Datasets
-
Pc - Critical pressure, kPa (2)
-
Pvap - Vapor or sublimation pressure, kPa (6)
-
ρc - Critical density, kg/m3 (2)
-
ρg - Mass density, kg/m3 (4)
-
ρl - Mass density, kg/m3 (2)
-
Tc - Critical temperature, K (2)
-
Binary diffusion coefficient, m2/s (2)
-
Vapor or sublimation pressure, kPa (8)
Critical pressure, kPa
[ref]
| Mole fraction of Styrene (1) - Liquid |
Critical pressure, kPa - Liquid |
| 0.0225 |
8900.00 |
| 0.0363 |
9750.00 |
| 0.0488 |
10440.00 |
Critical pressure, kPa
[ref]
| Mole fraction of Styrene (1) - Liquid |
Critical pressure, kPa - Liquid |
| 0.0225 |
8900.00 |
| 0.0363 |
9750.00 |
| 0.0488 |
10440.00 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of Carbon dioxide (2) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
| 308.20 |
0.2010 |
2690.00 |
| 308.20 |
0.2980 |
3410.00 |
| 308.20 |
0.3740 |
4170.00 |
| 308.20 |
0.4510 |
4870.00 |
| 308.20 |
0.5450 |
5670.00 |
| 308.20 |
0.6200 |
6030.00 |
| 308.20 |
0.7510 |
6560.00 |
| 308.20 |
0.7990 |
6690.00 |
| 308.20 |
0.8290 |
6770.00 |
| 308.20 |
0.8550 |
6860.00 |
| 308.20 |
0.8840 |
6970.00 |
| 308.20 |
0.9120 |
7100.00 |
| 308.20 |
0.9320 |
7190.00 |
| 308.20 |
0.9480 |
7320.00 |
| 308.20 |
0.9660 |
7540.00 |
| 308.20 |
0.9840 |
7830.00 |
| 318.20 |
0.2010 |
3010.00 |
| 318.20 |
0.2980 |
3940.00 |
| 318.20 |
0.3740 |
4830.00 |
| 318.20 |
0.4510 |
5650.00 |
| 318.20 |
0.5450 |
6650.00 |
| 318.20 |
0.6200 |
7160.00 |
| 318.20 |
0.7510 |
7750.00 |
| 318.20 |
0.7990 |
7990.00 |
| 318.20 |
0.8290 |
8110.00 |
| 318.20 |
0.8550 |
8220.00 |
| 318.20 |
0.8840 |
8380.00 |
| 318.20 |
0.9120 |
8540.00 |
| 318.20 |
0.9320 |
8680.00 |
| 318.20 |
0.9480 |
8760.00 |
| 318.20 |
0.9660 |
8890.00 |
| 328.20 |
0.2010 |
3360.00 |
| 328.20 |
0.2980 |
4510.00 |
| 328.20 |
0.3740 |
5430.00 |
| 328.20 |
0.4510 |
6410.00 |
| 328.20 |
0.5450 |
7570.00 |
| 328.20 |
0.6200 |
8230.00 |
| 328.20 |
0.7510 |
9160.00 |
| 328.20 |
0.7990 |
9420.00 |
| 328.20 |
0.8290 |
9580.00 |
| 328.20 |
0.8550 |
9730.00 |
| 328.20 |
0.8840 |
9840.00 |
| 328.20 |
0.9120 |
10040.00 |
| 328.20 |
0.9320 |
10150.00 |
| 333.20 |
0.2010 |
3610.00 |
| 333.20 |
0.2980 |
5080.00 |
| 333.20 |
0.3740 |
5800.00 |
| 333.20 |
0.4510 |
6840.00 |
| 333.20 |
0.5450 |
8090.00 |
| 333.20 |
0.6200 |
8820.00 |
| 333.20 |
0.7510 |
9850.00 |
| 333.20 |
0.7990 |
10210.00 |
| 333.20 |
0.8290 |
10340.00 |
| 333.20 |
0.8550 |
10540.00 |
| 333.20 |
0.8840 |
10710.00 |
| 333.20 |
0.9120 |
10830.00 |
| 333.20 |
0.9320 |
10890.00 |
| 343.20 |
0.2010 |
4000.00 |
| 343.20 |
0.2980 |
5450.00 |
| 343.20 |
0.3740 |
6400.00 |
| 343.20 |
0.4510 |
7600.00 |
| 343.20 |
0.5450 |
9060.00 |
| 343.20 |
0.6200 |
10090.00 |
| 343.20 |
0.7510 |
11370.00 |
| 343.20 |
0.7990 |
11780.00 |
| 343.20 |
0.8290 |
11960.00 |
| 343.20 |
0.8550 |
12150.00 |
| 343.20 |
0.8840 |
12290.00 |
| 343.20 |
0.9120 |
12450.00 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Mole fraction of Styrene (1) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
| 0.0225 |
303.20 |
6890.00 |
| 0.0225 |
308.20 |
7590.00 |
| 0.0225 |
313.20 |
8230.00 |
| 0.0225 |
318.20 |
8860.00 |
| 0.0363 |
303.20 |
6770.00 |
| 0.0363 |
308.20 |
7380.00 |
| 0.0363 |
313.20 |
8130.00 |
| 0.0363 |
318.20 |
8750.00 |
| 0.0363 |
323.20 |
9430.00 |
| 0.0488 |
303.20 |
6590.00 |
| 0.0488 |
308.20 |
7240.00 |
| 0.0488 |
313.20 |
8020.00 |
| 0.0488 |
318.20 |
8610.00 |
| 0.0488 |
323.20 |
9290.00 |
| 0.0488 |
328.20 |
10090.00 |
| 0.0742 |
303.20 |
6540.00 |
| 0.0742 |
308.20 |
7150.00 |
| 0.0742 |
313.20 |
7840.00 |
| 0.0742 |
318.20 |
8530.00 |
| 0.0742 |
323.20 |
9260.00 |
| 0.0742 |
328.20 |
10030.00 |
| 0.0742 |
333.20 |
10720.00 |
| 0.1010 |
303.20 |
6390.00 |
| 0.1010 |
308.20 |
7000.00 |
| 0.1010 |
313.20 |
7700.00 |
| 0.1010 |
318.20 |
8430.00 |
| 0.1010 |
323.20 |
9190.00 |
| 0.1010 |
328.20 |
9890.00 |
| 0.1010 |
333.20 |
10670.00 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of Carbon dioxide (2) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
| 303.00 |
0.6140 |
5470.00 |
| 303.00 |
0.7080 |
5490.00 |
| 303.00 |
0.7840 |
5630.00 |
| 303.00 |
0.8770 |
5940.00 |
| 303.00 |
0.9370 |
6180.00 |
| 303.00 |
0.9520 |
6440.00 |
| 313.00 |
0.6140 |
6480.00 |
| 313.00 |
0.7080 |
6820.00 |
| 313.00 |
0.7840 |
6940.00 |
| 313.00 |
0.8770 |
7310.00 |
| 313.00 |
0.9370 |
7490.00 |
| 313.00 |
0.9520 |
7770.00 |
| 323.00 |
0.6140 |
7580.00 |
| 323.00 |
0.7080 |
8050.00 |
| 323.00 |
0.7840 |
8290.00 |
| 323.00 |
0.8770 |
8790.00 |
| 323.00 |
0.9370 |
9060.00 |
| 333.00 |
0.6140 |
8720.00 |
| 333.00 |
0.7080 |
9360.00 |
| 333.00 |
0.7840 |
9820.00 |
| 333.00 |
0.8770 |
10310.00 |
| 343.00 |
0.6140 |
9900.00 |
| 343.00 |
0.7080 |
10820.00 |
| 343.00 |
0.7840 |
11440.00 |
| 343.00 |
0.8770 |
12130.00 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of Carbon dioxide (2) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
| 308.20 |
0.2010 |
2690.00 |
| 308.20 |
0.2980 |
3410.00 |
| 308.20 |
0.3740 |
4170.00 |
| 308.20 |
0.4510 |
4870.00 |
| 308.20 |
0.5450 |
5670.00 |
| 308.20 |
0.6200 |
6030.00 |
| 308.20 |
0.7510 |
6560.00 |
| 308.20 |
0.7990 |
6690.00 |
| 308.20 |
0.8290 |
6770.00 |
| 308.20 |
0.8550 |
6860.00 |
| 308.20 |
0.8840 |
6970.00 |
| 308.20 |
0.9120 |
7100.00 |
| 308.20 |
0.9320 |
7190.00 |
| 308.20 |
0.9480 |
7320.00 |
| 308.20 |
0.9660 |
7540.00 |
| 308.20 |
0.9840 |
7830.00 |
| 318.20 |
0.2010 |
3010.00 |
| 318.20 |
0.2980 |
3940.00 |
| 318.20 |
0.3740 |
4830.00 |
| 318.20 |
0.4510 |
5650.00 |
| 318.20 |
0.5450 |
6650.00 |
| 318.20 |
0.6200 |
7160.00 |
| 318.20 |
0.7510 |
7750.00 |
| 318.20 |
0.7990 |
7990.00 |
| 318.20 |
0.8290 |
8110.00 |
| 318.20 |
0.8550 |
8220.00 |
| 318.20 |
0.8840 |
8380.00 |
| 318.20 |
0.9120 |
8540.00 |
| 318.20 |
0.9320 |
8680.00 |
| 318.20 |
0.9480 |
8760.00 |
| 318.20 |
0.9660 |
8890.00 |
| 328.20 |
0.2010 |
3360.00 |
| 328.20 |
0.2980 |
4510.00 |
| 328.20 |
0.3740 |
5430.00 |
| 328.20 |
0.4510 |
6410.00 |
| 328.20 |
0.5450 |
7570.00 |
| 328.20 |
0.6200 |
8230.00 |
| 328.20 |
0.7510 |
9160.00 |
| 328.20 |
0.7990 |
9420.00 |
| 328.20 |
0.8290 |
9580.00 |
| 328.20 |
0.8550 |
9730.00 |
| 328.20 |
0.8840 |
9840.00 |
| 328.20 |
0.9120 |
10040.00 |
| 328.20 |
0.9320 |
10150.00 |
| 333.20 |
0.2010 |
3610.00 |
| 333.20 |
0.2980 |
5080.00 |
| 333.20 |
0.3740 |
5800.00 |
| 333.20 |
0.4510 |
6840.00 |
| 333.20 |
0.5450 |
8090.00 |
| 333.20 |
0.6200 |
8820.00 |
| 333.20 |
0.7510 |
9850.00 |
| 333.20 |
0.7990 |
10210.00 |
| 333.20 |
0.8290 |
10340.00 |
| 333.20 |
0.8550 |
10540.00 |
| 333.20 |
0.8840 |
10710.00 |
| 333.20 |
0.9120 |
10830.00 |
| 333.20 |
0.9320 |
10890.00 |
| 343.20 |
0.2010 |
4000.00 |
| 343.20 |
0.2980 |
5450.00 |
| 343.20 |
0.3740 |
6400.00 |
| 343.20 |
0.4510 |
7600.00 |
| 343.20 |
0.5450 |
9060.00 |
| 343.20 |
0.6200 |
10090.00 |
| 343.20 |
0.7510 |
11370.00 |
| 343.20 |
0.7990 |
11780.00 |
| 343.20 |
0.8290 |
11960.00 |
| 343.20 |
0.8550 |
12150.00 |
| 343.20 |
0.8840 |
12290.00 |
| 343.20 |
0.9120 |
12450.00 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Mole fraction of Styrene (1) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
| 0.0225 |
303.20 |
6890.00 |
| 0.0225 |
308.20 |
7590.00 |
| 0.0225 |
313.20 |
8230.00 |
| 0.0225 |
318.20 |
8860.00 |
| 0.0363 |
303.20 |
6770.00 |
| 0.0363 |
308.20 |
7380.00 |
| 0.0363 |
313.20 |
8130.00 |
| 0.0363 |
318.20 |
8750.00 |
| 0.0363 |
323.20 |
9430.00 |
| 0.0488 |
303.20 |
6590.00 |
| 0.0488 |
308.20 |
7240.00 |
| 0.0488 |
313.20 |
8020.00 |
| 0.0488 |
318.20 |
8610.00 |
| 0.0488 |
323.20 |
9290.00 |
| 0.0488 |
328.20 |
10090.00 |
| 0.0742 |
303.20 |
6540.00 |
| 0.0742 |
308.20 |
7150.00 |
| 0.0742 |
313.20 |
7840.00 |
| 0.0742 |
318.20 |
8530.00 |
| 0.0742 |
323.20 |
9260.00 |
| 0.0742 |
328.20 |
10030.00 |
| 0.0742 |
333.20 |
10720.00 |
| 0.1010 |
303.20 |
6390.00 |
| 0.1010 |
308.20 |
7000.00 |
| 0.1010 |
313.20 |
7700.00 |
| 0.1010 |
318.20 |
8430.00 |
| 0.1010 |
323.20 |
9190.00 |
| 0.1010 |
328.20 |
9890.00 |
| 0.1010 |
333.20 |
10670.00 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of Carbon dioxide (2) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
| 303.00 |
0.6140 |
5470.00 |
| 303.00 |
0.7080 |
5490.00 |
| 303.00 |
0.7840 |
5630.00 |
| 303.00 |
0.8770 |
5940.00 |
| 303.00 |
0.9370 |
6180.00 |
| 303.00 |
0.9520 |
6440.00 |
| 313.00 |
0.6140 |
6480.00 |
| 313.00 |
0.7080 |
6820.00 |
| 313.00 |
0.7840 |
6940.00 |
| 313.00 |
0.8770 |
7310.00 |
| 313.00 |
0.9370 |
7490.00 |
| 313.00 |
0.9520 |
7770.00 |
| 323.00 |
0.6140 |
7580.00 |
| 323.00 |
0.7080 |
8050.00 |
| 323.00 |
0.7840 |
8290.00 |
| 323.00 |
0.8770 |
8790.00 |
| 323.00 |
0.9370 |
9060.00 |
| 333.00 |
0.6140 |
8720.00 |
| 333.00 |
0.7080 |
9360.00 |
| 333.00 |
0.7840 |
9820.00 |
| 333.00 |
0.8770 |
10310.00 |
| 343.00 |
0.6140 |
9900.00 |
| 343.00 |
0.7080 |
10820.00 |
| 343.00 |
0.7840 |
11440.00 |
| 343.00 |
0.8770 |
12130.00 |
Critical density, kg/m3
[ref]
| Mole fraction of Styrene (1) - Liquid |
Critical density, kg/m3 - Liquid |
| 0.0211 |
504.0 |
| 0.0384 |
546.0 |
| 0.0512 |
560.0 |
| 0.0637 |
590.0 |
Critical density, kg/m3
[ref]
| Mole fraction of Styrene (1) - Liquid |
Critical density, kg/m3 - Liquid |
| 0.0211 |
504.0 |
| 0.0384 |
546.0 |
| 0.0512 |
560.0 |
| 0.0637 |
590.0 |
Mass density, kg/m3
[ref]
| Fixed |
Measured |
| Temperature, K - Gas |
Mole fraction of Styrene (1) - Gas |
Mass density, kg/m3 - Gas |
| 323.15 |
0.0182 |
479.0 |
| 323.15 |
0.0256 |
494.0 |
| 323.15 |
0.0300 |
521.0 |
| 328.15 |
0.0182 |
450.0 |
| 328.15 |
0.0256 |
471.0 |
| 328.15 |
0.0300 |
499.0 |
| 328.15 |
0.0343 |
529.0 |
| 328.15 |
0.0393 |
547.0 |
| 328.15 |
0.0476 |
580.0 |
| 333.15 |
0.0182 |
430.0 |
| 333.15 |
0.0256 |
453.0 |
| 333.15 |
0.0300 |
479.0 |
| 333.15 |
0.0343 |
507.0 |
| 333.15 |
0.0393 |
527.0 |
| 333.15 |
0.0476 |
560.0 |
Mass density, kg/m3
[ref]
| Fixed |
Measured |
| Mole fraction of Styrene (1) - Gas |
Temperature, K - Gas |
Mass density, kg/m3 - Gas |
| 0.0225 |
321.20 |
500.0 |
| 0.0363 |
330.20 |
527.0 |
| 0.0488 |
333.20 |
570.0 |
Mass density, kg/m3
[ref]
| Fixed |
Measured |
| Temperature, K - Gas |
Mole fraction of Styrene (1) - Gas |
Mass density, kg/m3 - Gas |
| 323.15 |
0.0182 |
479.0 |
| 323.15 |
0.0256 |
494.0 |
| 323.15 |
0.0300 |
521.0 |
| 328.15 |
0.0182 |
450.0 |
| 328.15 |
0.0256 |
471.0 |
| 328.15 |
0.0300 |
499.0 |
| 328.15 |
0.0343 |
529.0 |
| 328.15 |
0.0393 |
547.0 |
| 328.15 |
0.0476 |
580.0 |
| 333.15 |
0.0182 |
430.0 |
| 333.15 |
0.0256 |
453.0 |
| 333.15 |
0.0300 |
479.0 |
| 333.15 |
0.0343 |
507.0 |
| 333.15 |
0.0393 |
527.0 |
| 333.15 |
0.0476 |
560.0 |
Mass density, kg/m3
[ref]
| Fixed |
Measured |
| Mole fraction of Styrene (1) - Gas |
Temperature, K - Gas |
Mass density, kg/m3 - Gas |
| 0.0225 |
321.20 |
500.0 |
| 0.0363 |
330.20 |
527.0 |
| 0.0488 |
333.20 |
570.0 |
Mass density, kg/m3
[ref]
| Fixed |
Measured |
| Mole fraction of Styrene (1) - Liquid |
Temperature, K - Liquid |
Mass density, kg/m3 - Liquid |
| 0.0225 |
303.20 |
721.0 |
| 0.0225 |
308.20 |
675.0 |
| 0.0225 |
313.20 |
615.0 |
| 0.0225 |
318.20 |
529.0 |
| 0.0363 |
303.20 |
755.0 |
| 0.0363 |
308.20 |
721.0 |
| 0.0363 |
313.20 |
683.0 |
| 0.0363 |
318.20 |
635.0 |
| 0.0363 |
323.20 |
582.0 |
| 0.0488 |
303.20 |
774.0 |
| 0.0488 |
308.20 |
747.0 |
| 0.0488 |
313.20 |
711.0 |
| 0.0488 |
318.20 |
682.0 |
| 0.0488 |
323.20 |
645.0 |
| 0.0488 |
328.20 |
608.0 |
| 0.0742 |
303.20 |
805.0 |
| 0.0742 |
308.20 |
781.0 |
| 0.0742 |
313.20 |
758.0 |
| 0.0742 |
318.20 |
734.0 |
| 0.0742 |
323.20 |
711.0 |
| 0.0742 |
328.20 |
685.0 |
| 0.0742 |
333.20 |
663.0 |
| 0.1010 |
303.20 |
831.0 |
| 0.1010 |
308.20 |
813.0 |
| 0.1010 |
313.20 |
794.0 |
| 0.1010 |
318.20 |
774.0 |
| 0.1010 |
323.20 |
755.0 |
| 0.1010 |
328.20 |
733.0 |
| 0.1010 |
333.20 |
713.0 |
Mass density, kg/m3
[ref]
| Fixed |
Measured |
| Mole fraction of Styrene (1) - Liquid |
Temperature, K - Liquid |
Mass density, kg/m3 - Liquid |
| 0.0225 |
303.20 |
721.0 |
| 0.0225 |
308.20 |
675.0 |
| 0.0225 |
313.20 |
615.0 |
| 0.0225 |
318.20 |
529.0 |
| 0.0363 |
303.20 |
755.0 |
| 0.0363 |
308.20 |
721.0 |
| 0.0363 |
313.20 |
683.0 |
| 0.0363 |
318.20 |
635.0 |
| 0.0363 |
323.20 |
582.0 |
| 0.0488 |
303.20 |
774.0 |
| 0.0488 |
308.20 |
747.0 |
| 0.0488 |
313.20 |
711.0 |
| 0.0488 |
318.20 |
682.0 |
| 0.0488 |
323.20 |
645.0 |
| 0.0488 |
328.20 |
608.0 |
| 0.0742 |
303.20 |
805.0 |
| 0.0742 |
308.20 |
781.0 |
| 0.0742 |
313.20 |
758.0 |
| 0.0742 |
318.20 |
734.0 |
| 0.0742 |
323.20 |
711.0 |
| 0.0742 |
328.20 |
685.0 |
| 0.0742 |
333.20 |
663.0 |
| 0.1010 |
303.20 |
831.0 |
| 0.1010 |
308.20 |
813.0 |
| 0.1010 |
313.20 |
794.0 |
| 0.1010 |
318.20 |
774.0 |
| 0.1010 |
323.20 |
755.0 |
| 0.1010 |
328.20 |
733.0 |
| 0.1010 |
333.20 |
713.0 |
Critical temperature, K
[ref]
| Mole fraction of Styrene (1) - Liquid |
Critical temperature, K - Liquid |
| 0.0225 |
318.80 |
| 0.0363 |
325.70 |
| 0.0488 |
331.00 |
Critical temperature, K
[ref]
| Mole fraction of Styrene (1) - Liquid |
Critical temperature, K - Liquid |
| 0.0225 |
318.80 |
| 0.0363 |
325.70 |
| 0.0488 |
331.00 |
Binary diffusion coefficient, m2/s
[ref]
Operational condition: Mole fraction =
0 (Fluid (supercritical or subcritical phases))
| Fixed |
Measured |
| Temperature, K - Fluid (supercritical or subcritical phases) |
Pressure, kPa - Fluid (supercritical or subcritical phases) |
Binary diffusion coefficient, m2/s - Fluid (supercritical or subcritical phases) |
| 313.16 |
15000.00 |
1.1950e-08 |
| 313.16 |
20000.00 |
1.0750e-08 |
| 313.16 |
25000.00 |
0.0000 |
| 313.16 |
30000.00 |
0.0000 |
| 313.16 |
35000.00 |
0.0000 |
| 323.16 |
15000.00 |
1.3170e-08 |
| 323.16 |
20000.00 |
1.1180e-08 |
| 323.16 |
25000.00 |
1.0550e-08 |
| 323.16 |
30000.00 |
0.0000 |
| 323.16 |
35000.00 |
0.0000 |
| 333.16 |
15000.00 |
1.5500e-08 |
| 333.16 |
20000.00 |
1.4090e-08 |
| 333.16 |
25000.00 |
1.2200e-08 |
| 333.16 |
30000.00 |
1.0900e-08 |
| 333.16 |
35000.00 |
1.0230e-08 |
Binary diffusion coefficient, m2/s
[ref]
Operational condition: Mole fraction =
0 (Fluid (supercritical or subcritical phases))
| Fixed |
Measured |
| Temperature, K - Fluid (supercritical or subcritical phases) |
Pressure, kPa - Fluid (supercritical or subcritical phases) |
Binary diffusion coefficient, m2/s - Fluid (supercritical or subcritical phases) |
| 313.16 |
15000.00 |
1.1950e-08 |
| 313.16 |
20000.00 |
1.0750e-08 |
| 313.16 |
25000.00 |
0.0000 |
| 313.16 |
30000.00 |
0.0000 |
| 313.16 |
35000.00 |
0.0000 |
| 323.16 |
15000.00 |
1.3170e-08 |
| 323.16 |
20000.00 |
1.1180e-08 |
| 323.16 |
25000.00 |
1.0550e-08 |
| 323.16 |
30000.00 |
0.0000 |
| 323.16 |
35000.00 |
0.0000 |
| 333.16 |
15000.00 |
1.5500e-08 |
| 333.16 |
20000.00 |
1.4090e-08 |
| 333.16 |
25000.00 |
1.2200e-08 |
| 333.16 |
30000.00 |
1.0900e-08 |
| 333.16 |
35000.00 |
1.0230e-08 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Temperature, K - Gas |
Mole fraction of Styrene (1) - Gas |
Vapor or sublimation pressure, kPa - Gas |
| 323.15 |
0.0093 |
8780.00 |
| 323.15 |
0.0182 |
9350.00 |
| 323.15 |
0.0256 |
9430.00 |
| 323.15 |
0.0300 |
9460.00 |
| 328.15 |
0.0093 |
8940.00 |
| 328.15 |
0.0182 |
9880.00 |
| 328.15 |
0.0256 |
10050.00 |
| 328.15 |
0.0300 |
10060.00 |
| 328.15 |
0.0343 |
10080.00 |
| 328.15 |
0.0393 |
10100.00 |
| 328.15 |
0.0476 |
10120.00 |
| 333.15 |
0.0093 |
9000.00 |
| 333.15 |
0.0182 |
10400.00 |
| 333.15 |
0.0256 |
10640.00 |
| 333.15 |
0.0300 |
10680.00 |
| 333.15 |
0.0343 |
10710.00 |
| 333.15 |
0.0393 |
10770.00 |
| 333.15 |
0.0476 |
10840.00 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Temperature, K - Gas |
Mole fraction of Carbon dioxide (2) - Gas |
Vapor or sublimation pressure, kPa - Gas |
| 308.20 |
0.9950 |
7810.00 |
| 318.20 |
0.9840 |
8880.00 |
| 318.20 |
0.9910 |
8450.00 |
| 328.20 |
0.9480 |
10240.00 |
| 328.20 |
0.9660 |
10110.00 |
| 328.20 |
0.9910 |
8960.00 |
| 333.20 |
0.9480 |
10920.00 |
| 333.20 |
0.9660 |
10650.00 |
| 333.20 |
0.9910 |
9150.00 |
| 343.20 |
0.9320 |
12300.00 |
| 343.20 |
0.9480 |
12240.00 |
| 343.20 |
0.9660 |
11860.00 |
| 343.20 |
0.9910 |
9490.00 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Mole fraction of Styrene (1) - Gas |
Temperature, K - Gas |
Vapor or sublimation pressure, kPa - Gas |
| 0.0225 |
321.20 |
9200.00 |
| 0.0363 |
330.20 |
10300.00 |
| 0.0488 |
333.20 |
10730.00 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Temperature, K - Gas |
Mole fraction of Carbon dioxide (2) - Gas |
Vapor or sublimation pressure, kPa - Gas |
| 333.00 |
0.9370 |
10600.00 |
| 333.00 |
0.9520 |
10640.00 |
| 343.00 |
0.9370 |
12190.00 |
| 343.00 |
0.9520 |
12170.00 |
| 323.00 |
0.9520 |
9260.00 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Temperature, K - Gas |
Mole fraction of Styrene (1) - Gas |
Vapor or sublimation pressure, kPa - Gas |
| 323.15 |
0.0093 |
8780.00 |
| 323.15 |
0.0182 |
9350.00 |
| 323.15 |
0.0256 |
9430.00 |
| 323.15 |
0.0300 |
9460.00 |
| 328.15 |
0.0093 |
8940.00 |
| 328.15 |
0.0182 |
9880.00 |
| 328.15 |
0.0256 |
10050.00 |
| 328.15 |
0.0300 |
10060.00 |
| 328.15 |
0.0343 |
10080.00 |
| 328.15 |
0.0393 |
10100.00 |
| 328.15 |
0.0476 |
10120.00 |
| 333.15 |
0.0093 |
9000.00 |
| 333.15 |
0.0182 |
10400.00 |
| 333.15 |
0.0256 |
10640.00 |
| 333.15 |
0.0300 |
10680.00 |
| 333.15 |
0.0343 |
10710.00 |
| 333.15 |
0.0393 |
10770.00 |
| 333.15 |
0.0476 |
10840.00 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Temperature, K - Gas |
Mole fraction of Carbon dioxide (2) - Gas |
Vapor or sublimation pressure, kPa - Gas |
| 308.20 |
0.9950 |
7810.00 |
| 318.20 |
0.9840 |
8880.00 |
| 318.20 |
0.9910 |
8450.00 |
| 328.20 |
0.9480 |
10240.00 |
| 328.20 |
0.9660 |
10110.00 |
| 328.20 |
0.9910 |
8960.00 |
| 333.20 |
0.9480 |
10920.00 |
| 333.20 |
0.9660 |
10650.00 |
| 333.20 |
0.9910 |
9150.00 |
| 343.20 |
0.9320 |
12300.00 |
| 343.20 |
0.9480 |
12240.00 |
| 343.20 |
0.9660 |
11860.00 |
| 343.20 |
0.9910 |
9490.00 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Mole fraction of Styrene (1) - Gas |
Temperature, K - Gas |
Vapor or sublimation pressure, kPa - Gas |
| 0.0225 |
321.20 |
9200.00 |
| 0.0363 |
330.20 |
10300.00 |
| 0.0488 |
333.20 |
10730.00 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Temperature, K - Gas |
Mole fraction of Carbon dioxide (2) - Gas |
Vapor or sublimation pressure, kPa - Gas |
| 333.00 |
0.9370 |
10600.00 |
| 333.00 |
0.9520 |
10640.00 |
| 343.00 |
0.9370 |
12190.00 |
| 343.00 |
0.9520 |
12170.00 |
| 323.00 |
0.9520 |
9260.00 |
Sources
-
Solubility of chlorobutane, ethyl methacrylate and trifluoroethyl acrylate in supercritical carbon dioxide
-
Vapour-liquid phase boundaries including the near critical regions of the (CO2 + styrene, CO2 + 1,4-dioxane, and CO2 + N,N-dimethylformamide) systems
-
Phase Behaviors, Density, and Isothermal Compressibility of Styrene + CO2, Ethylbenzene + CO2, and Ethylbezene + Styrene + CO2 Systems
-
Phase Equilibria of the Systems CO2 + Styrene, CO2 + Safrole, and CO2 + Styrene + Safrole
-
Limiting Binary Diffusivities of Aniline, Styrene, and Mesitylene in Supercritical Carbon Dioxide
