Mixture of 1-Butanol + Furan, tetrahydro-2-methyl-

Excel

1-Butanol

Name
1-Butanol
InChI
InChI=1S/C4H10O/c1-2-3-4-5/h5H,2-4H2,1H3
InChI Key
LRHPLDYGYMQRHN-UHFFFAOYSA-N
Formula
C4H10O
SMILES
CCCCO
Mol. Weight (g/mol)
74.12
CAS
71-36-3

Furan, tetrahydro-2-methyl-

Name
Furan, tetrahydro-2-methyl-
InChI
InChI=1S/C5H10O/c1-5-3-2-4-6-5/h5H,2-4H2,1H3
InChI Key
JWUJQDFVADABEY-UHFFFAOYSA-N
Formula
C5H10O
SMILES
CC1CCCO1
Mol. Weight (g/mol)
86.13
CAS
96-47-9
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry. Do not hesitate to contact us for your projects.

Datasets

  1. η - Viscosity, Pa*s (2)
  2. Excess molar enthalpy (molar enthalpy (2)
  3. ν - Kinematic viscosity, m2/s (2)
  4. ρl - Mass density, kg/m3 (4)
  5. csound,fluid - Speed of Sound, m/s (2)

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Mole fraction of Furan, tetrahydro-2-methyl- (2) - Liquid Temperature, K - Liquid Viscosity, Pa*s - Liquid
0.0518 283.15 0.0032
0.0518 298.15 0.0022
0.0518 313.15 0.0016
0.1048 283.15 0.0027
0.1048 298.15 0.0019
0.1048 313.15 0.0014
0.2123 283.15 0.0020
0.2123 298.15 0.0014
0.2123 313.15 0.0011
0.3159 283.15 0.0015
0.3159 298.15 0.0011
0.3159 313.15 0.0009
0.4197 283.15 0.0012
0.4197 298.15 0.0010
0.4197 313.15 0.0008
0.5195 283.15 0.0010
0.5195 298.15 0.0008
0.5195 313.15 0.0007
0.6211 283.15 0.0009
0.6211 298.15 0.0007
0.6211 313.15 0.0006
0.7116 283.15 0.0008
0.7116 298.15 0.0006
0.7116 313.15 0.0005
0.8103 283.15 0.0007
0.8103 298.15 0.0006
0.8103 313.15 0.0005
0.9246 283.15 0.0006
0.9246 298.15 0.0005
0.9246 313.15 0.0004
0.9585 283.15 0.0006
0.9585 298.15 0.0005
0.9585 313.15 0.0004

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Mole fraction of Furan, tetrahydro-2-methyl- (2) - Liquid Temperature, K - Liquid Viscosity, Pa*s - Liquid
0.0518 283.15 0.0032
0.0518 298.15 0.0022
0.0518 313.15 0.0016
0.1048 283.15 0.0027
0.1048 298.15 0.0019
0.1048 313.15 0.0014
0.2123 283.15 0.0020
0.2123 298.15 0.0014
0.2123 313.15 0.0011
0.3159 283.15 0.0015
0.3159 298.15 0.0011
0.3159 313.15 0.0009
0.4197 283.15 0.0012
0.4197 298.15 0.0010
0.4197 313.15 0.0008
0.5195 283.15 0.0010
0.5195 298.15 0.0008
0.5195 313.15 0.0007
0.6211 283.15 0.0009
0.6211 298.15 0.0007
0.6211 313.15 0.0006
0.7116 283.15 0.0008
0.7116 298.15 0.0006
0.7116 313.15 0.0005
0.8103 283.15 0.0007
0.8103 298.15 0.0006
0.8103 313.15 0.0005
0.9246 283.15 0.0006
0.9246 298.15 0.0005
0.9246 313.15 0.0004
0.9585 283.15 0.0006
0.9585 298.15 0.0005
0.9585 313.15 0.0004

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Mole fraction of Furan, tetrahydro-2-methyl- (2) - Liquid Temperature, K - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0540 283.15 0.0990
0.0540 298.15 0.1100
0.0540 313.15 0.1160
0.1040 283.15 0.2060
0.1040 298.15 0.2200
0.1040 313.15 0.2340
0.2060 283.15 0.3850
0.2060 298.15 0.4250
0.2060 313.15 0.4550
0.3080 283.15 0.5480
0.3080 298.15 0.5870
0.3080 313.15 0.6320
0.4110 283.15 0.6460
0.4110 298.15 0.6940
0.4110 313.15 0.7480
0.5100 283.15 0.6950
0.5100 298.15 0.7480
0.5100 313.15 0.8060
0.6090 283.15 0.6930
0.6090 298.15 0.7460
0.6090 313.15 0.8030
0.7080 283.15 0.6310
0.7080 298.15 0.6780
0.7080 313.15 0.7280
0.8060 283.15 0.5050
0.8060 298.15 0.5410
0.8060 313.15 0.5780
0.9070 283.15 0.2910
0.9070 298.15 0.3100
0.9070 313.15 0.3290
0.9530 283.15 0.1590
0.9530 298.15 0.1700
0.9530 313.15 0.1790

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Mole fraction of Furan, tetrahydro-2-methyl- (2) - Liquid Temperature, K - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0540 283.15 0.0990
0.0540 298.15 0.1100
0.0540 313.15 0.1160
0.1040 283.15 0.2060
0.1040 298.15 0.2200
0.1040 313.15 0.2340
0.2060 283.15 0.3850
0.2060 298.15 0.4250
0.2060 313.15 0.4550
0.3080 283.15 0.5480
0.3080 298.15 0.5870
0.3080 313.15 0.6320
0.4110 283.15 0.6460
0.4110 298.15 0.6940
0.4110 313.15 0.7480
0.5100 283.15 0.6950
0.5100 298.15 0.7480
0.5100 313.15 0.8060
0.6090 283.15 0.6930
0.6090 298.15 0.7460
0.6090 313.15 0.8030
0.7080 283.15 0.6310
0.7080 298.15 0.6780
0.7080 313.15 0.7280
0.8060 283.15 0.5050
0.8060 298.15 0.5410
0.8060 313.15 0.5780
0.9070 283.15 0.2910
0.9070 298.15 0.3100
0.9070 313.15 0.3290
0.9530 283.15 0.1590
0.9530 298.15 0.1700
0.9530 313.15 0.1790

Kinematic viscosity, m2/s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 1-Butanol (1) - Liquid Kinematic viscosity, m2/s - Liquid
298.15 0.0000 5.5930e-07
298.15 0.0488 5.9130e-07
298.15 0.1039 6.2160e-07
298.15 0.2050 6.9270e-07
298.15 0.3006 7.6990e-07
298.15 0.4051 8.8060e-07
298.15 0.5099 1.0508e-06
298.15 0.6036 1.2082e-06
298.15 0.7034 1.4661e-06
298.15 0.8042 1.8409e-06
298.15 0.9060 2.4024e-06
298.15 0.9582 2.7999e-06
298.15 1.0000 3.1928e-06
313.15 0.0000 4.9160e-07
313.15 0.0488 5.1060e-07
313.15 0.1039 5.3450e-07
313.15 0.2050 5.8810e-07
313.15 0.3006 6.5150e-07
313.15 0.4051 7.3390e-07
313.15 0.5099 8.4120e-07
313.15 0.6036 9.6950e-07
313.15 0.7034 1.1555e-06
313.15 0.8042 1.3925e-06
313.15 0.9060 1.7561e-06
313.15 0.9582 1.9934e-06
313.15 1.0000 2.2249e-06

Kinematic viscosity, m2/s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 1-Butanol (1) - Liquid Kinematic viscosity, m2/s - Liquid
298.15 0.0000 5.5930e-07
298.15 0.0488 5.9130e-07
298.15 0.1039 6.2160e-07
298.15 0.2050 6.9270e-07
298.15 0.3006 7.6990e-07
298.15 0.4051 8.8060e-07
298.15 0.5099 1.0508e-06
298.15 0.6036 1.2082e-06
298.15 0.7034 1.4661e-06
298.15 0.8042 1.8409e-06
298.15 0.9060 2.4024e-06
298.15 0.9582 2.7999e-06
298.15 1.0000 3.1928e-06
313.15 0.0000 4.9160e-07
313.15 0.0488 5.1060e-07
313.15 0.1039 5.3450e-07
313.15 0.2050 5.8810e-07
313.15 0.3006 6.5150e-07
313.15 0.4051 7.3390e-07
313.15 0.5099 8.4120e-07
313.15 0.6036 9.6950e-07
313.15 0.7034 1.1555e-06
313.15 0.8042 1.3925e-06
313.15 0.9060 1.7561e-06
313.15 0.9582 1.9934e-06
313.15 1.0000 2.2249e-06

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 1-Butanol (1) - Liquid Mass density, kg/m3 - Liquid
298.15 0.0000 849.28
298.15 0.0488 847.62
298.15 0.1039 845.56
298.15 0.2050 841.78
298.15 0.3006 838.03
298.15 0.4051 833.86
298.15 0.5099 829.37
298.15 0.6036 825.28
298.15 0.7034 820.68
298.15 0.8042 815.8
298.15 0.9060 810.56
298.15 0.9582 807.81
298.15 1.0000 805.56
313.15 0.0000 834.01
313.15 0.0488 832.35
313.15 0.1039 830.5
313.15 0.2050 827.07
313.15 0.3006 823.64
313.15 0.4051 820.0
313.15 0.5099 815.98
313.15 0.6036 812.07
313.15 0.7034 807.96
313.15 0.8042 803.45
313.15 0.9060 798.76
313.15 0.9582 796.23
313.15 1.0000 794.19

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Mole fraction of Furan, tetrahydro-2-methyl- (2) - Liquid Temperature, K - Liquid Mass density, kg/m3 - Liquid
0.0539 283.15 820.03
0.1020 298.15 811.16
0.1038 313.15 799.46
0.1047 283.15 822.92
0.2068 283.15 828.51
0.2068 298.15 816.38
0.2098 313.15 804.34
0.3108 283.15 833.9
0.3108 298.15 821.37
0.3139 313.15 808.86
0.4135 313.15 813.0
0.4147 283.15 839.04
0.4152 298.15 826.08
0.4848 298.15 829.16
0.4893 283.15 842.56
0.4906 313.15 816.02
0.6175 313.15 820.8
0.6191 298.15 834.74
0.6195 283.15 848.41
0.7240 283.15 852.97
0.7245 298.15 838.88
0.7256 313.15 824.59
0.8157 298.15 842.28
0.8172 313.15 827.71
0.8909 313.15 830.17
0.8911 298.15 845.05
0.8923 283.15 859.92

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 1-Butanol (1) - Liquid Mass density, kg/m3 - Liquid
298.15 0.0000 849.28
298.15 0.0488 847.62
298.15 0.1039 845.56
298.15 0.2050 841.78
298.15 0.3006 838.03
298.15 0.4051 833.86
298.15 0.5099 829.37
298.15 0.6036 825.28
298.15 0.7034 820.68
298.15 0.8042 815.8
298.15 0.9060 810.56
298.15 0.9582 807.81
298.15 1.0000 805.56
313.15 0.0000 834.01
313.15 0.0488 832.35
313.15 0.1039 830.5
313.15 0.2050 827.07
313.15 0.3006 823.64
313.15 0.4051 820.0
313.15 0.5099 815.98
313.15 0.6036 812.07
313.15 0.7034 807.96
313.15 0.8042 803.45
313.15 0.9060 798.76
313.15 0.9582 796.23
313.15 1.0000 794.19

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Mole fraction of Furan, tetrahydro-2-methyl- (2) - Liquid Temperature, K - Liquid Mass density, kg/m3 - Liquid
0.0539 283.15 820.03
0.1020 298.15 811.16
0.1038 313.15 799.46
0.1047 283.15 822.92
0.2068 283.15 828.51
0.2068 298.15 816.38
0.2098 313.15 804.34
0.3108 283.15 833.9
0.3108 298.15 821.37
0.3139 313.15 808.86
0.4135 313.15 813.0
0.4147 283.15 839.04
0.4152 298.15 826.08
0.4848 298.15 829.16
0.4893 283.15 842.56
0.4906 313.15 816.02
0.6175 313.15 820.8
0.6191 298.15 834.74
0.6195 283.15 848.41
0.7240 283.15 852.97
0.7245 298.15 838.88
0.7256 313.15 824.59
0.8157 298.15 842.28
0.8172 313.15 827.71
0.8909 313.15 830.17
0.8911 298.15 845.05
0.8923 283.15 859.92

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Mole fraction of Furan, tetrahydro-2-methyl- (2) - Liquid Temperature, K - Liquid Speed of sound, m/s - Liquid
0.0341 298.15 1242.6
0.0447 283.15 1292.4
0.0519 313.15 1184.6
0.1054 298.15 1241.6
0.1154 283.15 1292.6
0.1237 313.15 1181.8
0.2085 298.15 1238.8
0.2143 283.15 1291.5
0.2168 313.15 1177.7
0.2451 283.15 1291.0
0.2968 298.15 1235.7
0.3097 313.15 1172.9
0.3535 298.15 1233.4
0.4133 313.15 1167.2
0.4221 283.15 1286.8
0.4283 298.15 1230.3
0.5058 298.15 1226.8
0.5110 313.15 1161.3
0.5204 283.15 1284.0
0.6075 298.15 1222.2
0.6172 283.15 1281.2
0.6561 313.15 1152.6
0.7077 298.15 1217.6
0.7128 283.15 1278.1
0.7265 313.15 1148.3
0.8078 283.15 1275.2
0.8111 298.15 1212.6
0.8151 313.15 1142.7
0.8947 298.15 1208.3
0.8952 283.15 1272.2
0.8995 313.15 1137.1
0.9337 298.15 1206.1
0.9364 283.15 1270.3
0.9476 313.15 1133.5

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Mole fraction of Furan, tetrahydro-2-methyl- (2) - Liquid Temperature, K - Liquid Speed of sound, m/s - Liquid
0.0341 298.15 1242.6
0.0447 283.15 1292.4
0.0519 313.15 1184.6
0.1054 298.15 1241.6
0.1154 283.15 1292.6
0.1237 313.15 1181.8
0.2085 298.15 1238.8
0.2143 283.15 1291.5
0.2168 313.15 1177.7
0.2451 283.15 1291.0
0.2968 298.15 1235.7
0.3097 313.15 1172.9
0.3535 298.15 1233.4
0.4133 313.15 1167.2
0.4221 283.15 1286.8
0.4283 298.15 1230.3
0.5058 298.15 1226.8
0.5110 313.15 1161.3
0.5204 283.15 1284.0
0.6075 298.15 1222.2
0.6172 283.15 1281.2
0.6561 313.15 1152.6
0.7077 298.15 1217.6
0.7128 283.15 1278.1
0.7265 313.15 1148.3
0.8078 283.15 1275.2
0.8111 298.15 1212.6
0.8151 313.15 1142.7
0.8947 298.15 1208.3
0.8952 283.15 1272.2
0.8995 313.15 1137.1
0.9337 298.15 1206.1
0.9364 283.15 1270.3
0.9476 313.15 1133.5

Sources