Mixture of Benzene + Trichloromethane

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

Trichloromethane

Name
Trichloromethane
InChI
InChI=1S/CHCl3/c2-1(3)4/h1H
InChI Key
HEDRZPFGACZZDS-UHFFFAOYSA-N
Formula
CHCl3
SMILES
ClC(Cl)Cl
Mol. Weight (g/mol)
119.38
CAS
67-66-3
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Datasets

  1. ρl - Mass density, kg/m3 (2)
  2. Binary diffusion coefficient, m2/s (2)
  3. Vapor Liquid Equilibrium at Constant Pressure (2)
  4. Vapor Liquid Equilibrium at Constant Temperature

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.33 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Trichloromethane (2) - Liquid Mass density, kg/m3 - Liquid
288.15 0.0000 884.246
288.15 0.1001 939.224
288.15 0.2000 995.529
288.15 0.3072 1057.295
288.15 0.3995 1111.961
288.15 0.4997 1172.451
288.15 0.6000 1234.482
288.15 0.6652 1275.682
288.15 0.7991 1362.317
288.15 0.8009 1363.447
288.15 0.9000 1429.592
288.15 1.0000 1498.077
293.15 0.0000 878.918
293.15 0.1001 933.584
293.15 0.2000 989.568
293.15 0.3072 1050.963
293.15 0.3995 1105.286
293.15 0.4997 1165.384
293.15 0.6000 1226.992
293.15 0.6652 1267.904
293.15 0.7991 1353.909
293.15 0.8009 1355.031
293.15 0.9000 1420.676
293.15 1.0000 1488.638
298.15 0.0000 873.582
298.15 0.1001 927.935
298.15 0.2000 983.589
298.15 0.3072 1044.608
298.15 0.3995 1098.581
298.15 0.4997 1158.284
298.15 0.6000 1219.472
298.15 0.6652 1260.092
298.15 0.7991 1345.461
298.15 0.8009 1346.576
298.15 0.9000 1411.713
298.15 1.0000 1479.148
303.15 0.0000 868.233
303.15 0.1001 922.271
303.15 0.2000 977.59
303.15 0.3072 1038.228
303.15 0.3995 1091.845
303.15 0.4997 1151.153
303.15 0.6000 1211.919
303.15 0.6652 1252.24
303.15 0.7991 1336.966
303.15 0.8009 1338.088
303.15 0.9000 1402.703
303.15 1.0000 1469.612
308.15 0.0000 862.871
308.15 0.1001 916.586
308.15 0.2000 971.567
308.15 0.3072 1031.818
308.15 0.3995 1085.078
308.15 0.4997 1143.984
308.15 0.6000 1204.331
308.15 0.6652 1244.341
308.15 0.7991 1328.421
308.15 0.8009 1329.56
308.15 0.9000 1393.631
308.15 1.0000 1460.025
313.15 0.0000 857.498
313.15 0.1001 910.883
313.15 0.2000 965.527
313.15 0.3072 1025.378
313.15 0.3995 1078.273
313.15 0.4997 1136.781
313.15 0.6000 1196.741
313.15 0.6652 1236.407
313.15 0.7991 1319.824
313.15 0.8009 1321.038
313.15 0.9000 1384.52
313.15 1.0000 1450.413

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.33 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Trichloromethane (2) - Liquid Mass density, kg/m3 - Liquid
288.15 0.0000 884.246
288.15 0.1001 939.224
288.15 0.2000 995.529
288.15 0.3072 1057.295
288.15 0.3995 1111.961
288.15 0.4997 1172.451
288.15 0.6000 1234.482
288.15 0.6652 1275.682
288.15 0.7991 1362.317
288.15 0.8009 1363.447
288.15 0.9000 1429.592
288.15 1.0000 1498.077
293.15 0.0000 878.918
293.15 0.1001 933.584
293.15 0.2000 989.568
293.15 0.3072 1050.963
293.15 0.3995 1105.286
293.15 0.4997 1165.384
293.15 0.6000 1226.992
293.15 0.6652 1267.904
293.15 0.7991 1353.909
293.15 0.8009 1355.031
293.15 0.9000 1420.676
293.15 1.0000 1488.638
298.15 0.0000 873.582
298.15 0.1001 927.935
298.15 0.2000 983.589
298.15 0.3072 1044.608
298.15 0.3995 1098.581
298.15 0.4997 1158.284
298.15 0.6000 1219.472
298.15 0.6652 1260.092
298.15 0.7991 1345.461
298.15 0.8009 1346.576
298.15 0.9000 1411.713
298.15 1.0000 1479.148
303.15 0.0000 868.233
303.15 0.1001 922.271
303.15 0.2000 977.59
303.15 0.3072 1038.228
303.15 0.3995 1091.845
303.15 0.4997 1151.153
303.15 0.6000 1211.919
303.15 0.6652 1252.24
303.15 0.7991 1336.966
303.15 0.8009 1338.088
303.15 0.9000 1402.703
303.15 1.0000 1469.612
308.15 0.0000 862.871
308.15 0.1001 916.586
308.15 0.2000 971.567
308.15 0.3072 1031.818
308.15 0.3995 1085.078
308.15 0.4997 1143.984
308.15 0.6000 1204.331
308.15 0.6652 1244.341
308.15 0.7991 1328.421
308.15 0.8009 1329.56
308.15 0.9000 1393.631
308.15 1.0000 1460.025
313.15 0.0000 857.498
313.15 0.1001 910.883
313.15 0.2000 965.527
313.15 0.3072 1025.378
313.15 0.3995 1078.273
313.15 0.4997 1136.781
313.15 0.6000 1196.741
313.15 0.6652 1236.407
313.15 0.7991 1319.824
313.15 0.8009 1321.038
313.15 0.9000 1384.52
313.15 1.0000 1450.413

Binary diffusion coefficient, m2/s [ref]

Fixed Measured
Mole fraction of Benzene (1) - Liquid Pressure, kPa - Liquid Temperature, K - Liquid Binary diffusion coefficient, m2/s - Liquid
0.0000 101.00 298.15 0.0000

Binary diffusion coefficient, m2/s [ref]

Fixed Measured
Mole fraction of Benzene (1) - Liquid Pressure, kPa - Liquid Temperature, K - Liquid Binary diffusion coefficient, m2/s - Liquid
0.0000 101.00 298.15 0.0000

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of Trichloromethane (2) - Liquid y1[mol/mol] of Trichloromethane (2) - Vapour
353.15 0.0500 0.0600
352.95 0.0800 0.1000
352.35 0.1200 0.1500
351.65 0.2000 0.2700
350.15 0.3200 0.4450
349.45 0.3800 0.5200
348.45 0.4500 0.6100
346.65 0.5600 0.7100
345.45 0.6400 0.7800
342.15 0.7800 0.8900
341.15 0.8200 0.9100

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of Trichloromethane (2) - Liquid y1[mol/mol] of Trichloromethane (2) - Vapour
352.35 0.0600 0.0890
352.15 0.0680 0.1000
351.55 0.1160 0.1670
351.05 0.1330 0.1900
350.05 0.1930 0.2700
349.35 0.2290 0.3160
348.85 0.2660 0.3610
347.85 0.3180 0.4290
347.55 0.3330 0.4430
346.45 0.3880 0.5080
345.35 0.4430 0.5700
344.75 0.4670 0.6010
343.95 0.5170 0.6520
342.85 0.5700 0.7020
341.45 0.6370 0.7620
340.15 0.7000 0.8140
338.55 0.7830 0.8750
337.25 0.8530 0.9220
335.75 0.9340 0.9680

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 298.2 (VLE)

Fixed Measured
P [kPa] - VLE x1[mol/mol] of Trichloromethane (2) - Liquid y1[mol/mol] of Trichloromethane (2) - Vapour
14.119 0.1340 0.2180
15.732 0.2840 0.4240
16.732 0.3600 0.5300
20.718 0.6280 0.8040
22.665 0.7400 0.8860
24.785 0.8660 0.9500

Sources