Mixture of Benzene + 1,3-Butadiene

Excel

Benzene

Name
Benzene
InChI
InChI=1S/C6H6/c1-2-4-6-5-3-1/h1-6H
InChI Key
UHOVQNZJYSORNB-UHFFFAOYSA-N
Formula
C6H6
SMILES
c1ccccc1
Mol. Weight (g/mol)
78.11
CAS
71-43-2

1,3-Butadiene

Name
1,3-Butadiene
InChI
InChI=1S/C4H6/c1-3-4-2/h3-4H,1-2H2
InChI Key
KAKZBPTYRLMSJV-UHFFFAOYSA-N
Formula
C4H6
SMILES
C=CC=C
Mol. Weight (g/mol)
54.09
CAS
106-99-0
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Datasets

  1. Activity coefficient (2)
  2. Henry's Law constant (mole fraction scale), kPa (2)
  3. Vapor Liquid Equilibrium at Constant Temperature (3)

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

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid Activity coefficient of 1,3-Butadiene (2) - Liquid
279.99 1.36
289.99 1.35
309.99 1.32
329.99 1.29

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

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid Activity coefficient of 1,3-Butadiene (2) - Liquid
279.99 1.36
289.99 1.35
309.99 1.32
329.99 1.29

Henry's Law constant (mole fraction scale), kPa of 1,3-Butadiene (2) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid Henry's Law constant (mole fraction scale), kPa of 1,3-Butadiene (2) - Liquid
279.99 200.0
289.99 276.0
309.99 481.0
329.99 760.0

Henry's Law constant (mole fraction scale), kPa of 1,3-Butadiene (2) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid Henry's Law constant (mole fraction scale), kPa of 1,3-Butadiene (2) - Liquid
279.99 200.0
289.99 276.0
309.99 481.0
329.99 760.0

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 298.15 (VLE)

Fixed Measured
P [kPa] - VLE x1[mol/mol] of 1,3-Butadiene (2) - Liquid y1[mol/mol] of 1,3-Butadiene (2) - Vapour
12.751 0.0000 0.0000
25.047 0.0376 0.5060
38.946 0.0818 0.6940
52.306 0.1253 0.7810
64.132 0.1650 0.8280
74.278 0.2003 0.8560
84.272 0.2353 0.8780

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 303.15 (VLE)

Fixed Measured
P [kPa] - VLE x1[mol/mol] of 1,3-Butadiene (2) - Liquid y1[mol/mol] of 1,3-Butadiene (2) - Vapour
15.908 0.0000 0.0000
50.663 0.1160 0.7480
101.325 0.2640 0.9080
151.988 0.4220 0.9580
202.65 0.5840 0.9800
253.313 0.7460 0.9950
303.975 0.9040 0.9990
333.359 1.0000 1.0000

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 343.15 (VLE)

Fixed Measured
P [kPa] - VLE x1[mol/mol] of 1,3-Butadiene (2) - Liquid y1[mol/mol] of 1,3-Butadiene (2) - Vapour
73.461 0.0000 0.0000
101.325 0.0400 0.4000
202.65 0.1480 0.7960
303.975 0.2660 0.8960
405.3 0.3760 0.9400
506.625 0.4920 0.9640
607.95 0.6100 0.9820
709.275 0.7280 0.9920
810.6 0.8440 0.9960
911.925 0.9580 0.9990
949.415 1.0000 1.0000

Sources