Datasets
-
ρg - Mass density, kg/m3 (2)
-
ρm,l - Amount density, mol/m3 (2)
-
Tboil - Boiling temperature at pressure P, K (2)
-
Vapor or sublimation pressure, kPa (2)
Mass density, kg/m3
[ref]
Fixed |
Measured |
Temperature, K - Gas |
Mole fraction of Benzene, chloro- (2) - Gas |
Mass density, kg/m3 - Gas |
323.15 |
0.0240 |
471.0 |
323.15 |
0.0293 |
507.0 |
323.15 |
0.2040 |
437.0 |
328.15 |
0.0240 |
441.0 |
328.15 |
0.0293 |
481.0 |
328.15 |
0.0352 |
516.0 |
328.15 |
0.0400 |
534.0 |
328.15 |
0.2040 |
406.0 |
333.15 |
0.0240 |
417.0 |
333.15 |
0.0293 |
458.0 |
333.15 |
0.0352 |
493.0 |
333.15 |
0.0400 |
516.0 |
333.15 |
0.0482 |
556.0 |
333.15 |
0.2040 |
386.0 |
Mass density, kg/m3
[ref]
Fixed |
Measured |
Temperature, K - Gas |
Mole fraction of Benzene, chloro- (2) - Gas |
Mass density, kg/m3 - Gas |
323.15 |
0.0240 |
471.0 |
323.15 |
0.0293 |
507.0 |
323.15 |
0.2040 |
437.0 |
328.15 |
0.0240 |
441.0 |
328.15 |
0.0293 |
481.0 |
328.15 |
0.0352 |
516.0 |
328.15 |
0.0400 |
534.0 |
328.15 |
0.2040 |
406.0 |
333.15 |
0.0240 |
417.0 |
333.15 |
0.0293 |
458.0 |
333.15 |
0.0352 |
493.0 |
333.15 |
0.0400 |
516.0 |
333.15 |
0.0482 |
556.0 |
333.15 |
0.2040 |
386.0 |
Amount density, mol/m3
[ref]
Operational condition: Mole fraction =
0.9 (Fluid (supercritical or subcritical phases))
Fixed |
Measured |
Temperature, K - Fluid (supercritical or subcritical phases) |
Pressure, kPa - Fluid (supercritical or subcritical phases) |
Amount density, mol/m3 - Fluid (supercritical or subcritical phases) |
313.20 |
4600.00 |
3020.0 |
313.20 |
6720.00 |
5840.0 |
313.20 |
7510.00 |
8030.0 |
313.20 |
7850.00 |
10140.0 |
313.20 |
8100.00 |
11950.0 |
313.20 |
8280.00 |
13540.0 |
313.20 |
9220.00 |
15760.0 |
323.20 |
4940.00 |
3020.0 |
323.20 |
7550.00 |
5840.0 |
323.20 |
8750.00 |
8030.0 |
323.20 |
9470.00 |
10140.0 |
323.20 |
9870.00 |
11950.0 |
323.20 |
10220.00 |
13540.0 |
323.20 |
11000.00 |
15760.0 |
333.20 |
5270.00 |
3020.0 |
333.20 |
8280.00 |
5840.0 |
333.20 |
9770.00 |
8030.0 |
333.20 |
10850.00 |
10140.0 |
333.20 |
11670.00 |
11950.0 |
333.20 |
12140.00 |
13540.0 |
333.20 |
14340.00 |
15760.0 |
343.20 |
5580.00 |
3020.0 |
343.20 |
8990.00 |
5840.0 |
343.20 |
10760.00 |
8030.0 |
343.20 |
12230.00 |
10140.0 |
343.20 |
13400.00 |
11950.0 |
343.20 |
14030.00 |
13540.0 |
343.20 |
18470.00 |
15760.0 |
353.20 |
5930.00 |
3020.0 |
353.20 |
9670.00 |
5840.0 |
353.20 |
11770.00 |
8030.0 |
353.20 |
13660.00 |
10140.0 |
353.20 |
15200.00 |
11950.0 |
353.20 |
16290.00 |
13540.0 |
353.20 |
22850.00 |
15760.0 |
363.20 |
6260.00 |
3020.0 |
363.20 |
10310.00 |
5840.0 |
363.20 |
12910.00 |
8030.0 |
363.20 |
15060.00 |
10140.0 |
363.20 |
16890.00 |
11950.0 |
363.20 |
19050.00 |
13540.0 |
363.20 |
27360.00 |
15760.0 |
373.20 |
6580.00 |
3020.0 |
373.20 |
10960.00 |
5840.0 |
373.20 |
14030.00 |
8030.0 |
373.20 |
16430.00 |
10140.0 |
373.20 |
18670.00 |
11950.0 |
373.20 |
22120.00 |
13540.0 |
373.20 |
31770.00 |
15760.0 |
383.20 |
6930.00 |
3020.0 |
383.20 |
11660.00 |
5840.0 |
383.20 |
15080.00 |
8030.0 |
383.20 |
17840.00 |
10140.0 |
383.20 |
20870.00 |
11950.0 |
383.20 |
25420.00 |
13540.0 |
383.20 |
36290.00 |
15760.0 |
393.20 |
7290.00 |
3020.0 |
393.20 |
12490.00 |
5840.0 |
393.20 |
16110.00 |
8030.0 |
393.20 |
19180.00 |
10140.0 |
393.20 |
23370.00 |
11950.0 |
393.20 |
28730.00 |
13540.0 |
393.20 |
40780.00 |
15760.0 |
Amount density, mol/m3
[ref]
Operational condition: Mole fraction =
0.9 (Fluid (supercritical or subcritical phases))
Fixed |
Measured |
Temperature, K - Fluid (supercritical or subcritical phases) |
Pressure, kPa - Fluid (supercritical or subcritical phases) |
Amount density, mol/m3 - Fluid (supercritical or subcritical phases) |
313.20 |
4600.00 |
3020.0 |
313.20 |
6720.00 |
5840.0 |
313.20 |
7510.00 |
8030.0 |
313.20 |
7850.00 |
10140.0 |
313.20 |
8100.00 |
11950.0 |
313.20 |
8280.00 |
13540.0 |
313.20 |
9220.00 |
15760.0 |
323.20 |
4940.00 |
3020.0 |
323.20 |
7550.00 |
5840.0 |
323.20 |
8750.00 |
8030.0 |
323.20 |
9470.00 |
10140.0 |
323.20 |
9870.00 |
11950.0 |
323.20 |
10220.00 |
13540.0 |
323.20 |
11000.00 |
15760.0 |
333.20 |
5270.00 |
3020.0 |
333.20 |
8280.00 |
5840.0 |
333.20 |
9770.00 |
8030.0 |
333.20 |
10850.00 |
10140.0 |
333.20 |
11670.00 |
11950.0 |
333.20 |
12140.00 |
13540.0 |
333.20 |
14340.00 |
15760.0 |
343.20 |
5580.00 |
3020.0 |
343.20 |
8990.00 |
5840.0 |
343.20 |
10760.00 |
8030.0 |
343.20 |
12230.00 |
10140.0 |
343.20 |
13400.00 |
11950.0 |
343.20 |
14030.00 |
13540.0 |
343.20 |
18470.00 |
15760.0 |
353.20 |
5930.00 |
3020.0 |
353.20 |
9670.00 |
5840.0 |
353.20 |
11770.00 |
8030.0 |
353.20 |
13660.00 |
10140.0 |
353.20 |
15200.00 |
11950.0 |
353.20 |
16290.00 |
13540.0 |
353.20 |
22850.00 |
15760.0 |
363.20 |
6260.00 |
3020.0 |
363.20 |
10310.00 |
5840.0 |
363.20 |
12910.00 |
8030.0 |
363.20 |
15060.00 |
10140.0 |
363.20 |
16890.00 |
11950.0 |
363.20 |
19050.00 |
13540.0 |
363.20 |
27360.00 |
15760.0 |
373.20 |
6580.00 |
3020.0 |
373.20 |
10960.00 |
5840.0 |
373.20 |
14030.00 |
8030.0 |
373.20 |
16430.00 |
10140.0 |
373.20 |
18670.00 |
11950.0 |
373.20 |
22120.00 |
13540.0 |
373.20 |
31770.00 |
15760.0 |
383.20 |
6930.00 |
3020.0 |
383.20 |
11660.00 |
5840.0 |
383.20 |
15080.00 |
8030.0 |
383.20 |
17840.00 |
10140.0 |
383.20 |
20870.00 |
11950.0 |
383.20 |
25420.00 |
13540.0 |
383.20 |
36290.00 |
15760.0 |
393.20 |
7290.00 |
3020.0 |
393.20 |
12490.00 |
5840.0 |
393.20 |
16110.00 |
8030.0 |
393.20 |
19180.00 |
10140.0 |
393.20 |
23370.00 |
11950.0 |
393.20 |
28730.00 |
13540.0 |
393.20 |
40780.00 |
15760.0 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Mole fraction =
0.9 (Gas)
Pressure, kPa - Gas |
Boiling temperature at pressure P, K - Gas |
11600.00 |
326.60 |
15100.00 |
349.00 |
19400.00 |
377.40 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Mole fraction =
0.9 (Gas)
Pressure, kPa - Gas |
Boiling temperature at pressure P, K - Gas |
11600.00 |
326.60 |
15100.00 |
349.00 |
19400.00 |
377.40 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Gas |
Mole fraction of Benzene, chloro- (2) - Gas |
Vapor or sublimation pressure, kPa - Gas |
323.15 |
0.0096 |
8550.00 |
323.15 |
0.0204 |
9300.00 |
323.15 |
0.0240 |
9340.00 |
323.15 |
0.0293 |
9360.00 |
328.15 |
0.0096 |
8600.00 |
328.15 |
0.0204 |
9780.00 |
328.15 |
0.0240 |
9880.00 |
328.15 |
0.0293 |
9960.00 |
328.15 |
0.0352 |
10000.00 |
328.15 |
0.0400 |
10030.00 |
333.15 |
0.0096 |
8650.00 |
333.15 |
0.0204 |
10200.00 |
333.15 |
0.0240 |
10370.00 |
333.15 |
0.0293 |
10520.00 |
333.15 |
0.0352 |
10580.00 |
333.15 |
0.0400 |
10650.00 |
333.15 |
0.0482 |
10680.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Gas |
Mole fraction of Benzene, chloro- (2) - Gas |
Vapor or sublimation pressure, kPa - Gas |
323.15 |
0.0096 |
8550.00 |
323.15 |
0.0204 |
9300.00 |
323.15 |
0.0240 |
9340.00 |
323.15 |
0.0293 |
9360.00 |
328.15 |
0.0096 |
8600.00 |
328.15 |
0.0204 |
9780.00 |
328.15 |
0.0240 |
9880.00 |
328.15 |
0.0293 |
9960.00 |
328.15 |
0.0352 |
10000.00 |
328.15 |
0.0400 |
10030.00 |
333.15 |
0.0096 |
8650.00 |
333.15 |
0.0204 |
10200.00 |
333.15 |
0.0240 |
10370.00 |
333.15 |
0.0293 |
10520.00 |
333.15 |
0.0352 |
10580.00 |
333.15 |
0.0400 |
10650.00 |
333.15 |
0.0482 |
10680.00 |
Sources