Mixture of Toluene + Morpholine, 4-acetyl-

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Toluene

Name
Toluene
InChI
InChI=1S/C7H8/c1-7-5-3-2-4-6-7/h2-6H,1H3
InChI Key
YXFVVABEGXRONW-UHFFFAOYSA-N
Formula
C7H8
SMILES
Cc1ccccc1
Mol. Weight (g/mol)
92.14
CAS
108-88-3

Morpholine, 4-acetyl-

Name
Morpholine, 4-acetyl-
InChI
InChI=1S/C6H11NO2/c1-6(8)7-2-4-9-5-3-7/h2-5H2,1H3
InChI Key
KYWXRBNOYGGPIZ-UHFFFAOYSA-N
Formula
C6H11NO2
SMILES
CC(=O)N1CCOCC1
Mol. Weight (g/mol)
129.16
CAS
1696-20-4
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Datasets

  1. ρl - Mass density, kg/m3 (2)

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Toluene (1) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0498 1104.1
293.15 0.0975 1094.3
293.15 0.1453 1084.0
293.15 0.2109 1070.1
293.15 0.2873 1053.3
293.15 0.3276 1044.3
293.15 0.3865 1030.8
293.15 0.4536 1015.1
293.15 0.4953 1005.1
293.15 0.5235 998.4
293.15 0.5641 988.2
293.15 0.6033 978.3
293.15 0.6844 957.3
293.15 0.7562 937.8
293.15 0.8126 922.2
293.15 0.8843 901.8
293.15 0.9225 890.5
293.15 0.9832 872.3
303.15 0.0498 1096.4
303.15 0.0975 1086.5
303.15 0.1453 1076.5
303.15 0.2109 1062.5
303.15 0.2873 1045.4
303.15 0.3276 1036.5
303.15 0.3865 1022.8
303.15 0.4536 1007.0
303.15 0.4953 996.9
303.15 0.5235 990.0
303.15 0.5641 979.8
303.15 0.6033 969.9
303.15 0.6844 949.0
303.15 0.7562 929.6
303.15 0.8126 913.7
303.15 0.8843 893.2
303.15 0.9225 881.8
303.15 0.9832 863.3
313.15 0.0498 1087.8
313.15 0.0975 1077.8
313.15 0.1453 1068.2
313.15 0.2109 1054.0
313.15 0.2873 1037.1
313.15 0.3276 1028.1
313.15 0.3865 1014.6
313.15 0.4536 998.7
313.15 0.4953 988.7
313.15 0.5235 981.7
313.15 0.5641 971.6
313.15 0.6033 961.7
313.15 0.6844 940.7
313.15 0.7562 921.3
313.15 0.8126 905.5
313.15 0.8843 885.0
313.15 0.9225 873.5
313.15 0.9832 855.2
323.15 0.0498 1079.4
323.15 0.0975 1069.6
323.15 0.1453 1059.9
323.15 0.2109 1045.6
323.15 0.2873 1028.6
323.15 0.3276 1019.5
323.15 0.3865 1005.8
323.15 0.4536 989.8
323.15 0.4953 979.7
323.15 0.5235 972.7
323.15 0.5641 962.5
323.15 0.6033 952.5
323.15 0.6844 931.5
323.15 0.7562 912.1
323.15 0.8126 896.2
323.15 0.8843 875.6
323.15 0.9225 864.1
323.15 0.9832 845.9
333.15 0.0498 1071.2
333.15 0.0975 1061.4
333.15 0.1453 1051.6
333.15 0.2109 1036.8
333.15 0.2873 1020.2
333.15 0.3276 1011.0
333.15 0.3865 997.2
333.15 0.4536 981.2
333.15 0.4953 970.8
333.15 0.5235 964.1
333.15 0.5641 953.8
333.15 0.6033 943.8
333.15 0.6844 922.7
333.15 0.7562 903.2
333.15 0.8126 887.4
333.15 0.8843 866.8
333.15 0.9225 855.3
333.15 0.9832 837.1
343.15 0.0498 1063.2
343.15 0.0975 1053.3
343.15 0.1453 1043.4
343.15 0.2109 1029.2
343.15 0.2873 1012.0
343.15 0.3276 1002.5
343.15 0.3865 988.6
343.15 0.4536 972.2
343.15 0.4953 962.1
343.15 0.5235 954.5
343.15 0.5641 944.9
343.15 0.6033 935.0
343.15 0.6844 913.9
343.15 0.7562 894.7
343.15 0.8126 879.3
343.15 0.8843 857.9
343.15 0.9225 846.4
343.15 0.9832 828.2

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Toluene (1) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0498 1104.1
293.15 0.0975 1094.3
293.15 0.1453 1084.0
293.15 0.2109 1070.1
293.15 0.2873 1053.3
293.15 0.3276 1044.3
293.15 0.3865 1030.8
293.15 0.4536 1015.1
293.15 0.4953 1005.1
293.15 0.5235 998.4
293.15 0.5641 988.2
293.15 0.6033 978.3
293.15 0.6844 957.3
293.15 0.7562 937.8
293.15 0.8126 922.2
293.15 0.8843 901.8
293.15 0.9225 890.5
293.15 0.9832 872.3
303.15 0.0498 1096.4
303.15 0.0975 1086.5
303.15 0.1453 1076.5
303.15 0.2109 1062.5
303.15 0.2873 1045.4
303.15 0.3276 1036.5
303.15 0.3865 1022.8
303.15 0.4536 1007.0
303.15 0.4953 996.9
303.15 0.5235 990.0
303.15 0.5641 979.8
303.15 0.6033 969.9
303.15 0.6844 949.0
303.15 0.7562 929.6
303.15 0.8126 913.7
303.15 0.8843 893.2
303.15 0.9225 881.8
303.15 0.9832 863.3
313.15 0.0498 1087.8
313.15 0.0975 1077.8
313.15 0.1453 1068.2
313.15 0.2109 1054.0
313.15 0.2873 1037.1
313.15 0.3276 1028.1
313.15 0.3865 1014.6
313.15 0.4536 998.7
313.15 0.4953 988.7
313.15 0.5235 981.7
313.15 0.5641 971.6
313.15 0.6033 961.7
313.15 0.6844 940.7
313.15 0.7562 921.3
313.15 0.8126 905.5
313.15 0.8843 885.0
313.15 0.9225 873.5
313.15 0.9832 855.2
323.15 0.0498 1079.4
323.15 0.0975 1069.6
323.15 0.1453 1059.9
323.15 0.2109 1045.6
323.15 0.2873 1028.6
323.15 0.3276 1019.5
323.15 0.3865 1005.8
323.15 0.4536 989.8
323.15 0.4953 979.7
323.15 0.5235 972.7
323.15 0.5641 962.5
323.15 0.6033 952.5
323.15 0.6844 931.5
323.15 0.7562 912.1
323.15 0.8126 896.2
323.15 0.8843 875.6
323.15 0.9225 864.1
323.15 0.9832 845.9
333.15 0.0498 1071.2
333.15 0.0975 1061.4
333.15 0.1453 1051.6
333.15 0.2109 1036.8
333.15 0.2873 1020.2
333.15 0.3276 1011.0
333.15 0.3865 997.2
333.15 0.4536 981.2
333.15 0.4953 970.8
333.15 0.5235 964.1
333.15 0.5641 953.8
333.15 0.6033 943.8
333.15 0.6844 922.7
333.15 0.7562 903.2
333.15 0.8126 887.4
333.15 0.8843 866.8
333.15 0.9225 855.3
333.15 0.9832 837.1
343.15 0.0498 1063.2
343.15 0.0975 1053.3
343.15 0.1453 1043.4
343.15 0.2109 1029.2
343.15 0.2873 1012.0
343.15 0.3276 1002.5
343.15 0.3865 988.6
343.15 0.4536 972.2
343.15 0.4953 962.1
343.15 0.5235 954.5
343.15 0.5641 944.9
343.15 0.6033 935.0
343.15 0.6844 913.9
343.15 0.7562 894.7
343.15 0.8126 879.3
343.15 0.8843 857.9
343.15 0.9225 846.4
343.15 0.9832 828.2

Sources