Mixture of Methane + Heptane + Water

Excel

Methane

Name
Methane
InChI
InChI=1S/CH4/h1H4
InChI Key
VNWKTOKETHGBQD-UHFFFAOYSA-N
Formula
CH4
SMILES
C
Mol. Weight (g/mol)
16.04
CAS
74-82-8

Heptane

Name
Heptane
InChI
InChI=1S/C7H16/c1-3-5-7-6-4-2/h3-7H2,1-2H3
InChI Key
IMNFDUFMRHMDMM-UHFFFAOYSA-N
Formula
C7H16
SMILES
CCCCCCC
Mol. Weight (g/mol)
100.20
CAS
142-82-5

Water

Name
Water
InChI
InChI=1S/H2O/h1H2
InChI Key
XLYOFNOQVPJJNP-UHFFFAOYSA-N
Formula
H2O
SMILES
O
Mol. Weight (g/mol)
18.02
CAS
7732-18-5
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. Mole fraction (10)
  2. η - Viscosity, Pa*s (2)
  3. Vapor or sublimation pressure, kPa (2)

Mole fraction of Methane (1) [ref]

Operational condition: Temperature, K = 275.5 (Liquid mixture 1)

Mole fraction of Methane (1) - Gas Mole fraction of Methane (1) - Liquid mixture 1
0.9640 0.0151
0.9935 0.0270
0.9950 0.0764

Mole fraction of Methane (1) [ref]

Operational condition: Temperature, K = 275.5 (Liquid mixture 2)

Mole fraction of Methane (1) - Gas Mole fraction of Methane (1) - Liquid mixture 2
0.9640 0.0000
0.9935 0.0003
0.9950 0.0005

Mole fraction of Water (3) [ref]

Operational condition: Temperature, K = 275.5 (Gas)

Mole fraction of Methane (1) - Gas Mole fraction of Water (3) - Gas
0.9640 0.0068
0.9935 0.0013
0.9950 0.0007

Mole fraction of Water (3) [ref]

Operational condition: Temperature, K = 275.5 (Liquid mixture 1)

Mole fraction of Methane (1) - Gas Mole fraction of Water (3) - Liquid mixture 1
0.9640 0.0008
0.9935 0.0006
0.9950 0.0006

Mole fraction of Water (3) [ref]

Operational condition: Temperature, K = 275.5 (Liquid mixture 2)

Mole fraction of Methane (1) - Gas Mole fraction of Water (3) - Liquid mixture 2
0.9640 1.0000
0.9935 0.9997
0.9950 0.9995

Mole fraction of Methane (1) [ref]

Operational condition: Temperature, K = 275.5 (Liquid mixture 1)

Mole fraction of Methane (1) - Gas Mole fraction of Methane (1) - Liquid mixture 1
0.9640 0.0151
0.9935 0.0270
0.9950 0.0764

Mole fraction of Methane (1) [ref]

Operational condition: Temperature, K = 275.5 (Liquid mixture 2)

Mole fraction of Methane (1) - Gas Mole fraction of Methane (1) - Liquid mixture 2
0.9640 0.0000
0.9935 0.0003
0.9950 0.0005

Mole fraction of Water (3) [ref]

Operational condition: Temperature, K = 275.5 (Gas)

Mole fraction of Methane (1) - Gas Mole fraction of Water (3) - Gas
0.9640 0.0068
0.9935 0.0013
0.9950 0.0007

Mole fraction of Water (3) [ref]

Operational condition: Temperature, K = 275.5 (Liquid mixture 1)

Mole fraction of Methane (1) - Gas Mole fraction of Water (3) - Liquid mixture 1
0.9640 0.0008
0.9935 0.0006
0.9950 0.0006

Mole fraction of Water (3) [ref]

Operational condition: Temperature, K = 275.5 (Liquid mixture 2)

Mole fraction of Methane (1) - Gas Mole fraction of Water (3) - Liquid mixture 2
0.9640 1.0000
0.9935 0.9997
0.9950 0.9995

Viscosity, Pa*s [ref]

Fixed Measured
Mole fraction of Methane (1) - Liquid Mole fraction of Heptane (2) - Liquid Temperature, K - Liquid Pressure, kPa - Liquid Viscosity, Pa*s - Liquid
0.4230 0.5590 423.15 34570.00 0.0001
0.4230 0.5590 423.15 51780.00 0.0001
0.4230 0.5590 423.15 68980.00 0.0002
0.4230 0.5590 423.15 86230.00 0.0002
0.4230 0.5590 423.15 103460.00 0.0002
0.4230 0.5590 423.15 120720.00 0.0002
0.4230 0.5590 423.15 137870.00 0.0002
0.4230 0.5590 473.15 34560.00 0.0001
0.4230 0.5590 473.15 51800.00 0.0001
0.4230 0.5590 473.15 68980.00 0.0001
0.4230 0.5590 473.15 86230.00 0.0001
0.4230 0.5590 473.15 103470.00 0.0002
0.4230 0.5590 473.15 120700.00 0.0002
0.4230 0.5590 473.15 137910.00 0.0002
0.4132 0.5373 473.15 34570.00 0.0001
0.4132 0.5373 473.15 51750.00 0.0001
0.4132 0.5373 473.15 69000.00 0.0001
0.4132 0.5373 473.15 86210.00 0.0001
0.4132 0.5373 473.15 103490.00 0.0002
0.4132 0.5373 473.15 120690.00 0.0002
0.4132 0.5373 473.15 137910.00 0.0002

Viscosity, Pa*s [ref]

Fixed Measured
Mole fraction of Methane (1) - Liquid Mole fraction of Heptane (2) - Liquid Temperature, K - Liquid Pressure, kPa - Liquid Viscosity, Pa*s - Liquid
0.4230 0.5590 423.15 34570.00 0.0001
0.4230 0.5590 423.15 51780.00 0.0001
0.4230 0.5590 423.15 68980.00 0.0002
0.4230 0.5590 423.15 86230.00 0.0002
0.4230 0.5590 423.15 103460.00 0.0002
0.4230 0.5590 423.15 120720.00 0.0002
0.4230 0.5590 423.15 137870.00 0.0002
0.4230 0.5590 473.15 34560.00 0.0001
0.4230 0.5590 473.15 51800.00 0.0001
0.4230 0.5590 473.15 68980.00 0.0001
0.4230 0.5590 473.15 86230.00 0.0001
0.4230 0.5590 473.15 103470.00 0.0002
0.4230 0.5590 473.15 120700.00 0.0002
0.4230 0.5590 473.15 137910.00 0.0002
0.4132 0.5373 473.15 34570.00 0.0001
0.4132 0.5373 473.15 51750.00 0.0001
0.4132 0.5373 473.15 69000.00 0.0001
0.4132 0.5373 473.15 86210.00 0.0001
0.4132 0.5373 473.15 103490.00 0.0002
0.4132 0.5373 473.15 120690.00 0.0002
0.4132 0.5373 473.15 137910.00 0.0002

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 275.5 (Gas)

Mole fraction of Methane (1) - Gas Vapor or sublimation pressure, kPa - Gas
0.9640 120.00
0.9935 1000.00
0.9950 2000.00

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 275.5 (Gas)

Mole fraction of Methane (1) - Gas Vapor or sublimation pressure, kPa - Gas
0.9640 120.00
0.9935 1000.00
0.9950 2000.00

Sources