Mixture of 1-Butanamine, N-butyl- + Diethylene glycol hexyl ether

Datasets

1. ρ_l - Mass density, kg/m3 (2)
2. c_sound,fluid - Speed of Sound, m/s (2)

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of Diethylene glycol hexyl ether (2) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.0974	288.15	787.886
0.0974	293.15	783.751
0.0974	298.15	779.614
0.0974	303.15	775.187
0.0974	308.15	771.079
0.1441	288.15	798.114
0.1441	293.15	793.988
0.1441	298.15	789.859
0.1441	303.15	785.667
0.1441	308.15	781.545
0.1908	288.15	808.103
0.1908	293.15	804.0
0.1908	298.15	799.885
0.1908	303.15	795.785
0.1908	308.15	791.662
0.2530	288.15	820.984
0.2530	293.15	816.934
0.2530	298.15	812.825
0.2530	303.15	808.731
0.2530	308.15	804.6
0.2986	288.15	830.092
0.2986	293.15	826.059
0.2986	298.15	821.948
0.2986	303.15	817.838
0.2986	308.15	813.671
0.3606	288.15	842.0
0.3606	293.15	837.97
0.3606	298.15	833.834
0.3606	303.15	829.692
0.3606	308.15	825.52
0.4018	288.15	849.578
0.4018	293.15	845.585
0.4018	298.15	841.423
0.4018	303.15	837.274
0.4018	308.15	833.078
0.4584	288.15	859.635
0.4584	293.15	855.602
0.4584	298.15	851.46
0.4584	303.15	847.291
0.4584	308.15	843.095
0.5091	288.15	868.247
0.5091	293.15	864.218
0.5091	298.15	860.074
0.5091	303.15	855.914
0.5091	308.15	851.724
0.5435	288.15	873.936
0.5435	293.15	869.891
0.5435	298.15	865.751
0.5435	303.15	861.602
0.5435	308.15	857.401
0.5870	288.15	880.891
0.5870	293.15	876.847
0.5870	298.15	872.72
0.5870	303.15	868.58
0.5870	308.15	864.406
0.6097	288.15	884.459
0.6097	293.15	880.409
0.6097	298.15	876.278
0.6097	303.15	872.165
0.6097	308.15	867.972
0.6572	288.15	891.716
0.6572	293.15	887.648
0.6572	298.15	883.547
0.6572	303.15	879.461
0.6572	308.15	875.302
0.7023	288.15	898.412
0.7023	293.15	894.343
0.7023	298.15	890.259
0.7023	303.15	886.201
0.7023	308.15	882.052
0.7451	288.15	904.586
0.7451	293.15	900.53
0.7451	298.15	896.459
0.7451	303.15	892.397
0.7451	308.15	888.281
0.8144	288.15	914.195
0.8144	293.15	910.151
0.8144	298.15	906.103
0.8144	303.15	902.062
0.8144	308.15	897.98
0.8675	288.15	921.188
0.8675	293.15	917.168
0.8675	298.15	913.137
0.8675	303.15	909.095
0.8675	308.15	905.045
0.9083	288.15	926.329
0.9083	293.15	922.317
0.9083	298.15	918.3
0.9083	303.15	914.27
0.9083	308.15	910.231
0.9414	288.15	930.322
0.9414	293.15	926.329
0.9414	298.15	922.323
0.9414	303.15	918.281
0.9414	308.15	914.269

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of Diethylene glycol hexyl ether (2) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.0974	288.15	787.886
0.0974	293.15	783.751
0.0974	298.15	779.614
0.0974	303.15	775.187
0.0974	308.15	771.079
0.1441	288.15	798.114
0.1441	293.15	793.988
0.1441	298.15	789.859
0.1441	303.15	785.667
0.1441	308.15	781.545
0.1908	288.15	808.103
0.1908	293.15	804.0
0.1908	298.15	799.885
0.1908	303.15	795.785
0.1908	308.15	791.662
0.2530	288.15	820.984
0.2530	293.15	816.934
0.2530	298.15	812.825
0.2530	303.15	808.731
0.2530	308.15	804.6
0.2986	288.15	830.092
0.2986	293.15	826.059
0.2986	298.15	821.948
0.2986	303.15	817.838
0.2986	308.15	813.671
0.3606	288.15	842.0
0.3606	293.15	837.97
0.3606	298.15	833.834
0.3606	303.15	829.692
0.3606	308.15	825.52
0.4018	288.15	849.578
0.4018	293.15	845.585
0.4018	298.15	841.423
0.4018	303.15	837.274
0.4018	308.15	833.078
0.4584	288.15	859.635
0.4584	293.15	855.602
0.4584	298.15	851.46
0.4584	303.15	847.291
0.4584	308.15	843.095
0.5091	288.15	868.247
0.5091	293.15	864.218
0.5091	298.15	860.074
0.5091	303.15	855.914
0.5091	308.15	851.724
0.5435	288.15	873.936
0.5435	293.15	869.891
0.5435	298.15	865.751
0.5435	303.15	861.602
0.5435	308.15	857.401
0.5870	288.15	880.891
0.5870	293.15	876.847
0.5870	298.15	872.72
0.5870	303.15	868.58
0.5870	308.15	864.406
0.6097	288.15	884.459
0.6097	293.15	880.409
0.6097	298.15	876.278
0.6097	303.15	872.165
0.6097	308.15	867.972
0.6572	288.15	891.716
0.6572	293.15	887.648
0.6572	298.15	883.547
0.6572	303.15	879.461
0.6572	308.15	875.302
0.7023	288.15	898.412
0.7023	293.15	894.343
0.7023	298.15	890.259
0.7023	303.15	886.201
0.7023	308.15	882.052
0.7451	288.15	904.586
0.7451	293.15	900.53
0.7451	298.15	896.459
0.7451	303.15	892.397
0.7451	308.15	888.281
0.8144	288.15	914.195
0.8144	293.15	910.151
0.8144	298.15	906.103
0.8144	303.15	902.062
0.8144	308.15	897.98
0.8675	288.15	921.188
0.8675	293.15	917.168
0.8675	298.15	913.137
0.8675	303.15	909.095
0.8675	308.15	905.045
0.9083	288.15	926.329
0.9083	293.15	922.317
0.9083	298.15	918.3
0.9083	303.15	914.27
0.9083	308.15	910.231
0.9414	288.15	930.322
0.9414	293.15	926.329
0.9414	298.15	922.323
0.9414	303.15	918.281
0.9414	308.15	914.269

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of Diethylene glycol hexyl ether (2) - Liquid	Temperature, K - Liquid	Speed of sound, m/s - Liquid
0.0974	288.15	1301.44
0.0974	293.15	1282.29
0.0974	298.15	1262.9
0.0974	303.15	1243.68
0.0974	308.15	1225.28
0.1441	288.15	1308.12
0.1441	293.15	1289.17
0.1441	298.15	1270.55
0.1441	303.15	1250.97
0.1441	308.15	1232.23
0.1908	288.15	1314.8
0.1908	293.15	1295.95
0.1908	298.15	1277.82
0.1908	303.15	1258.2
0.1908	308.15	1239.18
0.2530	288.15	1323.47
0.2530	293.15	1304.81
0.2530	298.15	1287.05
0.2530	303.15	1267.67
0.2530	308.15	1248.65
0.2986	288.15	1329.78
0.2986	293.15	1311.25
0.2986	298.15	1293.6
0.2986	303.15	1274.45
0.2986	308.15	1255.53
0.3606	288.15	1338.03
0.3606	293.15	1319.71
0.3606	298.15	1302.12
0.3606	303.15	1283.44
0.3606	308.15	1264.84
0.4018	288.15	1343.36
0.4018	293.15	1325.25
0.4018	298.15	1307.6
0.4018	303.15	1289.3
0.4018	308.15	1270.93
0.4584	288.15	1350.4
0.4584	293.15	1332.64
0.4584	298.15	1314.96
0.4584	303.15	1297.05
0.4584	308.15	1279.08
0.5091	288.15	1356.69
0.5091	293.15	1339.01
0.5091	298.15	1321.35
0.5091	303.15	1303.79
0.5091	308.15	1286.18
0.5435	288.15	1360.77
0.5435	293.15	1343.21
0.5435	298.15	1325.65
0.5435	303.15	1308.19
0.5435	308.15	1290.82
0.5870	288.15	1365.8
0.5870	293.15	1348.42
0.5870	298.15	1330.88
0.5870	303.15	1313.63
0.5870	308.15	1296.48
0.6097	288.15	1368.36
0.6097	293.15	1351.05
0.6097	298.15	1333.56
0.6097	303.15	1316.39
0.6097	308.15	1299.36
0.6572	288.15	1373.58
0.6572	293.15	1356.39
0.6572	298.15	1339.05
0.6572	303.15	1321.98
0.6572	308.15	1305.05
0.7023	288.15	1378.35
0.7023	293.15	1361.27
0.7023	298.15	1344.12
0.7023	303.15	1327.0
0.7023	308.15	1310.12
0.7451	288.15	1382.71
0.7451	293.15	1365.7
0.7451	298.15	1348.64
0.7451	303.15	1331.58
0.7451	308.15	1314.55
0.8144	288.15	1389.39
0.8144	293.15	1372.42
0.8144	298.15	1355.55
0.8144	303.15	1338.46
0.8144	308.15	1320.88
0.8675	288.15	1394.19
0.8675	293.15	1377.16
0.8675	298.15	1360.35
0.8675	303.15	1343.32
0.8675	308.15	1325.02
0.9083	288.15	1397.68
0.9083	293.15	1380.58
0.9083	298.15	1363.7
0.9083	303.15	1346.75
0.9083	308.15	1327.65
0.9414	288.15	1400.38
0.9414	293.15	1383.16
0.9414	298.15	1366.18
0.9414	303.15	1349.33
0.9414	308.15	1329.46

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of Diethylene glycol hexyl ether (2) - Liquid	Temperature, K - Liquid	Speed of sound, m/s - Liquid
0.0974	288.15	1301.44
0.0974	293.15	1282.29
0.0974	298.15	1262.9
0.0974	303.15	1243.68
0.0974	308.15	1225.28
0.1441	288.15	1308.12
0.1441	293.15	1289.17
0.1441	298.15	1270.55
0.1441	303.15	1250.97
0.1441	308.15	1232.23
0.1908	288.15	1314.8
0.1908	293.15	1295.95
0.1908	298.15	1277.82
0.1908	303.15	1258.2
0.1908	308.15	1239.18
0.2530	288.15	1323.47
0.2530	293.15	1304.81
0.2530	298.15	1287.05
0.2530	303.15	1267.67
0.2530	308.15	1248.65
0.2986	288.15	1329.78
0.2986	293.15	1311.25
0.2986	298.15	1293.6
0.2986	303.15	1274.45
0.2986	308.15	1255.53
0.3606	288.15	1338.03
0.3606	293.15	1319.71
0.3606	298.15	1302.12
0.3606	303.15	1283.44
0.3606	308.15	1264.84
0.4018	288.15	1343.36
0.4018	293.15	1325.25
0.4018	298.15	1307.6
0.4018	303.15	1289.3
0.4018	308.15	1270.93
0.4584	288.15	1350.4
0.4584	293.15	1332.64
0.4584	298.15	1314.96
0.4584	303.15	1297.05
0.4584	308.15	1279.08
0.5091	288.15	1356.69
0.5091	293.15	1339.01
0.5091	298.15	1321.35
0.5091	303.15	1303.79
0.5091	308.15	1286.18
0.5435	288.15	1360.77
0.5435	293.15	1343.21
0.5435	298.15	1325.65
0.5435	303.15	1308.19
0.5435	308.15	1290.82
0.5870	288.15	1365.8
0.5870	293.15	1348.42
0.5870	298.15	1330.88
0.5870	303.15	1313.63
0.5870	308.15	1296.48
0.6097	288.15	1368.36
0.6097	293.15	1351.05
0.6097	298.15	1333.56
0.6097	303.15	1316.39
0.6097	308.15	1299.36
0.6572	288.15	1373.58
0.6572	293.15	1356.39
0.6572	298.15	1339.05
0.6572	303.15	1321.98
0.6572	308.15	1305.05
0.7023	288.15	1378.35
0.7023	293.15	1361.27
0.7023	298.15	1344.12
0.7023	303.15	1327.0
0.7023	308.15	1310.12
0.7451	288.15	1382.71
0.7451	293.15	1365.7
0.7451	298.15	1348.64
0.7451	303.15	1331.58
0.7451	308.15	1314.55
0.8144	288.15	1389.39
0.8144	293.15	1372.42
0.8144	298.15	1355.55
0.8144	303.15	1338.46
0.8144	308.15	1320.88
0.8675	288.15	1394.19
0.8675	293.15	1377.16
0.8675	298.15	1360.35
0.8675	303.15	1343.32
0.8675	308.15	1325.02
0.9083	288.15	1397.68
0.9083	293.15	1380.58
0.9083	298.15	1363.7
0.9083	303.15	1346.75
0.9083	308.15	1327.65
0.9414	288.15	1400.38
0.9414	293.15	1383.16
0.9414	298.15	1366.18
0.9414	303.15	1349.33
0.9414	308.15	1329.46

Sources

• Densities, Excess Molar Volumes, Speeds of Sound, and Isothermal Compressibilities for 2-(2-Hexyloxyethoxy)ethanol + n-Alkylamine at Temperatures Between 288.15 K and 308.15 K