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Graphical Analysis and 3D Thermodynamic Cycle Construction for Variable-Composition Ejector Refrigeration Cycle

Anxiang Shen1, Xinxin Ren2, Tao Wang1, Jianqiu Zhou1,2,*

1 School of Mechanical and Power Engineering, Nanjing Tech University, No. 30 Puzhu Road(S), Nanjing, China
2 School of Energy Science and Engineering, Nanjing Tech University, No. 30 Puzhu Road(S), Nanjing, China

* Corresponding Author: Jianqiu Zhou. Email: email

(This article belongs to the Special Issue: High Efficiency Cooling Technology in New and Renewable Energy System)

Frontiers in Heat and Mass Transfer 2026, 24(4), 14 https://doi.org/10.32604/fhmt.2026.082573

Abstract

To address the growing number of variable-composition ejector refrigeration cycles, this study proposes analyzing the matching performance between working fluids and cycles through 3D (Temperature-Entropy-Mass fraction) Thermodynamic Diagrams. The ejector refrigeration cycle is decoupled into a driving module and a refrigeration module, and a theoretical upper-bound model (COPlimiting) that depends only on working-fluid properties is derived from the T-s diagram. Graph-theoretic analysis yields an explicit relation between COPlimiting and fluid-specific parameters such as Δsb-bsa-b and Δse-e/Δsd-e. Definition of k1T47se-e) and k2T34sb-b) reveals that wet fluids favour the refrigeration module, whereas dry fluids favour the driving module. The influence of different mixtures has been also analyzed. The mixture of R227ea/R152a, R245fa/R134a, and Isobutane/pentane achieved their maximum COPlimiting values at x = 0.5, 0.4, and 0.2, respectively. These optimal compositions all falling within the high-slope region of k2. Additional parameters (x, tg, tc) are evaluated: At MFt = 0.5, increasing x from 0.1 to 0.2 raises the limiting cycle COP from 0.08 to 0.18 and elevates te from −79.24°C to −35.15°C. Raising tg from 85°C to 95°C lowers the limiting cycle COP from 0.1269 to 0.1235 while lifting te from −56.00°C to −49.18°C. Increasing tc from 30°C to 40°C boosts the limiting cycle COP from 0.1216 to 0.1285 and raises te from −60.84°C to −44.26°C.

Keywords

Ejector refrigeration cycle; limiting cycle; zeotropic mixture; graph theory

Cite This Article

APA Style
Shen, A., Ren, X., Wang, T., Zhou, J. (2026). Graphical Analysis and 3D Thermodynamic Cycle Construction for Variable-Composition Ejector Refrigeration Cycle. Frontiers in Heat and Mass Transfer, 24(4), 14. https://doi.org/10.32604/fhmt.2026.082573
Vancouver Style
Shen A, Ren X, Wang T, Zhou J. Graphical Analysis and 3D Thermodynamic Cycle Construction for Variable-Composition Ejector Refrigeration Cycle. Front Heat Mass Transf. 2026;24(4):14. https://doi.org/10.32604/fhmt.2026.082573
IEEE Style
A. Shen, X. Ren, T. Wang, and J. Zhou, “Graphical Analysis and 3D Thermodynamic Cycle Construction for Variable-Composition Ejector Refrigeration Cycle,” Front. Heat Mass Transf., vol. 24, no. 4, pp. 14, 2026. https://doi.org/10.32604/fhmt.2026.082573



cc Copyright © 2026 The Author(s). Published by Tech Science Press.
This work is licensed under a Creative Commons Attribution 4.0 International License , which permits unrestricted use, distribution, and reproduction in any medium, provided the original work is properly cited.
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