Mixture of Dodecane + 2-Butanol

Datasets

1. C_p,liquid - Molar heat capacity at constant pressure, J/K/mol
2. η - Viscosity, Pa*s
3. P_vap - Vapor or sublimation pressure, kPa (2)
4. ρ_l - Mass density, kg/m3 (2)
5. c_sound,fluid - Speed of Sound, m/s (2)

Molar heat capacity at constant pressure, J/K/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 2-Butanol (2) - Liquid	Molar heat capacity at constant pressure, J/K/mol - Liquid
283.15	0.0460	368.81
283.15	0.0507	368.27
283.15	0.0929	362.22
283.15	0.1813	347.53
283.15	0.2498	335.43
283.15	0.3004	326.19
283.15	0.3397	319.07
283.15	0.3827	310.89
283.15	0.4894	291.24
283.15	0.5943	271.63
283.15	0.6983	250.80
283.15	0.8047	228.10
283.15	0.9024	205.58
283.15	0.9518	193.81
288.15	0.0460	371.20
288.15	0.0507	370.87
288.15	0.0929	365.51
288.15	0.1813	351.44
288.15	0.2498	339.54
288.15	0.3004	330.40
288.15	0.3397	323.35
288.15	0.3827	315.22
288.15	0.4894	295.51
288.15	0.5943	276.16
288.15	0.6983	255.61
288.15	0.8047	233.26
288.15	0.9024	210.78
288.15	0.9518	198.92
298.15	0.0460	375.87
298.15	0.0507	375.91
298.15	0.0929	371.99
298.15	0.1813	359.44
298.15	0.2498	348.04
298.15	0.3004	339.21
298.15	0.3397	332.29
298.15	0.3827	324.42
298.15	0.4894	304.59
298.15	0.5943	285.33
298.15	0.6983	265.16
298.15	0.8047	243.52
298.15	0.9024	221.25
298.15	0.9518	209.36
308.15	0.0460	380.02
308.15	0.0507	380.01
308.15	0.0929	377.88
308.15	0.1813	367.12
308.15	0.2498	356.53
308.15	0.3004	348.12
308.15	0.3397	341.43
308.15	0.3827	333.69
308.15	0.4894	313.86
308.15	0.5943	294.46
308.15	0.6983	274.50
308.15	0.8047	253.41
308.15	0.9024	231.68
308.15	0.9518	219.79
313.15	0.0460	381.77
313.15	0.0507	381.76
313.15	0.0929	380.52
313.15	0.1813	370.85
313.15	0.2498	360.66
313.15	0.3004	352.50
313.15	0.3397	345.94
313.15	0.3827	338.16
313.15	0.4894	318.50
313.15	0.5943	299.14
313.15	0.6983	279.14
313.15	0.8047	258.32
313.15	0.9024	236.78
313.15	0.9518	225.00
318.15	0.0460	383.08
318.15	0.0507	383.28
318.15	0.0929	382.79
318.15	0.1813	374.26
318.15	0.2498	364.70
318.15	0.3004	356.68
318.15	0.3397	350.35
318.15	0.3827	342.58
318.15	0.4894	323.17
318.15	0.5943	303.75
318.15	0.6983	284.00
318.15	0.8047	263.01
318.15	0.9024	241.63
318.15	0.9518	230.03

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 2-Butanol (2) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0000	0.0015
293.15	0.0486	0.0014
293.15	0.0976	0.0014
293.15	0.2046	0.0014
293.15	0.2956	0.0014
293.15	0.3959	0.0015
293.15	0.4979	0.0015
293.15	0.5980	0.0016
293.15	0.7021	0.0018
293.15	0.8008	0.0021
293.15	0.9002	0.0026
293.15	0.9504	0.0030
293.15	1.0000	0.0036
298.15	0.0000	0.0013
298.15	0.0486	0.0013
298.15	0.0976	0.0013
298.15	0.2046	0.0013
298.15	0.2956	0.0013
298.15	0.3959	0.0013
298.15	0.4979	0.0014
298.15	0.5980	0.0014
298.15	0.7021	0.0016
298.15	0.8008	0.0018
298.15	0.9002	0.0022
298.15	0.9504	0.0025
298.15	1.0000	0.0030
303.15	0.0000	0.0012
303.15	0.0486	0.0012
303.15	0.0976	0.0012
303.15	0.2046	0.0012
303.15	0.2956	0.0012
303.15	0.3959	0.0012
303.15	0.4979	0.0012
303.15	0.5980	0.0013
303.15	0.7021	0.0014
303.15	0.8008	0.0016
303.15	0.9002	0.0019
303.15	0.9504	0.0021
303.15	1.0000	0.0025

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 2-Butanol (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
342.70	0.0000	0.36
342.70	0.0050	0.96
342.70	0.0130	2.57
342.70	0.0197	3.68
342.70	0.0342	5.59
342.70	0.0564	8.54
342.70	0.0660	9.30
342.70	0.0771	10.36
342.70	0.0899	11.48
342.70	0.1032	12.58
342.70	0.1190	13.30
342.70	0.1314	14.17
342.70	0.1480	14.61
342.70	0.1659	15.83
342.70	0.1814	16.15
342.70	0.1965	16.60
342.70	0.2134	17.27
342.70	0.2352	17.91
342.70	0.2515	18.19
342.70	0.2715	18.82
342.70	0.2946	19.27
342.70	0.3199	19.85
342.70	0.3453	20.40
342.70	0.3743	20.87
342.70	0.4007	21.43
342.70	0.4277	21.94
342.70	0.4557	22.26
342.70	0.4855	22.65
342.70	0.5104	23.16
342.70	0.5331	23.47
342.70	0.5662	24.00
342.70	0.6217	24.70
342.70	0.6791	25.23
342.70	0.7297	25.64
342.70	0.7572	26.27
342.70	0.8053	26.59
342.70	0.8521	26.77
342.70	0.8991	27.69
342.70	0.9520	27.91
342.70	0.9769	28.30
342.70	0.9833	28.33
342.70	0.9893	28.42
342.70	0.9939	28.48
342.70	0.9979	28.40
342.70	1.0000	28.43
352.80	0.0000	0.75
352.80	0.0053	1.87
352.80	0.0094	3.03
352.80	0.0146	4.46
352.80	0.0258	6.48
352.80	0.0354	8.17
352.80	0.0442	9.58
352.80	0.0590	11.49
352.80	0.0789	14.72
352.80	0.0989	17.11
352.80	0.1199	19.14
352.80	0.1501	21.75
352.80	0.1825	23.95
352.80	0.2092	25.59
352.80	0.2429	27.04
352.80	0.2934	28.63
352.80	0.3366	29.89
352.80	0.3745	31.15
352.80	0.4102	32.43
352.80	0.4481	33.54
352.80	0.4818	34.07
352.80	0.5166	35.21
352.80	0.5638	35.96
352.80	0.5661	34.74
352.80	0.6382	36.95
352.80	0.7561	39.26
352.80	0.8052	40.06
352.80	0.8565	41.31
352.80	0.9070	42.24
352.80	0.9487	43.40
352.80	0.9828	44.18
352.80	0.9895	44.33
352.80	0.9969	44.38
352.80	1.0000	44.66

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of 2-Butanol (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	0.06
0.0500	2.45
0.1006	3.21
0.1490	3.60
0.1989	3.90
0.2489	4.14
0.2986	4.33
0.3489	4.50
0.3995	4.63
0.4102	4.66
0.4485	4.75
0.4488	4.76
0.4990	4.88
0.5008	4.87
0.5494	4.98
0.5551	4.97
0.5996	5.07
0.6008	5.06
0.6504	5.15
0.7009	5.23
0.7504	5.32
0.8008	5.42
0.8508	5.53
0.9003	5.67
0.9505	5.84
1.0000	6.05

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 2-Butanol (2) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	748.5
293.15	0.0486	749.3
293.15	0.0976	750.2
293.15	0.2046	752.5
293.15	0.2956	754.9
293.15	0.3959	758.1
293.15	0.4979	762.2
293.15	0.5980	767.2
293.15	0.7021	773.9
293.15	0.8008	781.9
293.15	0.9002	792.7
293.15	0.9504	799.1
293.15	1.0000	806.8
298.15	0.0000	744.9
298.15	0.0486	745.6
298.15	0.0976	746.4
298.15	0.2046	748.7
298.15	0.2956	751.1
298.15	0.3959	754.2
298.15	0.4979	758.3
298.15	0.5980	763.2
298.15	0.7021	769.8
298.15	0.8008	777.8
298.15	0.9002	788.5
298.15	0.9504	794.9
298.15	1.0000	802.7
303.15	0.0000	741.3
303.15	0.0486	741.9
303.15	0.0976	742.7
303.15	0.2046	744.9
303.15	0.2956	747.2
303.15	0.3959	750.3
303.15	0.4979	754.3
303.15	0.5980	759.1
303.15	0.7021	765.6
303.15	0.8008	773.6
303.15	0.9002	784.3
303.15	0.9504	790.7
303.15	1.0000	798.5

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 2-Butanol (2) - Liquid	Mass density, kg/m3 - Liquid
278.15	0.0460	760.12
278.15	0.0507	760.17
278.15	0.0929	760.95
278.15	0.1813	762.89
278.15	0.2498	764.65
278.15	0.2836	765.59
278.15	0.3004	766.1
278.15	0.3397	767.36
278.15	0.3827	768.8
278.15	0.4894	773.14
278.15	0.5943	778.5
278.15	0.6983	785.13
278.15	0.8047	793.85
278.15	0.9024	804.21
278.15	0.9518	810.69
283.15	0.0460	756.43
283.15	0.0507	756.5
283.15	0.0929	757.29
283.15	0.1813	759.18
283.15	0.2498	760.89
283.15	0.2836	761.85
283.15	0.3004	762.33
283.15	0.3397	763.57
283.15	0.3827	765.02
283.15	0.4894	769.3
283.15	0.5943	774.61
283.15	0.6983	781.24
283.15	0.8047	789.92
283.15	0.9024	800.31
283.15	0.9518	806.8
288.15	0.0460	752.79
288.15	0.0507	752.85
288.15	0.0929	753.61
288.15	0.1813	755.47
288.15	0.2498	757.15
288.15	0.2836	758.09
288.15	0.3004	758.57
288.15	0.3397	759.79
288.15	0.3827	761.21
288.15	0.4894	765.43
288.15	0.5943	770.68
288.15	0.6983	777.27
288.15	0.8047	785.96
288.15	0.9024	796.36
288.15	0.9518	802.84
298.15	0.0460	745.46
298.15	0.0507	745.51
298.15	0.0929	746.19
298.15	0.1813	747.97
298.15	0.2498	749.59
298.15	0.2836	750.5
298.15	0.3004	750.94
298.15	0.3397	752.15
298.15	0.3827	753.51
298.15	0.4894	757.62
298.15	0.5943	762.72
298.15	0.6983	769.2
298.15	0.8047	777.8
298.15	0.9024	788.21
298.15	0.9518	794.74
308.15	0.0460	738.06
308.15	0.0507	738.11
308.15	0.0929	738.72
308.15	0.1813	740.36
308.15	0.2498	741.9
308.15	0.2836	742.77
308.15	0.3004	743.22
308.15	0.3397	744.36
308.15	0.3827	745.69
308.15	0.4894	749.62
308.15	0.5943	754.56
308.15	0.6983	760.88
308.15	0.8047	769.39
308.15	0.9024	779.73
308.15	0.9518	786.27
313.15	0.0460	734.35
313.15	0.0507	734.39
313.15	0.0929	734.95
313.15	0.1813	736.52
313.15	0.2498	738.02
313.15	0.2836	738.86
313.15	0.3004	739.3
313.15	0.3397	740.42
313.15	0.3827	741.71
313.15	0.4894	745.57
313.15	0.5943	750.42
313.15	0.6983	756.65
313.15	0.8047	765.06
313.15	0.9024	775.36
313.15	0.9518	781.89
318.15	0.0460	730.61
318.15	0.0507	730.64
318.15	0.0929	731.15
318.15	0.1813	732.63
318.15	0.2498	734.07
318.15	0.2836	734.9
318.15	0.3004	735.32
318.15	0.3397	736.4
318.15	0.3827	737.68
318.15	0.4894	741.45
318.15	0.5943	746.23
318.15	0.6983	752.33
318.15	0.8047	760.64
318.15	0.9024	770.88
318.15	0.9518	777.38

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 2-Butanol (2) - Liquid	Speed of sound, m/s - Liquid
293.15	0.0000	1297.0
293.15	0.0486	1293.0
293.15	0.0976	1289.0
293.15	0.2046	1282.0
293.15	0.2956	1276.0
293.15	0.3959	1268.0
293.15	0.4979	1261.0
293.15	0.5980	1255.0
293.15	0.7021	1248.0
293.15	0.8008	1242.0
293.15	0.9002	1236.0
293.15	0.9504	1233.0
293.15	1.0000	1230.0
298.15	0.0000	1278.0
298.15	0.0486	1274.0
298.15	0.0976	1270.0
298.15	0.2046	1263.0
298.15	0.2956	1256.0
298.15	0.3959	1249.0
298.15	0.4979	1242.0
298.15	0.5980	1235.0
298.15	0.7021	1229.0
298.15	0.8008	1223.0
298.15	0.9002	1217.0
298.15	0.9504	1215.0
298.15	1.0000	1212.0
303.15	0.0000	1259.0
303.15	0.0486	1255.0
303.15	0.0976	1251.0
303.15	0.2046	1243.0
303.15	0.2956	1237.0
303.15	0.3959	1230.0
303.15	0.4979	1222.0
303.15	0.5980	1216.0
303.15	0.7021	1209.0
303.15	0.8008	1204.0
303.15	0.9002	1199.0
303.15	0.9504	1196.0
303.15	1.0000	1194.0

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 2-Butanol (2) - Liquid	Speed of sound, m/s - Liquid
278.15	0.0460	1352.71
278.15	0.0507	1352.23
278.15	0.0929	1349.11
278.15	0.1813	1342.7
278.15	0.2498	1337.8
278.15	0.3004	1333.96
278.15	0.3397	1331.15
278.15	0.3827	1327.93
278.15	0.4894	1320.58
278.15	0.5943	1313.68
278.15	0.6983	1306.65
278.15	0.8047	1298.97
278.15	0.9024	1291.01
278.15	0.9518	1286.96
283.15	0.0460	1332.55
283.15	0.0507	1332.16
283.15	0.0929	1329.1
283.15	0.1813	1322.72
283.15	0.2498	1317.72
283.15	0.3004	1313.93
283.15	0.3397	1311.08
283.15	0.3827	1307.94
283.15	0.4894	1300.59
283.15	0.5943	1293.66
283.15	0.6983	1286.88
283.15	0.8047	1279.62
283.15	0.9024	1272.34
283.15	0.9518	1268.68
288.15	0.0460	1312.74
288.15	0.0507	1312.32
288.15	0.0929	1309.26
288.15	0.1813	1302.82
288.15	0.2498	1297.76
288.15	0.3004	1294.05
288.15	0.3397	1291.23
288.15	0.3827	1288.14
288.15	0.4894	1280.62
288.15	0.5943	1273.68
288.15	0.6983	1267.06
288.15	0.8047	1260.19
288.15	0.9024	1253.5
288.15	0.9518	1250.22
298.15	0.0460	1273.46
298.15	0.0507	1273.1
298.15	0.0929	1269.82
298.15	0.1813	1263.38
298.15	0.2498	1258.36
298.15	0.3004	1254.67
298.15	0.3397	1251.84
298.15	0.3827	1248.76
298.15	0.4894	1241.13
298.15	0.5943	1234.11
298.15	0.6983	1227.66
298.15	0.8047	1221.36
298.15	0.9024	1215.73
298.15	0.9518	1213.24
308.15	0.0460	1234.92
308.15	0.0507	1234.48
308.15	0.0929	1231.07
308.15	0.1813	1224.51
308.15	0.2498	1219.48
308.15	0.3004	1215.85
308.15	0.3397	1213.01
308.15	0.3827	1209.91
308.15	0.4894	1202.2
308.15	0.5943	1195.02
308.15	0.6983	1188.52
308.15	0.8047	1182.58
308.15	0.9024	1177.79
308.15	0.9518	1175.92
313.15	0.0460	1215.9
313.15	0.0507	1215.47
313.15	0.0929	1211.97
313.15	0.1813	1205.33
313.15	0.2498	1200.26
313.15	0.3004	1196.6
313.15	0.3397	1193.81
313.15	0.3827	1190.64
313.15	0.4894	1182.95
313.15	0.5943	1175.58
313.15	0.6983	1169.12
313.15	0.8047	1163.24
313.15	0.9024	1158.73
313.15	0.9518	1157.14
318.15	0.0460	1197.08
318.15	0.0507	1196.62
318.15	0.0929	1193.03
318.15	0.1813	1186.25
318.15	0.2498	1181.2
318.15	0.3004	1177.53
318.15	0.3397	1174.71
318.15	0.3827	1171.59
318.15	0.4894	1163.8
318.15	0.5943	1156.43
318.15	0.6983	1149.84
318.15	0.8047	1143.97
318.15	0.9024	1139.65
318.15	0.9518	1138.24

Sources

• P-x data for binary systems using a novel static total pressure apparatus
• Dynamic viscosities of 2-butanol with alkanes (C8, C10, and C12) at several temperatures
• Thermodynamic Properties of dodecane + 1-butanol and + 2-butanol systems
• Vapor Liquid Equilibria of Binary Mixtures Containing 2-Butanol and Hydrocarbons at 313.15 K

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