Experimental and analytical procedure for the characterization of innovative working fluids for power plants applications. (September 2020)

• Record Type: Journal Article
• Authors: Di Marcoberardino, G.; Invernizzi, C.M.; Iora, P.; Ayub, A.; Di Bona, D.; Chiesa, P.; Binotti, M.; Manzolini, G.
• Is Part Of: Applied thermal engineering. Volume 178(2020)
• Publication Date: 2020-09
• Subjects: Power cycle definition -- Equation of state -- Thermal Stability -- Vapour liquid equilibrium -- Thermodynamic characterization; Heat engineering -- Periodicals; Heating -- Equipment and supplies -- Periodicals; Periodicals; 621.40205
• DOI: 10.1016/j.applthermaleng.2020.115513
• Languages: English
• ISSNs: 1359-4311

Abstract

Highlights: A comprehensive procedure for innovative fluid identification is proposed. Thermodynamic properties must be assessed through Equation of state. Equation of State must be calibrated with VLE experiments for innovative fluids. Maximum operating fluid temperature is identified through thermal stability tests. Abstract: In the last years, several fluids have been proposed to replace steam as working fluid in power cycle for converting thermal power into electricity. This paper describes the procedure to be adopted for the selection of any 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 properties 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 CO2 and C6 F14 as 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 /C6 F14 mixture which provides 3% points efficiency increase at 400 °C with respect to the pure CO2 together with a preliminary design of the expander.