Mixture of Ethanol, 2-butoxy- + Methane, nitro-

Datasets

1. η - Viscosity, Pa*s (2)
2. ρ_l - Mass density, kg/m3 (2)
3. c_sound,fluid - Speed of Sound, m/s (2)
4. Excess molar volume, m3/mol (2)

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Methane, nitro- (2) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0000	0.0032
293.15	0.0557	0.0030
293.15	0.1060	0.0028
293.15	0.1974	0.0025
293.15	0.3083	0.0020
293.15	0.4014	0.0017
293.15	0.4487	0.0016
293.15	0.4997	0.0014
293.15	0.5492	0.0013
293.15	0.5947	0.0012
293.15	0.6990	0.0010
293.15	0.8012	0.0008
293.15	0.8981	0.0007
293.15	0.9475	0.0007
293.15	1.0000	0.0006
298.45	0.0000	0.0028
298.45	0.0506	0.0027
298.45	0.1012	0.0025
298.45	0.2015	0.0022
298.45	0.2997	0.0019
298.45	0.4047	0.0016
298.45	0.4498	0.0015
298.45	0.5008	0.0013
298.45	0.5481	0.0012
298.45	0.5976	0.0011
298.45	0.6984	0.0009
298.45	0.7981	0.0008
298.45	0.8986	0.0007
298.45	0.9394	0.0007
298.45	1.0000	0.0006
303.15	0.0000	0.0024
303.15	0.0522	0.0023
303.15	0.1004	0.0022
303.15	0.2155	0.0019
303.15	0.2990	0.0016
303.15	0.3996	0.0014
303.15	0.4495	0.0013
303.15	0.5002	0.0012
303.15	0.5482	0.0011
303.15	0.5993	0.0010
303.15	0.6998	0.0009
303.15	0.7994	0.0007
303.15	0.9005	0.0006
303.15	0.9436	0.0006
303.15	1.0000	0.0006
308.15	0.0000	0.0021
308.15	0.0501	0.0020
308.15	0.1048	0.0018
308.15	0.1980	0.0016
308.15	0.3012	0.0014
308.15	0.3999	0.0012
308.15	0.4502	0.0012
308.15	0.4998	0.0011
308.15	0.5499	0.0010
308.15	0.5998	0.0009
308.15	0.6994	0.0008
308.15	0.7997	0.0007
308.15	0.8986	0.0006
308.15	0.9465	0.0006
308.15	1.0000	0.0006
313.15	0.0000	0.0017
313.15	0.0511	0.0016
313.15	0.1135	0.0015
313.15	0.2156	0.0013
313.15	0.2993	0.0012
313.15	0.3971	0.0010
313.15	0.4497	0.0010
313.15	0.4973	0.0009
313.15	0.5458	0.0009
313.15	0.5989	0.0008
313.15	0.6958	0.0007
313.15	0.8004	0.0006
313.15	0.8930	0.0006
313.15	0.9491	0.0006
313.15	1.0000	0.0005

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Methane, nitro- (2) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0000	0.0032
293.15	0.0557	0.0030
293.15	0.1060	0.0028
293.15	0.1974	0.0025
293.15	0.3083	0.0020
293.15	0.4014	0.0017
293.15	0.4487	0.0016
293.15	0.4997	0.0014
293.15	0.5492	0.0013
293.15	0.5947	0.0012
293.15	0.6990	0.0010
293.15	0.8012	0.0008
293.15	0.8981	0.0007
293.15	0.9475	0.0007
293.15	1.0000	0.0006
298.45	0.0000	0.0028
298.45	0.0506	0.0027
298.45	0.1012	0.0025
298.45	0.2015	0.0022
298.45	0.2997	0.0019
298.45	0.4047	0.0016
298.45	0.4498	0.0015
298.45	0.5008	0.0013
298.45	0.5481	0.0012
298.45	0.5976	0.0011
298.45	0.6984	0.0009
298.45	0.7981	0.0008
298.45	0.8986	0.0007
298.45	0.9394	0.0007
298.45	1.0000	0.0006
303.15	0.0000	0.0024
303.15	0.0522	0.0023
303.15	0.1004	0.0022
303.15	0.2155	0.0019
303.15	0.2990	0.0016
303.15	0.3996	0.0014
303.15	0.4495	0.0013
303.15	0.5002	0.0012
303.15	0.5482	0.0011
303.15	0.5993	0.0010
303.15	0.6998	0.0009
303.15	0.7994	0.0007
303.15	0.9005	0.0006
303.15	0.9436	0.0006
303.15	1.0000	0.0006
308.15	0.0000	0.0021
308.15	0.0501	0.0020
308.15	0.1048	0.0018
308.15	0.1980	0.0016
308.15	0.3012	0.0014
308.15	0.3999	0.0012
308.15	0.4502	0.0012
308.15	0.4998	0.0011
308.15	0.5499	0.0010
308.15	0.5998	0.0009
308.15	0.6994	0.0008
308.15	0.7997	0.0007
308.15	0.8986	0.0006
308.15	0.9465	0.0006
308.15	1.0000	0.0006
313.15	0.0000	0.0017
313.15	0.0511	0.0016
313.15	0.1135	0.0015
313.15	0.2156	0.0013
313.15	0.2993	0.0012
313.15	0.3971	0.0010
313.15	0.4497	0.0010
313.15	0.4973	0.0009
313.15	0.5458	0.0009
313.15	0.5989	0.0008
313.15	0.6958	0.0007
313.15	0.8004	0.0006
313.15	0.8930	0.0006
313.15	0.9491	0.0006
313.15	1.0000	0.0005

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Methane, nitro- (2) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	901.19
293.15	0.0500	905.83
293.15	0.0999	910.77
293.15	0.2000	921.75
293.15	0.3000	934.29
293.15	0.4000	948.84
293.15	0.5000	966.21
293.15	0.6000	987.24
293.15	0.7000	1013.09
293.15	0.8002	1045.18
293.15	0.8999	1085.39
293.15	0.9503	1109.89
293.15	1.0000	1137.63
298.15	0.0000	896.29
298.15	0.0500	900.85
298.15	0.0999	905.68
298.15	0.2000	916.48
298.15	0.3000	928.9
298.15	0.4000	943.34
298.15	0.5000	960.53
298.15	0.6000	981.35
298.15	0.7000	1006.9
298.15	0.8002	1038.68
298.15	0.8999	1078.61
298.15	0.9503	1103.01
298.15	1.0000	1130.62
303.15	0.0000	892.35
303.15	0.0500	896.7
303.15	0.0999	901.4
303.15	0.2000	911.94
303.15	0.3000	924.13
303.15	0.4000	938.41
303.15	0.5000	955.38
303.15	0.6000	975.84
303.15	0.7000	1000.85
303.15	0.8002	1032.09
303.15	0.8999	1071.54
303.15	0.9503	1095.83
303.15	1.0000	1123.6
308.15	0.0000	887.83
308.15	0.0500	891.97
308.15	0.0999	896.44
308.15	0.2000	906.69
308.15	0.3000	918.65
308.15	0.4000	932.71
308.15	0.5000	949.47
308.15	0.6000	969.67
308.15	0.7000	994.45
308.15	0.8002	1025.45
308.15	0.8999	1064.77
308.15	0.9503	1089.08
308.15	1.0000	1116.86
313.15	0.0000	883.59
313.15	0.0500	887.43
313.15	0.0999	891.75
313.15	0.2000	901.79
313.15	0.3000	913.58
313.15	0.4000	927.46
313.15	0.5000	943.98
313.15	0.6000	963.96
313.15	0.7000	988.46
313.15	0.8002	1018.86
313.15	0.8999	1057.69
313.15	0.9503	1081.78
313.15	1.0000	1109.87

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Methane, nitro- (2) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	901.19
293.15	0.0500	905.83
293.15	0.0999	910.77
293.15	0.2000	921.75
293.15	0.3000	934.29
293.15	0.4000	948.84
293.15	0.5000	966.21
293.15	0.6000	987.24
293.15	0.7000	1013.09
293.15	0.8002	1045.18
293.15	0.8999	1085.39
293.15	0.9503	1109.89
293.15	1.0000	1137.63
298.15	0.0000	896.29
298.15	0.0500	900.85
298.15	0.0999	905.68
298.15	0.2000	916.48
298.15	0.3000	928.9
298.15	0.4000	943.34
298.15	0.5000	960.53
298.15	0.6000	981.35
298.15	0.7000	1006.9
298.15	0.8002	1038.68
298.15	0.8999	1078.61
298.15	0.9503	1103.01
298.15	1.0000	1130.62
303.15	0.0000	892.35
303.15	0.0500	896.7
303.15	0.0999	901.4
303.15	0.2000	911.94
303.15	0.3000	924.13
303.15	0.4000	938.41
303.15	0.5000	955.38
303.15	0.6000	975.84
303.15	0.7000	1000.85
303.15	0.8002	1032.09
303.15	0.8999	1071.54
303.15	0.9503	1095.83
303.15	1.0000	1123.6
308.15	0.0000	887.83
308.15	0.0500	891.97
308.15	0.0999	896.44
308.15	0.2000	906.69
308.15	0.3000	918.65
308.15	0.4000	932.71
308.15	0.5000	949.47
308.15	0.6000	969.67
308.15	0.7000	994.45
308.15	0.8002	1025.45
308.15	0.8999	1064.77
308.15	0.9503	1089.08
308.15	1.0000	1116.86
313.15	0.0000	883.59
313.15	0.0500	887.43
313.15	0.0999	891.75
313.15	0.2000	901.79
313.15	0.3000	913.58
313.15	0.4000	927.46
313.15	0.5000	943.98
313.15	0.6000	963.96
313.15	0.7000	988.46
313.15	0.8002	1018.86
313.15	0.8999	1057.69
313.15	0.9503	1081.78
313.15	1.0000	1109.87

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Methane, nitro- (2) - Liquid	Speed of sound, m/s - Liquid
293.15	0.0000	1323.9
293.15	0.0507	1322.4
293.15	0.1001	1321.8
293.15	0.2003	1318.8
293.15	0.3003	1316.1
293.15	0.4005	1313.7
293.15	0.5002	1312.0
293.15	0.6000	1311.8
293.15	0.7000	1313.7
293.15	0.7999	1318.2
293.15	0.8999	1326.4
293.15	0.9500	1332.4
293.15	1.0000	1340.2
298.15	0.0000	1306.8
298.15	0.0507	1305.6
298.15	0.1001	1304.5
298.15	0.2003	1302.2
298.15	0.3003	1299.6
298.15	0.4005	1297.2
298.15	0.5002	1295.5
298.15	0.6000	1295.2
298.15	0.7000	1296.8
298.15	0.7999	1300.9
298.15	0.8999	1308.5
298.15	0.9500	1313.8
298.15	1.0000	1320.4
303.15	0.0000	1290.6
303.15	0.0507	1289.5
303.15	0.1001	1288.6
303.15	0.2003	1286.3
303.15	0.3003	1283.6
303.15	0.4005	1281.1
303.15	0.5002	1279.2
303.15	0.6000	1278.5
303.15	0.7000	1279.5
303.15	0.7999	1282.9
303.15	0.8999	1288.9
303.15	0.9500	1293.2
303.15	1.0000	1298.1
308.15	0.0000	1273.5
308.15	0.0507	1273.1
308.15	0.1001	1272.2
308.15	0.2003	1270.2
308.15	0.3003	1267.9
308.15	0.4005	1265.9
308.15	0.5002	1264.2
308.15	0.6000	1263.4
308.15	0.7000	1264.3
308.15	0.7999	1267.3
308.15	0.8999	1273.2
308.15	0.9500	1276.9
308.15	1.0000	1281.2
313.15	0.0000	1257.7
313.15	0.0507	1257.4
313.15	0.1001	1256.8
313.15	0.2003	1254.9
313.15	0.3003	1252.7
313.15	0.4005	1250.6
313.15	0.5002	1248.8
313.15	0.6000	1248.0
313.15	0.7000	1248.7
313.15	0.7999	1251.4
313.15	0.8999	1256.3
313.15	0.9500	1259.5
313.15	1.0000	1262.8

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Methane, nitro- (2) - Liquid	Speed of sound, m/s - Liquid
293.15	0.0000	1323.9
293.15	0.0507	1322.4
293.15	0.1001	1321.8
293.15	0.2003	1318.8
293.15	0.3003	1316.1
293.15	0.4005	1313.7
293.15	0.5002	1312.0
293.15	0.6000	1311.8
293.15	0.7000	1313.7
293.15	0.7999	1318.2
293.15	0.8999	1326.4
293.15	0.9500	1332.4
293.15	1.0000	1340.2
298.15	0.0000	1306.8
298.15	0.0507	1305.6
298.15	0.1001	1304.5
298.15	0.2003	1302.2
298.15	0.3003	1299.6
298.15	0.4005	1297.2
298.15	0.5002	1295.5
298.15	0.6000	1295.2
298.15	0.7000	1296.8
298.15	0.7999	1300.9
298.15	0.8999	1308.5
298.15	0.9500	1313.8
298.15	1.0000	1320.4
303.15	0.0000	1290.6
303.15	0.0507	1289.5
303.15	0.1001	1288.6
303.15	0.2003	1286.3
303.15	0.3003	1283.6
303.15	0.4005	1281.1
303.15	0.5002	1279.2
303.15	0.6000	1278.5
303.15	0.7000	1279.5
303.15	0.7999	1282.9
303.15	0.8999	1288.9
303.15	0.9500	1293.2
303.15	1.0000	1298.1
308.15	0.0000	1273.5
308.15	0.0507	1273.1
308.15	0.1001	1272.2
308.15	0.2003	1270.2
308.15	0.3003	1267.9
308.15	0.4005	1265.9
308.15	0.5002	1264.2
308.15	0.6000	1263.4
308.15	0.7000	1264.3
308.15	0.7999	1267.3
308.15	0.8999	1273.2
308.15	0.9500	1276.9
308.15	1.0000	1281.2
313.15	0.0000	1257.7
313.15	0.0507	1257.4
313.15	0.1001	1256.8
313.15	0.2003	1254.9
313.15	0.3003	1252.7
313.15	0.4005	1250.6
313.15	0.5002	1248.8
313.15	0.6000	1248.0
313.15	0.7000	1248.7
313.15	0.7999	1251.4
313.15	0.8999	1256.3
313.15	0.9500	1259.5
313.15	1.0000	1262.8

Excess molar volume, m3/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Methane, nitro- (2) - Liquid	Excess molar volume, m3/mol - Liquid
566.30	0.0000	0.0000
566.30	0.0500	4.8000e-08
566.30	0.0999	9.4000e-08
566.30	0.2000	1.7300e-07
566.30	0.3000	2.5100e-07
566.30	0.4000	3.1900e-07
566.30	0.5000	3.4700e-07
566.30	0.6000	3.3200e-07
566.30	0.7000	2.7200e-07
566.30	0.8002	1.8800e-07
566.30	0.8999	9.6000e-08
566.30	0.9503	4.9000e-08
566.30	1.0000	0.0000
571.30	0.0000	0.0000
571.30	0.0500	5.4000e-08
571.30	0.0999	1.0900e-07
571.30	0.2000	1.9900e-07
571.30	0.3000	2.7700e-07
571.30	0.4000	3.4100e-07
571.30	0.5000	3.7000e-07
571.30	0.6000	3.5500e-07
571.30	0.7000	2.9800e-07
571.30	0.8002	2.1200e-07
571.30	0.8999	1.1200e-07
571.30	0.9503	5.6000e-08
571.30	1.0000	0.0000
576.30	0.0000	0.0000
576.30	0.0500	7.6000e-08
576.30	0.0999	1.4100e-07
576.30	0.2000	2.4500e-07
576.30	0.3000	3.2900e-07
576.30	0.4000	3.8800e-07
576.30	0.5000	4.1400e-07
576.30	0.6000	4.0300e-07
576.30	0.7000	3.5700e-07
576.30	0.8002	2.7200e-07
576.30	0.8999	1.5800e-07
576.30	0.9503	8.6000e-08
576.30	1.0000	0.0000
581.30	0.0000	0.0000
581.30	0.0500	1.0200e-07
581.30	0.0999	1.9200e-07
581.30	0.2000	3.1900e-07
581.30	0.3000	4.1100e-07
581.30	0.4000	4.7300e-07
581.30	0.5000	4.9600e-07
581.30	0.6000	4.8400e-07
581.30	0.7000	4.2800e-07
581.30	0.8002	3.2900e-07
581.30	0.8999	1.9200e-07
581.30	0.9503	1.0200e-07
581.30	1.0000	0.0000
586.30	0.0000	0.0000
586.30	0.0500	1.3900e-07
586.30	0.0999	2.4300e-07
586.30	0.2000	3.7800e-07
586.30	0.3000	4.7100e-07
586.30	0.4000	5.3100e-07
586.30	0.5000	5.5400e-07
586.30	0.6000	5.3400e-07
586.30	0.7000	4.7200e-07
586.30	0.8002	3.8300e-07
586.30	0.8999	2.3800e-07
586.30	0.9503	1.3900e-07
586.30	1.0000	0.0000

Excess molar volume, m3/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Methane, nitro- (2) - Liquid	Excess molar volume, m3/mol - Liquid
566.30	0.0000	0.0000
566.30	0.0500	4.8000e-08
566.30	0.0999	9.4000e-08
566.30	0.2000	1.7300e-07
566.30	0.3000	2.5100e-07
566.30	0.4000	3.1900e-07
566.30	0.5000	3.4700e-07
566.30	0.6000	3.3200e-07
566.30	0.7000	2.7200e-07
566.30	0.8002	1.8800e-07
566.30	0.8999	9.6000e-08
566.30	0.9503	4.9000e-08
566.30	1.0000	0.0000
571.30	0.0000	0.0000
571.30	0.0500	5.4000e-08
571.30	0.0999	1.0900e-07
571.30	0.2000	1.9900e-07
571.30	0.3000	2.7700e-07
571.30	0.4000	3.4100e-07
571.30	0.5000	3.7000e-07
571.30	0.6000	3.5500e-07
571.30	0.7000	2.9800e-07
571.30	0.8002	2.1200e-07
571.30	0.8999	1.1200e-07
571.30	0.9503	5.6000e-08
571.30	1.0000	0.0000
576.30	0.0000	0.0000
576.30	0.0500	7.6000e-08
576.30	0.0999	1.4100e-07
576.30	0.2000	2.4500e-07
576.30	0.3000	3.2900e-07
576.30	0.4000	3.8800e-07
576.30	0.5000	4.1400e-07
576.30	0.6000	4.0300e-07
576.30	0.7000	3.5700e-07
576.30	0.8002	2.7200e-07
576.30	0.8999	1.5800e-07
576.30	0.9503	8.6000e-08
576.30	1.0000	0.0000
581.30	0.0000	0.0000
581.30	0.0500	1.0200e-07
581.30	0.0999	1.9200e-07
581.30	0.2000	3.1900e-07
581.30	0.3000	4.1100e-07
581.30	0.4000	4.7300e-07
581.30	0.5000	4.9600e-07
581.30	0.6000	4.8400e-07
581.30	0.7000	4.2800e-07
581.30	0.8002	3.2900e-07
581.30	0.8999	1.9200e-07
581.30	0.9503	1.0200e-07
581.30	1.0000	0.0000
586.30	0.0000	0.0000
586.30	0.0500	1.3900e-07
586.30	0.0999	2.4300e-07
586.30	0.2000	3.7800e-07
586.30	0.3000	4.7100e-07
586.30	0.4000	5.3100e-07
586.30	0.5000	5.5400e-07
586.30	0.6000	5.3400e-07
586.30	0.7000	4.7200e-07
586.30	0.8002	3.8300e-07
586.30	0.8999	2.3800e-07
586.30	0.9503	1.3900e-07
586.30	1.0000	0.0000

Sources

• Thermodynamic and physicochemical properties of binary mixtures of nitromethane with {2-methoxyethanol + 2-butoxyethanol} systems at T = (293.15, 298.15, 303.15, 308.15, and 313.15) K

Note: These property values are available through the Cheméo API. A free account gives you an access key.