Mixture of Carbon dioxide + Hexanedioic acid, bis(2-methylpropyl) ester
Datasets
-
Pvap - Vapor or sublimation pressure, kPa (2)
-
ρg - Mass density, kg/m3 (2)
-
ρl - Mass density, kg/m3 (2)
-
Vapor or sublimation pressure, kPa (2)
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Hexanedioic acid, bis(2-methylpropyl) ester (2) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.0390 |
295.25 |
5770.00 |
0.0390 |
305.75 |
7210.00 |
0.0390 |
316.85 |
9210.00 |
0.0390 |
332.65 |
12960.00 |
0.0390 |
345.25 |
15650.00 |
0.0390 |
357.75 |
18120.00 |
0.0390 |
366.65 |
19640.00 |
0.0640 |
310.35 |
7900.00 |
0.0640 |
343.35 |
15060.00 |
0.0640 |
360.85 |
18370.00 |
0.0640 |
381.65 |
21810.00 |
0.0960 |
302.75 |
6520.00 |
0.0960 |
322.15 |
9790.00 |
0.0960 |
347.35 |
15170.00 |
0.0960 |
369.85 |
19330.00 |
0.0960 |
392.25 |
22710.00 |
0.0960 |
420.05 |
25670.00 |
0.1100 |
294.75 |
5350.00 |
0.1100 |
298.95 |
5870.00 |
0.1100 |
304.65 |
6550.00 |
0.1100 |
308.85 |
7170.00 |
0.1100 |
314.45 |
8030.00 |
0.1100 |
322.55 |
9480.00 |
0.1100 |
330.75 |
10930.00 |
0.1100 |
342.05 |
13130.00 |
0.1100 |
356.25 |
15790.00 |
0.1100 |
371.25 |
18400.00 |
0.1100 |
401.65 |
22750.00 |
0.1100 |
423.65 |
25120.00 |
0.1610 |
311.25 |
6480.00 |
0.1610 |
353.25 |
13680.00 |
0.1610 |
380.95 |
18160.00 |
0.1610 |
408.05 |
21540.00 |
0.1610 |
421.85 |
23060.00 |
0.2820 |
312.15 |
5490.00 |
0.2820 |
323.65 |
6590.00 |
0.2820 |
337.45 |
8100.00 |
0.2820 |
350.15 |
9620.00 |
0.2820 |
363.05 |
11140.00 |
0.2820 |
371.55 |
12100.00 |
0.2820 |
383.95 |
13550.00 |
0.2820 |
400.55 |
15340.00 |
0.2820 |
419.65 |
17200.00 |
0.5920 |
311.95 |
2490.00 |
0.5920 |
332.75 |
3490.00 |
0.5920 |
351.35 |
4320.00 |
0.5920 |
370.95 |
5350.00 |
0.5920 |
391.15 |
6250.00 |
0.5920 |
409.85 |
7000.00 |
0.5920 |
423.15 |
7660.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Hexanedioic acid, bis(2-methylpropyl) ester (2) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.0390 |
295.25 |
5770.00 |
0.0390 |
305.75 |
7210.00 |
0.0390 |
316.85 |
9210.00 |
0.0390 |
332.65 |
12960.00 |
0.0390 |
345.25 |
15650.00 |
0.0390 |
357.75 |
18120.00 |
0.0390 |
366.65 |
19640.00 |
0.0640 |
310.35 |
7900.00 |
0.0640 |
343.35 |
15060.00 |
0.0640 |
360.85 |
18370.00 |
0.0640 |
381.65 |
21810.00 |
0.0960 |
302.75 |
6520.00 |
0.0960 |
322.15 |
9790.00 |
0.0960 |
347.35 |
15170.00 |
0.0960 |
369.85 |
19330.00 |
0.0960 |
392.25 |
22710.00 |
0.0960 |
420.05 |
25670.00 |
0.1100 |
294.75 |
5350.00 |
0.1100 |
298.95 |
5870.00 |
0.1100 |
304.65 |
6550.00 |
0.1100 |
308.85 |
7170.00 |
0.1100 |
314.45 |
8030.00 |
0.1100 |
322.55 |
9480.00 |
0.1100 |
330.75 |
10930.00 |
0.1100 |
342.05 |
13130.00 |
0.1100 |
356.25 |
15790.00 |
0.1100 |
371.25 |
18400.00 |
0.1100 |
401.65 |
22750.00 |
0.1100 |
423.65 |
25120.00 |
0.1610 |
311.25 |
6480.00 |
0.1610 |
353.25 |
13680.00 |
0.1610 |
380.95 |
18160.00 |
0.1610 |
408.05 |
21540.00 |
0.1610 |
421.85 |
23060.00 |
0.2820 |
312.15 |
5490.00 |
0.2820 |
323.65 |
6590.00 |
0.2820 |
337.45 |
8100.00 |
0.2820 |
350.15 |
9620.00 |
0.2820 |
363.05 |
11140.00 |
0.2820 |
371.55 |
12100.00 |
0.2820 |
383.95 |
13550.00 |
0.2820 |
400.55 |
15340.00 |
0.2820 |
419.65 |
17200.00 |
0.5920 |
311.95 |
2490.00 |
0.5920 |
332.75 |
3490.00 |
0.5920 |
351.35 |
4320.00 |
0.5920 |
370.95 |
5350.00 |
0.5920 |
391.15 |
6250.00 |
0.5920 |
409.85 |
7000.00 |
0.5920 |
423.15 |
7660.00 |
Mass density, kg/m3
[ref]
Fixed |
Measured |
Mole fraction of Hexanedioic acid, bis(2-methylpropyl) ester (2) - Gas |
Temperature, K - Gas |
Mass density, kg/m3 - Gas |
0.0110 |
305.35 |
702.0 |
0.0110 |
311.05 |
667.0 |
0.0110 |
329.95 |
639.0 |
0.0110 |
357.45 |
558.0 |
0.0110 |
378.45 |
518.0 |
0.0110 |
404.55 |
471.0 |
0.0390 |
376.85 |
638.0 |
0.0390 |
401.45 |
588.0 |
0.0390 |
424.65 |
541.0 |
0.0640 |
400.05 |
655.0 |
0.0640 |
421.25 |
617.0 |
Mass density, kg/m3
[ref]
Fixed |
Measured |
Mole fraction of Hexanedioic acid, bis(2-methylpropyl) ester (2) - Gas |
Temperature, K - Gas |
Mass density, kg/m3 - Gas |
0.0110 |
305.35 |
702.0 |
0.0110 |
311.05 |
667.0 |
0.0110 |
329.95 |
639.0 |
0.0110 |
357.45 |
558.0 |
0.0110 |
378.45 |
518.0 |
0.0110 |
404.55 |
471.0 |
0.0390 |
376.85 |
638.0 |
0.0390 |
401.45 |
588.0 |
0.0390 |
424.65 |
541.0 |
0.0640 |
400.05 |
655.0 |
0.0640 |
421.25 |
617.0 |
Mass density, kg/m3
[ref]
Fixed |
Measured |
Mole fraction of Hexanedioic acid, bis(2-methylpropyl) ester (2) - Liquid |
Temperature, K - Liquid |
Mass density, kg/m3 - Liquid |
0.0390 |
295.25 |
795.0 |
0.0390 |
305.75 |
764.0 |
0.0390 |
316.85 |
739.0 |
0.0390 |
332.65 |
732.0 |
0.0390 |
345.25 |
702.0 |
0.0390 |
357.75 |
675.0 |
0.0390 |
366.65 |
660.0 |
0.0640 |
310.35 |
793.0 |
0.0640 |
343.35 |
762.0 |
0.0640 |
360.85 |
724.0 |
0.0640 |
381.65 |
687.0 |
0.0960 |
302.75 |
814.0 |
0.0960 |
322.15 |
800.0 |
0.0960 |
347.35 |
768.0 |
0.0960 |
369.85 |
731.0 |
0.0960 |
392.25 |
696.0 |
0.0960 |
420.05 |
651.0 |
0.1100 |
294.75 |
807.0 |
0.1100 |
298.95 |
805.0 |
0.1100 |
304.65 |
805.0 |
0.1100 |
308.85 |
791.0 |
0.1100 |
314.45 |
789.0 |
0.1100 |
322.55 |
791.0 |
0.1100 |
330.75 |
766.0 |
0.1100 |
342.05 |
756.0 |
0.1100 |
356.25 |
740.0 |
0.1100 |
371.25 |
723.0 |
0.1100 |
401.65 |
681.0 |
0.1100 |
423.65 |
650.0 |
0.1610 |
311.25 |
865.0 |
0.1610 |
353.25 |
791.0 |
0.1610 |
380.95 |
760.0 |
0.1610 |
408.05 |
721.0 |
0.1610 |
421.85 |
706.0 |
0.2820 |
312.15 |
853.0 |
0.2820 |
323.65 |
832.0 |
0.2820 |
337.45 |
821.0 |
0.2820 |
350.15 |
810.0 |
0.2820 |
363.05 |
800.0 |
0.2820 |
371.55 |
791.0 |
0.2820 |
383.95 |
776.0 |
0.2820 |
400.55 |
760.0 |
0.2820 |
419.65 |
740.0 |
0.5920 |
311.95 |
813.0 |
0.5920 |
332.75 |
829.0 |
0.5920 |
351.35 |
819.0 |
0.5920 |
370.95 |
807.0 |
0.5920 |
391.15 |
790.0 |
0.5920 |
409.85 |
777.0 |
0.5920 |
423.15 |
772.0 |
Mass density, kg/m3
[ref]
Fixed |
Measured |
Mole fraction of Hexanedioic acid, bis(2-methylpropyl) ester (2) - Liquid |
Temperature, K - Liquid |
Mass density, kg/m3 - Liquid |
0.0390 |
295.25 |
795.0 |
0.0390 |
305.75 |
764.0 |
0.0390 |
316.85 |
739.0 |
0.0390 |
332.65 |
732.0 |
0.0390 |
345.25 |
702.0 |
0.0390 |
357.75 |
675.0 |
0.0390 |
366.65 |
660.0 |
0.0640 |
310.35 |
793.0 |
0.0640 |
343.35 |
762.0 |
0.0640 |
360.85 |
724.0 |
0.0640 |
381.65 |
687.0 |
0.0960 |
302.75 |
814.0 |
0.0960 |
322.15 |
800.0 |
0.0960 |
347.35 |
768.0 |
0.0960 |
369.85 |
731.0 |
0.0960 |
392.25 |
696.0 |
0.0960 |
420.05 |
651.0 |
0.1100 |
294.75 |
807.0 |
0.1100 |
298.95 |
805.0 |
0.1100 |
304.65 |
805.0 |
0.1100 |
308.85 |
791.0 |
0.1100 |
314.45 |
789.0 |
0.1100 |
322.55 |
791.0 |
0.1100 |
330.75 |
766.0 |
0.1100 |
342.05 |
756.0 |
0.1100 |
356.25 |
740.0 |
0.1100 |
371.25 |
723.0 |
0.1100 |
401.65 |
681.0 |
0.1100 |
423.65 |
650.0 |
0.1610 |
311.25 |
865.0 |
0.1610 |
353.25 |
791.0 |
0.1610 |
380.95 |
760.0 |
0.1610 |
408.05 |
721.0 |
0.1610 |
421.85 |
706.0 |
0.2820 |
312.15 |
853.0 |
0.2820 |
323.65 |
832.0 |
0.2820 |
337.45 |
821.0 |
0.2820 |
350.15 |
810.0 |
0.2820 |
363.05 |
800.0 |
0.2820 |
371.55 |
791.0 |
0.2820 |
383.95 |
776.0 |
0.2820 |
400.55 |
760.0 |
0.2820 |
419.65 |
740.0 |
0.5920 |
311.95 |
813.0 |
0.5920 |
332.75 |
829.0 |
0.5920 |
351.35 |
819.0 |
0.5920 |
370.95 |
807.0 |
0.5920 |
391.15 |
790.0 |
0.5920 |
409.85 |
777.0 |
0.5920 |
423.15 |
772.0 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Hexanedioic acid, bis(2-methylpropyl) ester (2) - Gas |
Temperature, K - Gas |
Vapor or sublimation pressure, kPa - Gas |
0.0110 |
305.35 |
7520.00 |
0.0110 |
311.05 |
8280.00 |
0.0110 |
329.95 |
13030.00 |
0.0110 |
357.45 |
17030.00 |
0.0110 |
378.45 |
19570.00 |
0.0110 |
404.55 |
21850.00 |
0.0390 |
376.85 |
21300.00 |
0.0390 |
401.45 |
24360.00 |
0.0390 |
424.65 |
26120.00 |
0.0640 |
400.05 |
24320.00 |
0.0640 |
421.25 |
26600.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Hexanedioic acid, bis(2-methylpropyl) ester (2) - Gas |
Temperature, K - Gas |
Vapor or sublimation pressure, kPa - Gas |
0.0110 |
305.35 |
7520.00 |
0.0110 |
311.05 |
8280.00 |
0.0110 |
329.95 |
13030.00 |
0.0110 |
357.45 |
17030.00 |
0.0110 |
378.45 |
19570.00 |
0.0110 |
404.55 |
21850.00 |
0.0390 |
376.85 |
21300.00 |
0.0390 |
401.45 |
24360.00 |
0.0390 |
424.65 |
26120.00 |
0.0640 |
400.05 |
24320.00 |
0.0640 |
421.25 |
26600.00 |
Sources