,22]. This study investigates the exergetic, economic, and exergo-environmental performance of two different configurations of bottoming power cycles powered by carbon dioxide-based binary mixture for warm climatic conditions. Aspen Plus computes entropies and enthalpies by calculating the integral of residual functions [35]

Energy and Exergy Model
Exergetic Analysis
Energetic Analysis
Air Condenser Modeling
Plant-Specific Cost
Levelized Cost of Electricity
Exergo-Environmental Analysis
Exergo-Environmental Impact Factor
Exergo-Environmental Impact Coefficient
Exergo-Environmental Impact Index
Exergo-Environmental Impact Improvement
Exergetic Stability Factor
CO2 Emissions Savings
Results and Discussion
Exergetic efficiency exergy destruction ratio
SRC and
Tables andand
Conclusions
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