Mixture of 2-Pyrrolidinone, 1-methyl- + Benzene, 1,3-dimethyl-

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2-Pyrrolidinone, 1-methyl-

Name
2-Pyrrolidinone, 1-methyl-
InChI
InChI=1S/C5H9NO/c1-6-4-2-3-5(6)7/h2-4H2,1H3
InChI Key
SECXISVLQFMRJM-UHFFFAOYSA-N
Formula
C5H9NO
SMILES
CN1CCCC1=O
Mol. Weight (g/mol)
99.13
CAS
872-50-4

Benzene, 1,3-dimethyl-

Name
Benzene, 1,3-dimethyl-
InChI
InChI=1S/C8H10/c1-7-4-3-5-8(2)6-7/h3-6H,1-2H3
InChI Key
IVSZLXZYQVIEFR-UHFFFAOYSA-N
Formula
C8H10
SMILES
Cc1cccc(C)c1
Mol. Weight (g/mol)
106.17
CAS
108-38-3
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Datasets

  1. ρl - Mass density, kg/m3 (2)
  2. Vapor Liquid Equilibrium at Constant Temperature (2)

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Benzene, 1,3-dimethyl- (2) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0000 1032.66
293.15 0.0451 1024.18
293.15 0.1145 1011.33
293.15 0.1874 998.07
293.15 0.2451 987.76
293.15 0.3258 973.58
293.15 0.3987 961.0
293.15 0.4657 949.63
293.15 0.5214 940.31
293.15 0.5985 927.59
293.15 0.6584 917.85
293.15 0.7214 907.73
293.15 0.7987 895.48
293.15 0.8547 886.71
293.15 0.9048 878.92
293.15 0.9597 870.47
293.15 1.0000 864.31
303.15 0.0000 1023.42
303.15 0.0541 1013.3
303.15 0.1134 1002.37
303.15 0.1954 987.52
303.15 0.2562 976.72
303.15 0.3214 965.31
303.15 0.3895 953.58
303.15 0.4487 943.53
303.15 0.5014 934.7
303.15 0.5782 922.02
303.15 0.6484 910.6
303.15 0.7154 899.86
303.15 0.7654 891.93
303.15 0.8241 882.72
303.15 0.8815 873.79
303.15 0.9465 863.8
303.15 1.0000 855.64
313.15 0.0000 1014.27
313.15 0.0487 1005.18
313.15 0.1151 992.96
313.15 0.1745 982.21
313.15 0.2495 968.86
313.15 0.3147 957.46
313.15 0.3851 945.34
313.15 0.4587 932.89
313.15 0.5185 922.93
313.15 0.6214 906.08
313.15 0.6785 896.89
313.15 0.7484 885.77
313.15 0.7945 878.53
313.15 0.8521 869.55
313.15 0.9021 861.83
313.15 0.9548 853.77
313.15 1.0000 846.9
323.15 0.0000 1005.62
323.15 0.0548 995.37
323.15 0.1154 984.22
323.15 0.1754 973.34
323.15 0.2354 962.63
323.15 0.2965 951.89
323.15 0.3551 941.73
323.15 0.4158 931.36
323.15 0.4814 920.31
323.15 0.5385 910.84
323.15 0.5821 903.68
323.15 0.6514 892.44
323.15 0.7085 883.3
323.15 0.7765 872.54
323.15 0.8512 860.88
323.15 0.9374 847.61
323.15 1.0000 838.09
333.15 0.0000 996.28
333.15 0.0451 987.86
333.15 0.1102 975.88
333.15 0.1985 959.95
333.15 0.2511 950.64
333.15 0.3201 938.59
333.15 0.3952 925.71
333.15 0.4625 914.36
333.15 0.5214 904.57
333.15 0.5985 891.95
333.15 0.6584 882.28
333.15 0.7121 873.71
333.15 0.7741 863.94
333.15 0.8351 854.42
333.15 0.8812 847.31
333.15 0.9487 836.99
333.15 1.0000 829.22
343.15 0.0000 987.39
343.15 0.0547 977.18
343.15 0.1241 964.43
343.15 0.1887 952.77
343.15 0.2654 939.18
343.15 0.3214 929.42
343.15 0.3985 916.19
343.15 0.4658 904.84
343.15 0.5214 895.6
343.15 0.5985 882.97
343.15 0.6541 874.0
343.15 0.7014 866.44
343.15 0.7654 856.33
343.15 0.8354 845.41
343.15 0.8924 836.63
343.15 0.9469 828.32
343.15 1.0000 820.29
353.15 0.0000 978.62
353.15 0.0544 968.44
353.15 0.1214 956.1
353.15 0.1958 942.64
353.15 0.2562 931.9
353.15 0.3214 920.5
353.15 0.3985 907.25
353.15 0.4515 898.28
353.15 0.5114 888.28
353.15 0.5941 874.69
353.15 0.6621 863.71
353.15 0.7214 854.26
353.15 0.7852 844.22
353.15 0.8471 834.59
353.15 0.8915 827.76
353.15 0.9565 817.85
353.15 1.0000 811.29

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Benzene, 1,3-dimethyl- (2) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0000 1032.66
293.15 0.0451 1024.18
293.15 0.1145 1011.33
293.15 0.1874 998.07
293.15 0.2451 987.76
293.15 0.3258 973.58
293.15 0.3987 961.0
293.15 0.4657 949.63
293.15 0.5214 940.31
293.15 0.5985 927.59
293.15 0.6584 917.85
293.15 0.7214 907.73
293.15 0.7987 895.48
293.15 0.8547 886.71
293.15 0.9048 878.92
293.15 0.9597 870.47
293.15 1.0000 864.31
303.15 0.0000 1023.42
303.15 0.0541 1013.3
303.15 0.1134 1002.37
303.15 0.1954 987.52
303.15 0.2562 976.72
303.15 0.3214 965.31
303.15 0.3895 953.58
303.15 0.4487 943.53
303.15 0.5014 934.7
303.15 0.5782 922.02
303.15 0.6484 910.6
303.15 0.7154 899.86
303.15 0.7654 891.93
303.15 0.8241 882.72
303.15 0.8815 873.79
303.15 0.9465 863.8
303.15 1.0000 855.64
313.15 0.0000 1014.27
313.15 0.0487 1005.18
313.15 0.1151 992.96
313.15 0.1745 982.21
313.15 0.2495 968.86
313.15 0.3147 957.46
313.15 0.3851 945.34
313.15 0.4587 932.89
313.15 0.5185 922.93
313.15 0.6214 906.08
313.15 0.6785 896.89
313.15 0.7484 885.77
313.15 0.7945 878.53
313.15 0.8521 869.55
313.15 0.9021 861.83
313.15 0.9548 853.77
313.15 1.0000 846.9
323.15 0.0000 1005.62
323.15 0.0548 995.37
323.15 0.1154 984.22
323.15 0.1754 973.34
323.15 0.2354 962.63
323.15 0.2965 951.89
323.15 0.3551 941.73
323.15 0.4158 931.36
323.15 0.4814 920.31
323.15 0.5385 910.84
323.15 0.5821 903.68
323.15 0.6514 892.44
323.15 0.7085 883.3
323.15 0.7765 872.54
323.15 0.8512 860.88
323.15 0.9374 847.61
323.15 1.0000 838.09
333.15 0.0000 996.28
333.15 0.0451 987.86
333.15 0.1102 975.88
333.15 0.1985 959.95
333.15 0.2511 950.64
333.15 0.3201 938.59
333.15 0.3952 925.71
333.15 0.4625 914.36
333.15 0.5214 904.57
333.15 0.5985 891.95
333.15 0.6584 882.28
333.15 0.7121 873.71
333.15 0.7741 863.94
333.15 0.8351 854.42
333.15 0.8812 847.31
333.15 0.9487 836.99
333.15 1.0000 829.22
343.15 0.0000 987.39
343.15 0.0547 977.18
343.15 0.1241 964.43
343.15 0.1887 952.77
343.15 0.2654 939.18
343.15 0.3214 929.42
343.15 0.3985 916.19
343.15 0.4658 904.84
343.15 0.5214 895.6
343.15 0.5985 882.97
343.15 0.6541 874.0
343.15 0.7014 866.44
343.15 0.7654 856.33
343.15 0.8354 845.41
343.15 0.8924 836.63
343.15 0.9469 828.32
343.15 1.0000 820.29
353.15 0.0000 978.62
353.15 0.0544 968.44
353.15 0.1214 956.1
353.15 0.1958 942.64
353.15 0.2562 931.9
353.15 0.3214 920.5
353.15 0.3985 907.25
353.15 0.4515 898.28
353.15 0.5114 888.28
353.15 0.5941 874.69
353.15 0.6621 863.71
353.15 0.7214 854.26
353.15 0.7852 844.22
353.15 0.8471 834.59
353.15 0.8915 827.76
353.15 0.9565 817.85
353.15 1.0000 811.29

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 373.15 (VLE)

Fixed Measured
P [kPa] - VLE x1[mol/mol] of Benzene, 1,3-dimethyl- (2) - Liquid y1[mol/mol] of Benzene, 1,3-dimethyl- (2) - Vapour
8.59 0.0983 0.6231
11.57 0.1865 0.7456
14.96 0.2860 0.8143
20.23 0.4757 0.8942
24.57 0.6865 0.9397
29.34 0.8942 0.9805

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 393.15 (VLE)

Fixed Measured
P [kPa] - VLE x1[mol/mol] of Benzene, 1,3-dimethyl- (2) - Liquid y1[mol/mol] of Benzene, 1,3-dimethyl- (2) - Vapour
16.5 0.0983 0.5581
22.439 0.1865 0.7140
29.63 0.2860 0.8039
39.63 0.4757 0.8895
48.24 0.6865 0.9407
55.619 0.8942 0.9786

Sources