Adoption of the CO2 + SO2 mixture as working fluid for transcritical cycles: A thermodynamic assessment with optimized equation of state
Energy Conversion and Management, 2022
This paper focuses on the use of the CO 2 + SO 2 binary mixture as innovative working fluid for c... more This paper focuses on the use of the CO 2 + SO 2 binary mixture as innovative working fluid for closed transcritical power cycles with a minimum temperature above 50 • C. Starting from a literature review of the available experimental data on the mixture, the PC-SAFT EoS is identified as a suitable model to characterize the mixture behavior. Once the proper thermodynamic model is selected for this mixture, a comparison between the innovative transcritical cycle and the sCO 2 cycle is proposed for various plant layouts in order to find out the advantages of the innovative mixture. The analysis is presented fixing the cycle maximum temperature at 700 • C and the maximum pressure at 250 bar: the results depict an increment in cycle electric efficiency and cycle specific work, along with a lower temperature of heat introduction in the cycle for any considered configuration of transcritical CO 2 + SO 2 cycle, when compared to pure sCO 2. An economic analysis of the power block is then performed to support the selection of the innovative working fluid. Two of the most promising plant layouts are evidenced: the recompression layout is selected for highly efficient power blocks, while the dual recuperated layout works effectively in applications characterized by higher hot source exploitation. The recompression layout adopting the CO 2 + SO 2 mixture presents a power block electric efficiency of 48.67% (2.33% higher than the respective sCO 2 cycle) and a reduction of the power block CAPEX from 1160 $/kW el to 1000 $/kW el when compared to the sCO2 configuration for a 100MW el size, while the dual recuperated layout exploiting the CO 2 + SO 2 mixture shows a power block electric efficiency of 39.58% (0.69% above the same sCO 2 cycle
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Papers by Abubakr Ayub
innovative fluid which can be even mixtures of fluids. The first step consists of the working fluid characterization
in terms of thermodynamic properties through equations of state. The equations of state have to be calibrated on
experimental Vapour-Liquid Equilibrium measurements while, in the second step, the maximum operating
temperature is identified through thermal stability tests. Finally, the impact of the fluid thermodynamic prop-erties on the performance of the power cycle in which it is implemented must be assessed through modelling
tools. In this work, the procedure is discussed for the mixture of CO2and C6F14as a potential working fluid for
gas thermodynamic cycles with liquid phase compression. Results of the application of this mixture in a closed
cycle show the benefit of using a CO2/C6F14mixture which provides 3% points efficiency increase at 400 °C with
respect to the pure CO2together with a preliminary design of the expander.