Mixture of salophen + Tetrahydrofuran

Datasets

1. ρ_l - Mass density, kg/m3

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 85.9 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Molality, mol/kg of salophen (1) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0103	893.79
288.15	0.0316	895.65
288.15	0.0496	897.21
288.15	0.0699	898.95
288.15	0.0908	900.71
288.15	0.1099	902.31
288.15	0.1293	903.88
288.15	0.1498	905.55
288.15	0.1704	907.21
288.15	0.0103	882.94
288.15	0.0316	884.82
288.15	0.0496	886.39
288.15	0.0699	888.13
288.15	0.0908	889.9
288.15	0.1099	891.51
288.15	0.1293	893.11
288.15	0.1498	894.79
288.15	0.1704	896.46
308.15	0.0103	871.92
308.15	0.0316	873.82
308.15	0.0496	875.41
308.15	0.0699	877.17
308.15	0.0908	878.97
308.15	0.1099	880.59
308.15	0.1293	882.21
308.15	0.1498	883.9
308.15	0.1704	885.6
318.15	0.0103	860.78
318.15	0.0316	862.7
318.15	0.0496	864.3
318.15	0.0699	866.08
318.15	0.0908	867.89
318.15	0.1099	869.54
318.15	0.1293	871.17
318.15	0.1498	872.89
318.15	0.1704	874.58

Sources

• Effect of solvent on the volumetric behavior ofN,N' -salicylidenephenyl diamine (Salophen) Schiff base at differenttemperatures (288.15 - 318.15) K