Zobrazeno 1 - 10
of 34
pro vyhledávání: '"Fufang Yang"'
Autor:
Fufang Yang, Shirazi, Abtin Raeispour, Roa Pinto, Juan Sebastian, Kontogeorgis, Georgios M., Ferrando, Nicolas, Galindo, Amparo, de Hemptinne, Jean-Charles
Publikováno v:
Industrial & Engineering Chemistry Research; 7/24/2024, Vol. 63 Issue 29, p12999-13015, 17p
Autor:
J. Ilja Siepmann, Elizabeth G. Rasmussen, Riccardo M. Swanepoel, Ardila H. Tiwikrama, Pedro Velho, Fufang Yang
Publikováno v:
Journal of Chemical & Engineering Data. 68:1-3
Publikováno v:
Industrial and engineering chemistry research
Industrial and engineering chemistry research, 2022, 61 (42), pp.15576-15593. ⟨10.1021/acs.iecr.2c00059⟩
Ind. Eng. Chem-Res.
Industrial and engineering chemistry research, 2022, 61 (42), pp.15576-15593. ⟨10.1021/acs.iecr.2c00059⟩
Ind. Eng. Chem-Res.
International audience; Modeling of thermodynamic properties of mixed-solvent electrolyte solutions is challenging. Reliable experimental data are essential for any model development and parametrization. In this work, a benchmark database for (water
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::adc40d2023131eef3ba5c8becdfdf500
https://hal-ifp.archives-ouvertes.fr/hal-03941779
https://hal-ifp.archives-ouvertes.fr/hal-03941779
Autor:
Fufang Yang, Tri Dat Ngo, Juan Sebastian Roa Pinto, Georgios M. Kontogeorgis, Jean-Charles de Hemptinne
Publikováno v:
Fluid Phase Equilibria
Fluid Phase Equilibria, 2023, 570, pp.113778. ⟨10.1016/j.fluid.2023.113778⟩
Fluid Phase Equilibria, 2023, 570, pp.113778. ⟨10.1016/j.fluid.2023.113778⟩
International audience; This work presents an analysis of various electrolyte SAFT model approaches through a rigorous benchmarking on extensively collected and critically evaluated databases. The primitive mean spherical approximation (MSA) and the
Publikováno v:
Yang, X, Yang, F & Yang, F 2023, ' Thermo-economic performance limit analysis of combined heat and power systems for optimal working fluid selections ', Energy, vol. 272, 127041 . https://doi.org/10.1016/j.energy.2023.127041
In previous works, we have proposed the thermodynamic performance limit analysis methodology for the organic Rankine cycle for analyzing the impact of working fluid properties on system performance. Here the concept is extended to the thermo-economic
Publikováno v:
Science China Technological Sciences. 64:1624-1640
In this paper, an exploration of the practical thermodynamic performance limits of the organic Rankine cycle (ORC) under working fluid and cycle parameter restrictions is presented. These performance limits are more realistic benchmarks for the therm
Publikováno v:
Yang, F, Qu, J, Kontogeorgis, G M & de Hemptinne, J-C 2022, ' Reference Density Database for 20 Aqueous Alkali Halide Solutions ', Journal of Physical and Chemical Reference Data, vol. 51, no. 4, 043104 . https://doi.org/10.1063/5.0124173
Journal of Physical and Chemical Reference Data
Journal of Physical and Chemical Reference Data, 2022, 51 (4), pp.043104. ⟨10.1063/5.0124173⟩
Journal of Physical and Chemical Reference Data
Journal of Physical and Chemical Reference Data, 2022, 51 (4), pp.043104. ⟨10.1063/5.0124173⟩
A reference density database of aqueous alkali halide solutions is presented. The solutes are the 20 alkali halides consisting of the cations Li+, Na+, K+, Rb+, Cs+, and anions F−, Cl−, Br−, I−. Experimental density data of these aqueous elec
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::7a513d4f554021dc90721bd5f1aea705
https://orbit.dtu.dk/en/publications/77474df1-5847-42e9-87a2-ade459645151
https://orbit.dtu.dk/en/publications/77474df1-5847-42e9-87a2-ade459645151
Publikováno v:
Chinese Science Bulletin. 64:2741-2750
Publikováno v:
Fluid Phase Equilibria. 494:161-171
The multiparameter equation of state represents experimental data in wide ranges of temperature and density with superb accuracy. However, at the critical point, all classical models fail in describing the asymptotic behavior of thermodynamic propert
Publikováno v:
Journal of Chemical & Engineering Data. 64:2947-2954
In this work, 95 data points for the vapor pressure of trans-1-chloro-3,3,3-trifluoroprop-1-ene (HCFO-1233zd(E)) were measured over the temperature range of 253–431 K and the pressure range of 17–3091 kPa using a Burnett apparatus. The effect of