Mixture of Diethyl carbonate + 1-Propanol

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Diethyl carbonate

Name
Diethyl carbonate
InChI
InChI=1S/C5H10O3/c1-3-7-5(6)8-4-2/h3-4H2,1-2H3
InChI Key
OIFBSDVPJOWBCH-UHFFFAOYSA-N
Formula
C5H10O3
SMILES
CCOC(=O)OCC
Mol. Weight (g/mol)
118.13
CAS
105-58-8

1-Propanol

Name
1-Propanol
InChI
InChI=1S/C3H8O/c1-2-3-4/h4H,2-3H2,1H3
InChI Key
BDERNNFJNOPAEC-UHFFFAOYSA-N
Formula
C3H8O
SMILES
CCCO
Mol. Weight (g/mol)
60.09
CAS
71-23-8
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Datasets

  1. Mole fraction (2)
  2. η - Viscosity, Pa*s (6)
  3. Excess molar enthalpy (molar enthalpy (2)
  4. ρl - Mass density, kg/m3 (4)
  5. Tboil - Boiling temperature at pressure P, K (2)

Mole fraction of 1-Propanol (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of 1-Propanol (2) - Liquid Mole fraction of 1-Propanol (2) - Gas
0.0200 0.0719
0.0352 0.1216
0.0532 0.1762
0.0679 0.2184
0.0940 0.2832
0.1304 0.3628
0.1764 0.4427
0.2218 0.5057
0.2718 0.5599
0.3101 0.5943
0.3366 0.6148
0.3690 0.6393
0.4195 0.6701
0.4525 0.6893
0.4871 0.7113
0.5355 0.7335
0.5731 0.7520
0.6089 0.7723
0.6447 0.7874
0.6867 0.8085
0.7361 0.8373
0.7764 0.8563
0.8234 0.8811
0.8641 0.9048
0.9065 0.9300
0.9458 0.9537
0.9729 0.9749
0.9887 0.9894

Mole fraction of 1-Propanol (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of 1-Propanol (2) - Liquid Mole fraction of 1-Propanol (2) - Gas
0.0200 0.0719
0.0352 0.1216
0.0532 0.1762
0.0679 0.2184
0.0940 0.2832
0.1304 0.3628
0.1764 0.4427
0.2218 0.5057
0.2718 0.5599
0.3101 0.5943
0.3366 0.6148
0.3690 0.6393
0.4195 0.6701
0.4525 0.6893
0.4871 0.7113
0.5355 0.7335
0.5731 0.7520
0.6089 0.7723
0.6447 0.7874
0.6867 0.8085
0.7361 0.8373
0.7764 0.8563
0.8234 0.8811
0.8641 0.9048
0.9065 0.9300
0.9458 0.9537
0.9729 0.9749
0.9887 0.9894

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Diethyl carbonate (1) - Liquid Viscosity, Pa*s - Liquid
293.15 0.0000 0.0022
293.15 0.0504 0.0019
293.15 0.1007 0.0017
293.15 0.2008 0.0013
293.15 0.3019 0.0011
293.15 0.4004 0.0010
293.15 0.5039 0.0009
293.15 0.6031 0.0009
293.15 0.7007 0.0008
293.15 0.7999 0.0008
293.15 0.9132 0.0008
293.15 0.9531 0.0008
293.15 1.0000 0.0008
298.15 0.0000 0.0020
298.15 0.0515 0.0017
298.15 0.0993 0.0015
298.15 0.2012 0.0012
298.15 0.3007 0.0010
298.15 0.4026 0.0009
298.15 0.5022 0.0008
298.15 0.6029 0.0008
298.15 0.7041 0.0008
298.15 0.8087 0.0007
298.15 0.9065 0.0007
298.15 0.9523 0.0007
298.15 1.0000 0.0007
303.15 0.0000 0.0017
303.15 0.0464 0.0015
303.15 0.0963 0.0013
303.15 0.1968 0.0011
303.15 0.2981 0.0009
303.15 0.3987 0.0008
303.15 0.4958 0.0008
303.15 0.5991 0.0007
303.15 0.6967 0.0007
303.15 0.8063 0.0007
303.15 0.9080 0.0007
303.15 0.9448 0.0007
303.15 1.0000 0.0007
313.15 0.0000 0.0014
313.15 0.0500 0.0012
313.15 0.1018 0.0011
313.15 0.2001 0.0009
313.15 0.3017 0.0008
313.15 0.3958 0.0007
313.15 0.5040 0.0007
313.15 0.6009 0.0006
313.15 0.7032 0.0006
313.15 0.7998 0.0006
313.15 0.8997 0.0006
313.15 0.9468 0.0006
313.15 1.0000 0.0006

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Diethyl carbonate (1) - Liquid Viscosity, Pa*s - Liquid
293.15 0.0993 0.0017
293.15 0.2003 0.0013
293.15 0.3011 0.0011
298.15 0.0993 0.0015
298.15 0.2003 0.0012
298.15 0.3011 0.0010
303.15 0.0993 0.0013
303.15 0.2003 0.0011
303.15 0.3011 0.0009
313.15 0.0993 0.0011
313.15 0.2003 0.0009
313.15 0.3011 0.0008
323.15 0.0993 0.0009
323.15 0.2003 0.0008
323.15 0.3011 0.0007
333.15 0.0993 0.0007
333.15 0.2003 0.0006
333.15 0.3011 0.0006
343.15 0.0993 0.0006
343.15 0.2003 0.0005
343.15 0.3011 0.0005
353.15 0.0993 0.0005
353.15 0.2003 0.0005
353.15 0.3011 0.0004
363.15 0.0993 0.0004
363.15 0.2003 0.0004
363.15 0.3011 0.0004

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Diethyl carbonate (1) - Liquid Viscosity, Pa*s - Liquid
288.15 0.0512 0.0021
288.15 0.0726 0.0020
288.15 0.1063 0.0018
288.15 0.1511 0.0016
288.15 0.2122 0.0015
288.15 0.2638 0.0013
288.15 0.3100 0.0012
288.15 0.4016 0.0011
288.15 0.5147 0.0010
288.15 0.5916 0.0009
288.15 0.5994 0.0009
288.15 0.6906 0.0009
288.15 0.7887 0.0009
288.15 0.8694 0.0009
288.15 0.9428 0.0009
293.15 0.0496 0.0019
293.15 0.1001 0.0017
293.15 0.2101 0.0013
293.15 0.3074 0.0011
293.15 0.4038 0.0010
293.15 0.5097 0.0009
293.15 0.6002 0.0009
293.15 0.6963 0.0008
293.15 0.8059 0.0008
293.15 0.8817 0.0008
293.15 0.9433 0.0008
303.15 0.0515 0.0015
303.15 0.1008 0.0013
303.15 0.2044 0.0011
303.15 0.3161 0.0009
303.15 0.4048 0.0008
303.15 0.4459 0.0008
303.15 0.6000 0.0007
303.15 0.6892 0.0007
303.15 0.7920 0.0007
303.15 0.8809 0.0007
303.15 0.9364 0.0007
313.15 0.0467 0.0012
313.15 0.1008 0.0011
313.15 0.2119 0.0009
313.15 0.3075 0.0008
313.15 0.4133 0.0007
313.15 0.5019 0.0007
313.15 0.5998 0.0006
313.15 0.6913 0.0006
313.15 0.7902 0.0006
313.15 0.8456 0.0006
313.15 0.8699 0.0006
313.15 0.8903 0.0006
313.15 0.9488 0.0006

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Diethyl carbonate (1) - Liquid Viscosity, Pa*s - Liquid
293.15 0.0000 0.0022
293.15 0.0504 0.0019
293.15 0.1007 0.0017
293.15 0.2008 0.0013
293.15 0.3019 0.0011
293.15 0.4004 0.0010
293.15 0.5039 0.0009
293.15 0.6031 0.0009
293.15 0.7007 0.0008
293.15 0.7999 0.0008
293.15 0.9132 0.0008
293.15 0.9531 0.0008
293.15 1.0000 0.0008
298.15 0.0000 0.0020
298.15 0.0515 0.0017
298.15 0.0993 0.0015
298.15 0.2012 0.0012
298.15 0.3007 0.0010
298.15 0.4026 0.0009
298.15 0.5022 0.0008
298.15 0.6029 0.0008
298.15 0.7041 0.0008
298.15 0.8087 0.0007
298.15 0.9065 0.0007
298.15 0.9523 0.0007
298.15 1.0000 0.0007
303.15 0.0000 0.0017
303.15 0.0464 0.0015
303.15 0.0963 0.0013
303.15 0.1968 0.0011
303.15 0.2981 0.0009
303.15 0.3987 0.0008
303.15 0.4958 0.0008
303.15 0.5991 0.0007
303.15 0.6967 0.0007
303.15 0.8063 0.0007
303.15 0.9080 0.0007
303.15 0.9448 0.0007
303.15 1.0000 0.0007
313.15 0.0000 0.0014
313.15 0.0500 0.0012
313.15 0.1018 0.0011
313.15 0.2001 0.0009
313.15 0.3017 0.0008
313.15 0.3958 0.0007
313.15 0.5040 0.0007
313.15 0.6009 0.0006
313.15 0.7032 0.0006
313.15 0.7998 0.0006
313.15 0.8997 0.0006
313.15 0.9468 0.0006
313.15 1.0000 0.0006

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Diethyl carbonate (1) - Liquid Viscosity, Pa*s - Liquid
293.15 0.0993 0.0017
293.15 0.2003 0.0013
293.15 0.3011 0.0011
298.15 0.0993 0.0015
298.15 0.2003 0.0012
298.15 0.3011 0.0010
303.15 0.0993 0.0013
303.15 0.2003 0.0011
303.15 0.3011 0.0009
313.15 0.0993 0.0011
313.15 0.2003 0.0009
313.15 0.3011 0.0008
323.15 0.0993 0.0009
323.15 0.2003 0.0008
323.15 0.3011 0.0007
333.15 0.0993 0.0007
333.15 0.2003 0.0006
333.15 0.3011 0.0006
343.15 0.0993 0.0006
343.15 0.2003 0.0005
343.15 0.3011 0.0005
353.15 0.0993 0.0005
353.15 0.2003 0.0005
353.15 0.3011 0.0004
363.15 0.0993 0.0004
363.15 0.2003 0.0004
363.15 0.3011 0.0004

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Diethyl carbonate (1) - Liquid Viscosity, Pa*s - Liquid
288.15 0.0512 0.0021
288.15 0.0726 0.0020
288.15 0.1063 0.0018
288.15 0.1511 0.0016
288.15 0.2122 0.0015
288.15 0.2638 0.0013
288.15 0.3100 0.0012
288.15 0.4016 0.0011
288.15 0.5147 0.0010
288.15 0.5916 0.0009
288.15 0.5994 0.0009
288.15 0.6906 0.0009
288.15 0.7887 0.0009
288.15 0.8694 0.0009
288.15 0.9428 0.0009
293.15 0.0496 0.0019
293.15 0.1001 0.0017
293.15 0.2101 0.0013
293.15 0.3074 0.0011
293.15 0.4038 0.0010
293.15 0.5097 0.0009
293.15 0.6002 0.0009
293.15 0.6963 0.0008
293.15 0.8059 0.0008
293.15 0.8817 0.0008
293.15 0.9433 0.0008
303.15 0.0515 0.0015
303.15 0.1008 0.0013
303.15 0.2044 0.0011
303.15 0.3161 0.0009
303.15 0.4048 0.0008
303.15 0.4459 0.0008
303.15 0.6000 0.0007
303.15 0.6892 0.0007
303.15 0.7920 0.0007
303.15 0.8809 0.0007
303.15 0.9364 0.0007
313.15 0.0467 0.0012
313.15 0.1008 0.0011
313.15 0.2119 0.0009
313.15 0.3075 0.0008
313.15 0.4133 0.0007
313.15 0.5019 0.0007
313.15 0.5998 0.0006
313.15 0.6913 0.0006
313.15 0.7902 0.0006
313.15 0.8456 0.0006
313.15 0.8699 0.0006
313.15 0.8903 0.0006
313.15 0.9488 0.0006

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

Operational conditions:

Mole fraction of Diethyl carbonate (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0595 0.4328
0.1227 0.8196
0.1956 1.1749
0.2498 1.3735
0.2677 1.4376
0.3018 1.5531
0.3762 1.7578
0.4569 1.8442
0.4906 1.868
0.5642 1.8851
0.6182 1.8491
0.6932 1.744
0.7453 1.5911
0.8240 1.3057
0.8720 1.0376
0.9168 0.7269

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

Operational conditions:

Mole fraction of Diethyl carbonate (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0595 0.4328
0.1227 0.8196
0.1956 1.1749
0.2498 1.3735
0.2677 1.4376
0.3018 1.5531
0.3762 1.7578
0.4569 1.8442
0.4906 1.868
0.5642 1.8851
0.6182 1.8491
0.6932 1.744
0.7453 1.5911
0.8240 1.3057
0.8720 1.0376
0.9168 0.7269

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Diethyl carbonate (1) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0993 829.06
293.15 0.2003 852.0
293.15 0.3011 872.49
298.15 0.0993 824.24
298.15 0.2003 846.98
298.15 0.3011 867.35
303.15 0.0993 819.57
303.15 0.2003 841.86
303.15 0.3011 861.83
313.15 0.0993 810.34
313.15 0.2003 832.49
313.15 0.3011 852.34
323.15 0.0993 798.04
323.15 0.2003 819.74
323.15 0.3011 839.43
333.15 0.0993 790.59
333.15 0.2003 811.83
333.15 0.3011 831.0
343.15 0.0993 778.86
343.15 0.2003 799.8
343.15 0.3011 818.79
353.15 0.0993 770.55
353.15 0.2003 790.85
353.15 0.3011 809.27
363.15 0.0993 761.19
363.15 0.2003 780.98
363.15 0.3011 799.0

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Diethyl carbonate (1) - Liquid Mass density, kg/m3 - Liquid
288.15 0.0512 821.17
288.15 0.0726 826.61
288.15 0.1063 834.89
288.15 0.1511 845.43
288.15 0.2122 858.98
288.15 0.2638 869.76
288.15 0.3100 878.92
288.15 0.4016 895.92
288.15 0.5147 915.01
288.15 0.5916 926.96
288.15 0.5994 928.13
288.15 0.6906 941.32
288.15 0.7887 954.53
288.15 0.8694 964.81
288.15 0.9428 973.71
293.15 0.0496 816.57
293.15 0.1001 829.1
293.15 0.2101 853.96
293.15 0.3074 873.57
293.15 0.4038 891.34
293.15 0.5097 909.09
293.15 0.6002 923.04
293.15 0.6963 936.76
293.15 0.8059 951.25
293.15 0.8817 960.76
293.15 0.9433 968.14
303.15 0.0515 808.69
303.15 0.1008 820.63
303.15 0.2044 843.53
303.15 0.3161 865.57
303.15 0.4048 881.45
303.15 0.4459 888.41
303.15 0.6000 912.35
303.15 0.6892 924.91
303.15 0.7920 938.39
303.15 0.8809 949.35
303.15 0.9364 955.95
313.15 0.0467 798.89
313.15 0.1008 811.63
313.15 0.2119 835.52
313.15 0.3075 854.04
313.15 0.4133 872.66
313.15 0.5019 886.95
313.15 0.5998 901.56
313.15 0.6913 914.21
313.15 0.7902 926.98
313.15 0.8456 933.82
313.15 0.8699 936.73
313.15 0.8903 939.21
313.15 0.9488 946.12

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Diethyl carbonate (1) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0993 829.06
293.15 0.2003 852.0
293.15 0.3011 872.49
298.15 0.0993 824.24
298.15 0.2003 846.98
298.15 0.3011 867.35
303.15 0.0993 819.57
303.15 0.2003 841.86
303.15 0.3011 861.83
313.15 0.0993 810.34
313.15 0.2003 832.49
313.15 0.3011 852.34
323.15 0.0993 798.04
323.15 0.2003 819.74
323.15 0.3011 839.43
333.15 0.0993 790.59
333.15 0.2003 811.83
333.15 0.3011 831.0
343.15 0.0993 778.86
343.15 0.2003 799.8
343.15 0.3011 818.79
353.15 0.0993 770.55
353.15 0.2003 790.85
353.15 0.3011 809.27
363.15 0.0993 761.19
363.15 0.2003 780.98
363.15 0.3011 799.0

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Diethyl carbonate (1) - Liquid Mass density, kg/m3 - Liquid
288.15 0.0512 821.17
288.15 0.0726 826.61
288.15 0.1063 834.89
288.15 0.1511 845.43
288.15 0.2122 858.98
288.15 0.2638 869.76
288.15 0.3100 878.92
288.15 0.4016 895.92
288.15 0.5147 915.01
288.15 0.5916 926.96
288.15 0.5994 928.13
288.15 0.6906 941.32
288.15 0.7887 954.53
288.15 0.8694 964.81
288.15 0.9428 973.71
293.15 0.0496 816.57
293.15 0.1001 829.1
293.15 0.2101 853.96
293.15 0.3074 873.57
293.15 0.4038 891.34
293.15 0.5097 909.09
293.15 0.6002 923.04
293.15 0.6963 936.76
293.15 0.8059 951.25
293.15 0.8817 960.76
293.15 0.9433 968.14
303.15 0.0515 808.69
303.15 0.1008 820.63
303.15 0.2044 843.53
303.15 0.3161 865.57
303.15 0.4048 881.45
303.15 0.4459 888.41
303.15 0.6000 912.35
303.15 0.6892 924.91
303.15 0.7920 938.39
303.15 0.8809 949.35
303.15 0.9364 955.95
313.15 0.0467 798.89
313.15 0.1008 811.63
313.15 0.2119 835.52
313.15 0.3075 854.04
313.15 0.4133 872.66
313.15 0.5019 886.95
313.15 0.5998 901.56
313.15 0.6913 914.21
313.15 0.7902 926.98
313.15 0.8456 933.82
313.15 0.8699 936.73
313.15 0.8903 939.21
313.15 0.9488 946.12

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of 1-Propanol (2) - Liquid Boiling temperature at pressure P, K - Liquid
0.0200 397.64
0.0352 395.99
0.0532 394.22
0.0679 392.87
0.0940 390.65
0.1304 387.95
0.1764 384.92
0.2218 382.59
0.2718 380.55
0.3101 379.29
0.3366 378.54
0.3690 377.70
0.4195 376.69
0.4525 376.06
0.4871 375.39
0.5355 374.74
0.5731 374.22
0.6089 373.68
0.6447 373.30
0.6867 372.80
0.7361 372.18
0.7764 371.76
0.8234 371.38
0.8641 371.07
0.9065 370.66
0.9458 370.45
0.9729 370.37
0.9887 370.35

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of 1-Propanol (2) - Liquid Boiling temperature at pressure P, K - Liquid
0.0200 397.64
0.0352 395.99
0.0532 394.22
0.0679 392.87
0.0940 390.65
0.1304 387.95
0.1764 384.92
0.2218 382.59
0.2718 380.55
0.3101 379.29
0.3366 378.54
0.3690 377.70
0.4195 376.69
0.4525 376.06
0.4871 375.39
0.5355 374.74
0.5731 374.22
0.6089 373.68
0.6447 373.30
0.6867 372.80
0.7361 372.18
0.7764 371.76
0.8234 371.38
0.8641 371.07
0.9065 370.66
0.9458 370.45
0.9729 370.37
0.9887 370.35

Sources