Mixture of Ethanol, 2-methoxy- + Benzene, 1,3-dimethyl-

Excel

Ethanol, 2-methoxy-

Name
Ethanol, 2-methoxy-
InChI
InChI=1S/C3H8O2/c1-5-3-2-4/h4H,2-3H2,1H3
InChI Key
XNWFRZJHXBZDAG-UHFFFAOYSA-N
Formula
C3H8O2
SMILES
COCCO
Mol. Weight (g/mol)
76.09
CAS
109-86-4

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
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. Activity coefficient (2)
  2. η - Viscosity, Pa*s (2)
  3. ρl - Mass density, kg/m3 (2)
  4. csound,fluid - Speed of Sound, m/s (2)

Activity coefficient of Benzene, 1,3-dimethyl- (2) [ref]

Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Mole fraction of Benzene, 1,3-dimethyl- (2) - Liquid Activity coefficient of Benzene, 1,3-dimethyl- (2) - Liquid
298.00 238.00 0.0000 5.2

Activity coefficient of Benzene, 1,3-dimethyl- (2) [ref]

Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Mole fraction of Benzene, 1,3-dimethyl- (2) - Liquid Activity coefficient of Benzene, 1,3-dimethyl- (2) - Liquid
298.00 238.00 0.0000 5.2

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethanol, 2-methoxy- (1) - Liquid Viscosity, Pa*s - Liquid
298.15 0.0519 0.0006
298.15 0.1498 0.0006
298.15 0.2504 0.0007
298.15 0.3476 0.0007
298.15 0.4520 0.0008
298.15 0.4991 0.0008
298.15 0.5538 0.0009
298.15 0.6476 0.0010
298.15 0.7504 0.0011
298.15 0.8491 0.0013
298.15 0.9558 0.0015
308.15 0.0519 0.0005
308.15 0.1498 0.0005
308.15 0.2504 0.0006
308.15 0.3476 0.0006
308.15 0.4520 0.0007
308.15 0.4991 0.0007
308.15 0.5538 0.0007
308.15 0.6476 0.0008
308.15 0.7504 0.0009
308.15 0.8491 0.0010
308.15 0.9558 0.0012

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethanol, 2-methoxy- (1) - Liquid Viscosity, Pa*s - Liquid
298.15 0.0519 0.0006
298.15 0.1498 0.0006
298.15 0.2504 0.0007
298.15 0.3476 0.0007
298.15 0.4520 0.0008
298.15 0.4991 0.0008
298.15 0.5538 0.0009
298.15 0.6476 0.0010
298.15 0.7504 0.0011
298.15 0.8491 0.0013
298.15 0.9558 0.0015
308.15 0.0519 0.0005
308.15 0.1498 0.0005
308.15 0.2504 0.0006
308.15 0.3476 0.0006
308.15 0.4520 0.0007
308.15 0.4991 0.0007
308.15 0.5538 0.0007
308.15 0.6476 0.0008
308.15 0.7504 0.0009
308.15 0.8491 0.0010
308.15 0.9558 0.0012

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethanol, 2-methoxy- (1) - Liquid Mass density, kg/m3 - Liquid
298.15 0.0519 862.4
298.15 0.1498 867.96
298.15 0.2504 874.92
298.15 0.3476 882.7
298.15 0.4520 892.1
298.15 0.4991 896.68
298.15 0.5538 902.24
298.15 0.6476 912.44
298.15 0.7504 924.64
298.15 0.8491 937.54
298.15 0.9558 953.14
303.15 0.0519 857.98
303.15 0.1498 863.28
303.15 0.2504 870.13
303.15 0.3476 877.91
303.15 0.4520 887.36
303.15 0.4991 891.97
303.15 0.5538 897.57
303.15 0.6476 907.82
303.15 0.7504 920.03
303.15 0.8491 932.9
303.15 0.9558 948.47
308.15 0.0519 853.64
308.15 0.1498 858.88
308.15 0.2504 865.82
308.15 0.3476 873.78
308.15 0.4520 883.47
308.15 0.4991 888.19
308.15 0.5538 893.92
308.15 0.6476 904.38
308.15 0.7504 916.84
308.15 0.8491 930.02
308.15 0.9558 946.12
313.15 0.0519 848.65
313.15 0.1498 853.65
313.15 0.2504 860.3
313.15 0.3476 867.96
313.15 0.4520 877.33
313.15 0.4991 881.91
313.15 0.5538 887.49
313.15 0.6476 897.71
313.15 0.7504 909.96
313.15 0.8491 922.98
313.15 0.9558 938.95

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethanol, 2-methoxy- (1) - Liquid Mass density, kg/m3 - Liquid
298.15 0.0519 862.4
298.15 0.1498 867.96
298.15 0.2504 874.92
298.15 0.3476 882.7
298.15 0.4520 892.1
298.15 0.4991 896.68
298.15 0.5538 902.24
298.15 0.6476 912.44
298.15 0.7504 924.64
298.15 0.8491 937.54
298.15 0.9558 953.14
303.15 0.0519 857.98
303.15 0.1498 863.28
303.15 0.2504 870.13
303.15 0.3476 877.91
303.15 0.4520 887.36
303.15 0.4991 891.97
303.15 0.5538 897.57
303.15 0.6476 907.82
303.15 0.7504 920.03
303.15 0.8491 932.9
303.15 0.9558 948.47
308.15 0.0519 853.64
308.15 0.1498 858.88
308.15 0.2504 865.82
308.15 0.3476 873.78
308.15 0.4520 883.47
308.15 0.4991 888.19
308.15 0.5538 893.92
308.15 0.6476 904.38
308.15 0.7504 916.84
308.15 0.8491 930.02
308.15 0.9558 946.12
313.15 0.0519 848.65
313.15 0.1498 853.65
313.15 0.2504 860.3
313.15 0.3476 867.96
313.15 0.4520 877.33
313.15 0.4991 881.91
313.15 0.5538 887.49
313.15 0.6476 897.71
313.15 0.7504 909.96
313.15 0.8491 922.98
313.15 0.9558 938.95

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethanol, 2-methoxy- (1) - Liquid Speed of sound, m/s - Liquid
298.15 0.0519 1317.0
298.15 0.1498 1312.0
298.15 0.2504 1309.0
298.15 0.3476 1309.0
298.15 0.4520 1310.0
298.15 0.4991 1311.0
298.15 0.5538 1312.0
298.15 0.6476 1316.0
298.15 0.7504 1321.0
298.15 0.8491 1327.0
298.15 0.9558 1335.0
308.15 0.0519 1279.0
308.15 0.1498 1275.0
308.15 0.2504 1273.0
308.15 0.3476 1273.0
308.15 0.4520 1275.0
308.15 0.4991 1277.0
308.15 0.5538 1279.0
308.15 0.6476 1285.0
308.15 0.7504 1293.0
308.15 0.8491 1304.0
308.15 0.9558 1320.0

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethanol, 2-methoxy- (1) - Liquid Speed of sound, m/s - Liquid
298.15 0.0519 1317.0
298.15 0.1498 1312.0
298.15 0.2504 1309.0
298.15 0.3476 1309.0
298.15 0.4520 1310.0
298.15 0.4991 1311.0
298.15 0.5538 1312.0
298.15 0.6476 1316.0
298.15 0.7504 1321.0
298.15 0.8491 1327.0
298.15 0.9558 1335.0
308.15 0.0519 1279.0
308.15 0.1498 1275.0
308.15 0.2504 1273.0
308.15 0.3476 1273.0
308.15 0.4520 1275.0
308.15 0.4991 1277.0
308.15 0.5538 1279.0
308.15 0.6476 1285.0
308.15 0.7504 1293.0
308.15 0.8491 1304.0
308.15 0.9558 1320.0

Sources