Open Access
| Issue |
E3S Web Conf.
Volume 267, 2021
7th International Conference on Energy Science and Chemical Engineering (ICESCE 2021)
|
|
|---|---|---|
| Article Number | 02052 | |
| Number of page(s) | 4 | |
| Section | Environmental Chemistry Research and Chemical Preparation Process | |
| DOI | https://doi.org/10.1051/e3sconf/202126702052 | |
| Published online | 04 June 2021 | |
- Deng, R., et al., Vapor – liquid equilibrium measurements and assessments of fluoroethane + N,N-dimethylformamide and fluoroethane + dimethylether diethylene glycol systems for the hybrid refrigeration cycle. International Journal of Refrigeration, 2014. 43: p. 176–186. [Google Scholar]
- Li, X., et al., Vapor – liquid equilibria of difluoromethane+N, N-dimethylacetamide, difluoromethane+dimethylether diethylene glycol and 1,1-difluoroethane+dimethylether diethylene glycol systems. Fluid Phase Equilibria, 2013. 347: p. 15–21. [Google Scholar]
- Jing, X., R. Deng and D. Zheng, Measurement and Correlation of Isothermal Vapor – Liquid Equilibrium of Fluoroethane +N, NDimethylacetamide, Fluoroethane +N-Methyl-2-pyrrolidone, and 1,1,1,2-Tetrafluoroethane +N, NDimethylacetamide Systems. Journal of Chemical & Engineering Data, 2013. 58(11): p. 3289–3296. [Google Scholar]
- Wu, W., et al., Comparative analysis of conventional and low-GWP refrigerants with ionic liquid used for compression-assisted absorption cooling cycles. Applied Thermal Engineering, 2020. 172: p. 115145. [Google Scholar]
- Fang, Y., et al., Isothermal Vapor–Liquid Equilibria of the Absorption Working Pairs (R1234yf + NMP, R1234yf + DMETrEG) at Temperatures from 293.15 K to 353.15 K. Journal of Chemical & Engineering Data, 2018. 63(5): p. 1212–1219. [Google Scholar]
- Zhang, X., et al., Vapor-liquid equilibrium measurements and assessments of Low-GWP absorption working pairs (R32+DMETEG, R152a+DMETEG, and R161+DMETEG) for absorption refrigeration systems. Energy, 2021. 224: p. 120082. [Google Scholar]
- Feng, L., et al., Measurement and Correlation of Isothermal Vapor − Liquid Equilibrium of Fluoroethane + Dimethyl Ether Triethylene Glycol, 1,1-Difluoroethane + Dimethyl Ether Triethylene Glycol, and 1,1-Difluoroethane + N ‑ Methyl-2-pyrrolidone Systems. 2016. [Google Scholar]
- Han, X., et al., Isothermal Vapor – Liquid Equilibrium of HFC-161 + DMETrEG within the Temperature Range of 293.15 – 353.15 K and Comparison for HFC-161 Combined with Different Absorbents. Journal of Chemical & Engineering Data, 2016. 61(3): p. 1321–1327. [Google Scholar]
- Kleiber, M. and J.K. Axmann, Evolutionary algorithms for the optimization of Modified UNIFAC parameters. Computers and Chemical Engineering, 1998. 23(1): p. 63–82. [Google Scholar]
- Kleiber, M., An extension to the UNIFAC group assignment for prediction of vapor-liquid equilibria of mixtures containing refrigerants. Fluid Phase Equilibria, 1995. 107(2): p. 161–188. [Google Scholar]
- Gmehling, J., J. Li and M. Schiller, A modified UNIFAC model. 2. Present parameter matrix and results for different thermodynamic properties. Industrial & Engineering Chemistry Research, 1993. 32(1): p. 178–193. [Google Scholar]
Current usage metrics show cumulative count of Article Views (full-text article views including HTML views, PDF and ePub downloads, according to the available data) and Abstracts Views on Vision4Press platform.
Data correspond to usage on the plateform after 2015. The current usage metrics is available 48-96 hours after online publication and is updated daily on week days.
Initial download of the metrics may take a while.