Evaluating Cubic Equations of State with Various α Functions for Viscosity Predictions of 124 Industrial Important Fluids Based on Residual Entropy Scaling. [PDF]
Xiao X, Yang X.
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Air Humidity Influence on Combustion of R-1234yf (CF<sub>3</sub>CFCH<sub>2</sub>), R-1234ze(E) (trans-CF<sub>3</sub>CHCHF) and R-134a (CH<sub>2</sub>FCF<sub>3</sub>) Refrigerants. [PDF]
Babushok VI, Linteris GT.
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Sealed Gravitational Capillary Viscometry of Dimethyl Ether and Two Next-Generation Alternative Refrigerants. [PDF]
Cousins DS, Laesecke A.
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R134a e R1234ze: differenze prestazionali tra due fluidi frigoriferi in un evaporatore
In questo elaborato si vuole discutere la differenza di un evaporatore che opera utilizzando due fluidi frigoriferi diversi. I fluidi trattati sono R134a e R1234ze. Sono stati prima acquisiti i dati da un banco prova, quindi le misure di pressione in ingresso e uscita dall’evaporatore e dal condensatore. Successivamente, attraverso il software CRE 1.0,
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Surface tension of low GWP refrigerants R1243zf, R1234ze(Z), and R1233zd(E)
The surface tension of R1243zf, R1234ze(Z), and R1233zd(E) were measured at temperatures from 270 K to 360 K by an experimental apparatus based on the differential capillary rise method. The deviation between the measured surface tension of R134a and R245fa and the calculated surface tension with REFPROP 9.1 (Lemmon et al., 2013) was ±0.13 mN m?1 ...
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The analysis of waste heat recovery in steel enterprises' data centers based on the Co-ah cycle. [PDF]
Wen K, Zhou C, Wang X.
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Si analizzano le prestazioni dell'impianto frigorifero di piccole dimensioni preposto al raffreddamento di componenti elettronici a bordo di ...
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Heat Pumps in CHP Systems:High-efficiency Energy System Utilising Combined Heat and Power and Heat Pumps [PDF]
Ommen, Torben Schmidt
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Cost and environmental analysis and optimization of a new and green three-level waste heat recovery-based cogeneration cycle: A comparative study. [PDF]
Nikafshan Rad H, Ghasemi A, Marefati M.
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