- Name
- Carbon dioxide
- InChI
- InChI=1S/CO2/c2-1-3
- InChI Key
- CURLTUGMZLYLDI-UHFFFAOYSA-N
- Formula
- CO2
- SMILES
- O=C=O
- Mol. Weight (g/mol)
- 44.01
- CAS
- 124-38-9
- Name
- Ethanol
- InChI
- InChI=1S/C2H6O/c1-2-3/h3H,2H2,1H3
- InChI Key
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N
- Formula
- C2H6O
- SMILES
- CCO
- Mol. Weight (g/mol)
- 46.07
- CAS
- 64-17-5
- Name
- Water
- InChI
- InChI=1S/H2O/h1H2
- InChI Key
- XLYOFNOQVPJJNP-UHFFFAOYSA-N
- Formula
- H2O
- SMILES
- O
- Mol. Weight (g/mol)
- 18.02
- CAS
- 7732-18-5
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Datasets
Mole fraction of Carbon dioxide (1) [ref]
| Fixed | Measured | ||
|---|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Solvent: Mole fraction of Ethanol (2) - Liquid | Mole fraction of Carbon dioxide (1) - Liquid |
| 308.00 | 86.63 | 0.2500 | 0.0007 |
| 298.00 | 96.16 | 0.7500 | 0.0030 |
| 323.00 | 98.39 | 0.2500 | 0.0007 |
| 288.00 | 101.83 | 0.2500 | 0.0011 |
| 308.00 | 102.95 | 0.9000 | 0.0041 |
| 288.00 | 107.41 | 0.9000 | 0.0059 |
| 288.00 | 109.13 | 0.7500 | 0.0041 |
| 298.00 | 110.04 | 0.5000 | 0.0023 |
| 288.00 | 110.34 | 0.5000 | 0.0027 |
| 288.00 | 117.13 | 0.9000 | 0.0065 |
| 298.00 | 118.75 | 0.9000 | 0.0054 |
| 298.00 | 121.89 | 0.2500 | 0.0011 |
| 308.00 | 123.82 | 0.1000 | 0.0006 |
| 323.00 | 124.43 | 0.9000 | 0.0043 |
| 323.00 | 126.86 | 0.5000 | 0.0020 |
| 298.00 | 127.47 | 0.1000 | 0.0008 |
| 323.00 | 128.58 | 0.7500 | 0.0033 |
| 308.00 | 134.76 | 0.7500 | 0.0040 |
| 308.00 | 135.67 | 0.5000 | 0.0024 |
| 288.00 | 136.38 | 0.1000 | 0.0010 |
| 298.00 | 138.51 | 0.1000 | 0.0009 |
| 323.00 | 140.44 | 0.1000 | 0.0006 |
| 288.00 | 141.55 | 0.1000 | 0.0010 |
| 288.00 | 158.27 | 0.2500 | 0.0017 |
| 308.00 | 166.17 | 0.2500 | 0.0014 |
| 323.00 | 174.68 | 0.2500 | 0.0013 |
| 298.00 | 175.90 | 0.7500 | 0.0060 |
| 323.00 | 181.37 | 0.7500 | 0.0048 |
| 288.00 | 185.02 | 0.7500 | 0.0073 |
| 288.00 | 185.73 | 0.2500 | 0.0021 |
| 298.00 | 188.46 | 0.9000 | 0.0091 |
| 323.00 | 190.19 | 0.9000 | 0.0063 |
| 298.00 | 190.79 | 0.5000 | 0.0041 |
| 288.00 | 191.50 | 0.9000 | 0.0105 |
| 308.00 | 192.72 | 0.9000 | 0.0079 |
| 288.00 | 197.69 | 0.9000 | 0.0106 |
| 298.00 | 200.22 | 0.2500 | 0.0019 |
| 308.00 | 200.62 | 0.1000 | 0.0011 |
| 323.00 | 201.33 | 0.5000 | 0.0032 |
| 288.00 | 209.34 | 0.5000 | 0.0049 |
| 298.00 | 210.45 | 0.2500 | 0.0020 |
| 288.00 | 215.92 | 0.1000 | 0.0016 |
| 298.00 | 217.04 | 0.1000 | 0.0013 |
| 308.00 | 219.47 | 0.5000 | 0.0039 |
| 288.00 | 220.18 | 0.1000 | 0.0017 |
| 308.00 | 221.70 | 0.7500 | 0.0070 |
| 298.00 | 222.00 | 0.1000 | 0.0014 |
| 323.00 | 228.08 | 0.1000 | 0.0010 |
| 308.00 | 247.74 | 0.9000 | 0.0102 |
| 298.00 | 249.77 | 0.7500 | 0.0089 |
| 323.00 | 251.69 | 0.9000 | 0.0085 |
| 308.00 | 251.89 | 0.2500 | 0.0022 |
| 298.00 | 253.41 | 0.9000 | 0.0121 |
| 298.00 | 253.72 | 0.2500 | 0.0025 |
| 288.00 | 256.05 | 0.9000 | 0.0149 |
| 288.00 | 258.48 | 0.7500 | 0.0107 |
| 323.00 | 258.48 | 0.2500 | 0.0020 |
| 288.00 | 264.15 | 0.2500 | 0.0030 |
| 298.00 | 266.49 | 0.5000 | 0.0058 |
| 308.00 | 266.69 | 0.1000 | 0.0014 |
| 288.00 | 267.09 | 0.5000 | 0.0064 |
| 323.00 | 269.63 | 0.7500 | 0.0073 |
| 288.00 | 271.75 | 0.2500 | 0.0031 |
| 298.00 | 272.56 | 0.1000 | 0.0017 |
| 288.00 | 273.07 | 0.1000 | 0.0021 |
| 323.00 | 274.08 | 0.5000 | 0.0044 |
| 323.00 | 277.73 | 0.1000 | 0.0012 |
| 298.00 | 282.09 | 0.1000 | 0.0018 |
| 288.00 | 282.70 | 0.1000 | 0.0022 |
| 298.00 | 292.02 | 0.2500 | 0.0029 |
| 308.00 | 295.26 | 0.7500 | 0.0095 |
| 323.00 | 311.57 | 0.9000 | 0.0108 |
| 323.00 | 314.11 | 0.2500 | 0.0024 |
| 298.00 | 318.77 | 0.7500 | 0.0118 |
| 288.00 | 319.48 | 0.9000 | 0.0182 |
| 298.00 | 320.80 | 0.9000 | 0.0157 |
| 288.00 | 322.52 | 0.9000 | 0.0190 |
| 308.00 | 325.66 | 0.9000 | 0.0137 |
| 308.00 | 328.29 | 0.5000 | 0.0062 |
| 308.00 | 329.51 | 0.1000 | 0.0018 |
| 288.00 | 329.91 | 0.7500 | 0.0140 |
| 308.00 | 334.37 | 0.2500 | 0.0030 |
| 323.00 | 336.70 | 0.5000 | 0.0054 |
| 298.00 | 342.48 | 0.1000 | 0.0022 |
| 298.00 | 342.68 | 0.1000 | 0.0022 |
| 288.00 | 343.59 | 0.1000 | 0.0027 |
| 288.00 | 346.23 | 0.2500 | 0.0040 |
| 323.00 | 347.55 | 0.7500 | 0.0098 |
| 323.00 | 348.86 | 0.1000 | 0.0015 |
| 298.00 | 349.17 | 0.2500 | 0.0035 |
| 298.00 | 353.52 | 0.5000 | 0.0079 |
| 288.00 | 353.62 | 0.1000 | 0.0028 |
| 288.00 | 354.44 | 0.5000 | 0.0087 |
| 323.00 | 377.13 | 0.2500 | 0.0029 |
| 308.00 | 378.65 | 0.7500 | 0.0120 |
| 298.00 | 382.70 | 0.9000 | 0.0190 |
| 308.00 | 385.95 | 0.2500 | 0.0034 |
| 288.00 | 386.86 | 0.9000 | 0.0222 |
| 323.00 | 387.87 | 0.9000 | 0.0140 |
| 298.00 | 389.49 | 0.2500 | 0.0040 |
| 308.00 | 390.30 | 0.9000 | 0.0168 |
| 288.00 | 396.79 | 0.2500 | 0.0046 |
| 288.00 | 398.71 | 0.7500 | 0.0173 |
| 308.00 | 400.94 | 0.5000 | 0.0077 |
| 298.00 | 403.38 | 0.7500 | 0.0152 |
| 288.00 | 406.21 | 0.1000 | 0.0032 |
| 308.00 | 407.93 | 0.1000 | 0.0022 |
| 288.00 | 408.64 | 0.9000 | 0.0245 |
| 288.00 | 412.29 | 0.1000 | 0.0033 |
| 298.00 | 412.39 | 0.1000 | 0.0027 |
| 298.00 | 416.04 | 0.1000 | 0.0027 |
| 323.00 | 418.88 | 0.7500 | 0.0120 |
| 298.00 | 422.52 | 0.5000 | 0.0095 |
| 298.00 | 424.25 | 0.2500 | 0.0043 |
| 288.00 | 427.79 | 0.2500 | 0.0050 |
| 323.00 | 430.73 | 0.5000 | 0.0072 |
| 323.00 | 431.04 | 0.1000 | 0.0018 |
| 323.00 | 444.21 | 0.2500 | 0.0035 |
| 308.00 | 454.14 | 0.7500 | 0.0153 |
| 288.00 | 461.23 | 0.5000 | 0.0119 |
| 298.00 | 471.57 | 0.2500 | 0.0051 |
| 308.00 | 484.13 | 0.5000 | 0.0092 |
| 288.00 | 491.63 | 0.2500 | 0.0057 |
| 288.00 | 604.81 | 0.2500 | 0.0070 |
Pressure, kPa x Mole fraction [ref]
Operational condition: Temperature, K = 313 (Liquid)
| Fixed | Measured | |||
|---|---|---|---|---|
| Pressure, kPa - Liquid | Mole fraction of Water (3) - Liquid | Mole fraction of Ethanol (2) - Liquid | Mole fraction of Water (3) - Gas | Mole fraction of Ethanol (2) - Gas |
| 10000.00 | 0.1083 | 0.3282 | 0.0641 | 0.2534 |
| 10000.00 | 0.1835 | 0.3890 | 0.0212 | 0.1347 |
| 10000.00 | 0.2985 | 0.3815 | 0.0151 | 0.0911 |
| 10000.00 | 0.4138 | 0.3632 | 0.0151 | 0.0626 |
| 10000.00 | 0.4880 | 0.3364 | 0.0147 | 0.0607 |
| 10000.00 | 0.5479 | 0.3114 | 0.0095 | 0.0527 |
| 10000.00 | 0.6320 | 0.2728 | 0.0097 | 0.0450 |
| 10000.00 | 0.7037 | 0.2312 | 0.0104 | 0.0481 |
| 10000.00 | 0.7514 | 0.1909 | 0.0081 | 0.0310 |
| 10000.00 | 0.7937 | 0.1558 | 0.0069 | 0.0243 |
| 10000.00 | 0.8712 | 0.0945 | 0.0055 | 0.0153 |
| 10000.00 | 0.8888 | 0.0777 | 0.0042 | 0.0138 |
| 20000.00 | 0.1202 | 0.3161 | 0.0747 | 0.2363 |
| 20000.00 | 0.2085 | 0.3726 | 0.0571 | 0.2014 |
| 20000.00 | 0.2765 | 0.3778 | 0.0454 | 0.1663 |
| 20000.00 | 0.3041 | 0.3799 | 0.0347 | 0.1225 |
| 20000.00 | 0.3569 | 0.3655 | 0.0298 | 0.1177 |
| 20000.00 | 0.4636 | 0.3254 | 0.0367 | 0.0962 |
| 20000.00 | 0.5034 | 0.3055 | 0.0243 | 0.0795 |
| 20000.00 | 0.5330 | 0.2918 | 0.0173 | 0.0689 |
| 20000.00 | 0.5636 | 0.2740 | 0.0151 | 0.0600 |
| 20000.00 | 0.6507 | 0.2285 | 0.0188 | 0.0530 |
| 20000.00 | 0.7408 | 0.1668 | 0.0084 | 0.0374 |
| 20000.00 | 0.7666 | 0.1463 | 0.0054 | 0.0277 |
| 20000.00 | 0.7863 | 0.1310 | 0.0088 | 0.0239 |
| 20000.00 | 0.8699 | 0.0800 | 0.0080 | 0.0200 |
| 30000.00 | 0.1584 | 0.3200 | 0.1146 | 0.2607 |
| 30000.00 | 0.2233 | 0.3517 | 0.0964 | 0.2244 |
| 30000.00 | 0.3163 | 0.3487 | 0.0957 | 0.2094 |
| 30000.00 | 0.3821 | 0.3378 | 0.0892 | 0.2056 |
| 30000.00 | 0.4194 | 0.3228 | 0.0483 | 0.1239 |
| 30000.00 | 0.4923 | 0.2988 | 0.0406 | 0.1110 |
| 30000.00 | 0.5864 | 0.2546 | 0.0302 | 0.0868 |
| 30000.00 | 0.6100 | 0.2441 | 0.0274 | 0.0849 |
| 30000.00 | 0.6465 | 0.2217 | 0.0337 | 0.0786 |
| 30000.00 | 0.6836 | 0.1980 | 0.0292 | 0.0706 |
| 30000.00 | 0.7941 | 0.1218 | 0.0153 | 0.0222 |
| 30000.00 | 0.8584 | 0.0725 | 0.0115 | 0.0138 |
Mole fraction [ref]
Operational conditions:
- Temperature, K = 353 (Liquid)
- Pressure, kPa = 12000 (Liquid)
| Fixed | Measured | ||
|---|---|---|---|
| Mole fraction of Carbon dioxide (1) - Liquid | Mole fraction of Water (3) - Liquid | Mole fraction of Water (3) - Gas | Mole fraction of Carbon dioxide (1) - Gas |
| 0.4230 | 0.1050 | 0.0095 | 0.9400 |
| 0.3400 | 0.2200 | 0.0107 | 0.9460 |
| 0.2570 | 0.3280 | 0.0126 | 0.9500 |
| 0.1800 | 0.4630 | 0.0119 | 0.9550 |
Mole fraction of Carbon dioxide (1) [ref]
Operational condition: Solvent: Mole fraction = 0.9 (Liquid)
| Temperature, K - Liquid | Mole fraction of Carbon dioxide (1) - Liquid |
|---|---|
| 318.20 | 0.9230 |
| 328.20 | 0.8260 |
| 338.20 | 0.8250 |
| 348.20 | 0.8200 |
Temperature, K x Pressure, kPa x Mole fraction [ref]
| Fixed | Measured | ||||
|---|---|---|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mole fraction of Carbon dioxide (1) - Liquid | Mole fraction of Ethanol (2) - Liquid | Mole fraction of Ethanol (2) - Gas | Mole fraction of Carbon dioxide (1) - Gas |
| 313.20 | 10000.00 | 0.4120 | 0.3700 | 0.1100 | 0.8580 |
| 313.20 | 15000.00 | 0.0540 | 0.1990 | 0.0500 | 0.9320 |
| 313.20 | 20000.00 | 0.2430 | 0.3460 | 0.1150 | 0.8400 |
| 313.20 | 20000.00 | 0.1500 | 0.3120 | 0.0870 | 0.8820 |
| 313.20 | 20000.00 | 0.0920 | 0.2710 | 0.0740 | 0.9050 |
| 313.20 | 20000.00 | 0.0470 | 0.1780 | 0.0530 | 0.9280 |
| 333.20 | 10000.00 | 0.3250 | 0.4550 | 0.0240 | 0.9700 |
| 333.20 | 10000.00 | 0.2670 | 0.4300 | 0.0220 | 0.9720 |
| 333.20 | 10000.00 | 0.1990 | 0.3900 | 0.0210 | 0.9710 |
| 333.20 | 10000.00 | 0.1270 | 0.3330 | 0.0190 | 0.9740 |
| 333.20 | 10000.00 | 0.0770 | 0.2620 | 0.0170 | 0.9750 |
| 313.20 | 10000.00 | 0.2690 | 0.3800 | 0.0760 | 0.9010 |
| 333.20 | 15000.00 | 0.3930 | 0.3470 | 0.1360 | 0.8130 |
| 333.20 | 15000.00 | 0.2420 | 0.3500 | 0.0940 | 0.8710 |
| 333.20 | 15000.00 | 0.1650 | 0.3210 | 0.0720 | 0.9030 |
| 333.20 | 15000.00 | 0.1020 | 0.2640 | 0.0620 | 0.9150 |
| 333.20 | 15000.00 | 0.0600 | 0.1990 | 0.0490 | 0.9320 |
| 333.20 | 20000.00 | 0.2420 | 0.3140 | 0.1180 | 0.8310 |
| 333.20 | 20000.00 | 0.1300 | 0.2850 | 0.0970 | 0.8640 |
| 333.20 | 20000.00 | 0.0750 | 0.2180 | 0.0750 | 0.8950 |
| 333.20 | 20000.00 | 0.0510 | 0.1740 | 0.0610 | 0.9140 |
| 353.20 | 10000.00 | 0.2510 | 0.5120 | 0.0310 | 0.9620 |
| 313.20 | 10000.00 | 0.1660 | 0.3480 | 0.0580 | 0.9240 |
| 353.20 | 10000.00 | 0.2030 | 0.4660 | 0.0250 | 0.9680 |
| 353.20 | 10000.00 | 0.1560 | 0.4000 | 0.0240 | 0.9670 |
| 353.20 | 10000.00 | 0.1090 | 0.3380 | 0.0220 | 0.9690 |
| 353.20 | 10000.00 | 0.0710 | 0.2630 | 0.0210 | 0.9700 |
| 353.20 | 15000.00 | 0.4190 | 0.3680 | 0.0910 | 0.8820 |
| 353.20 | 15000.00 | 0.2970 | 0.3720 | 0.0710 | 0.9070 |
| 353.20 | 15000.00 | 0.1970 | 0.3350 | 0.0590 | 0.9200 |
| 353.20 | 15000.00 | 0.1290 | 0.2830 | 0.0500 | 0.9310 |
| 353.20 | 15000.00 | 0.0780 | 0.2190 | 0.0450 | 0.9380 |
| 353.20 | 20000.00 | 0.2500 | 0.3140 | 0.1210 | 0.8240 |
| 313.20 | 10000.00 | 0.1010 | 0.2690 | 0.0480 | 0.9390 |
| 353.20 | 20000.00 | 0.1550 | 0.2810 | 0.1000 | 0.8560 |
| 353.20 | 20000.00 | 0.0940 | 0.2330 | 0.0780 | 0.8890 |
| 353.20 | 20000.00 | 0.0600 | 0.1750 | 0.0620 | 0.9120 |
| 313.20 | 10000.00 | 0.0560 | 0.2140 | 0.0400 | 0.9480 |
| 313.20 | 15000.00 | 0.4550 | 0.3260 | 0.1650 | 0.7690 |
| 313.20 | 15000.00 | 0.2470 | 0.3630 | 0.1030 | 0.8620 |
| 313.20 | 15000.00 | 0.1550 | 0.3250 | 0.0800 | 0.8930 |
| 313.20 | 15000.00 | 0.0730 | 0.2760 | 0.0660 | 0.9130 |
Pressure, kPa x Mass fraction [ref]
Operational condition: Temperature, K = 333 (Liquid)
| Fixed | Measured | |||
|---|---|---|---|---|
| Pressure, kPa - Liquid | Mass fraction of Carbon dioxide (1) - Liquid | Mass fraction of Ethanol (2) - Liquid | Mass fraction of Ethanol (2) - Gas | Mass fraction of Carbon dioxide (1) - Gas |
| 10110.00 | 0.0345 | 0.0559 | 0.0090 | 0.9821 |
| 10050.00 | 0.0374 | 0.1457 | 0.0084 | 0.9906 |
| 10220.00 | 0.0399 | 0.1466 | 0.0113 | 0.9859 |
| 10060.00 | 0.0635 | 0.3011 | 0.0136 | 0.9844 |
| 9960.00 | 0.1529 | 0.4859 | 0.0165 | 0.9821 |
| 10200.00 | 0.1628 | 0.4672 | 0.0205 | 0.9789 |
| 10030.00 | 0.3364 | 0.4831 | 0.0218 | 0.9764 |
Mole fraction of Carbon dioxide (1) [ref]
| Fixed | Measured | ||
|---|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Solvent: Mole fraction of Ethanol (2) - Liquid | Mole fraction of Carbon dioxide (1) - Liquid |
| 308.00 | 86.63 | 0.2500 | 0.0007 |
| 298.00 | 96.16 | 0.7500 | 0.0030 |
| 323.00 | 98.39 | 0.2500 | 0.0007 |
| 288.00 | 101.83 | 0.2500 | 0.0011 |
| 308.00 | 102.95 | 0.9000 | 0.0041 |
| 288.00 | 107.41 | 0.9000 | 0.0059 |
| 288.00 | 109.13 | 0.7500 | 0.0041 |
| 298.00 | 110.04 | 0.5000 | 0.0023 |
| 288.00 | 110.34 | 0.5000 | 0.0027 |
| 288.00 | 117.13 | 0.9000 | 0.0065 |
| 298.00 | 118.75 | 0.9000 | 0.0054 |
| 298.00 | 121.89 | 0.2500 | 0.0011 |
| 308.00 | 123.82 | 0.1000 | 0.0006 |
| 323.00 | 124.43 | 0.9000 | 0.0043 |
| 323.00 | 126.86 | 0.5000 | 0.0020 |
| 298.00 | 127.47 | 0.1000 | 0.0008 |
| 323.00 | 128.58 | 0.7500 | 0.0033 |
| 308.00 | 134.76 | 0.7500 | 0.0040 |
| 308.00 | 135.67 | 0.5000 | 0.0024 |
| 288.00 | 136.38 | 0.1000 | 0.0010 |
| 298.00 | 138.51 | 0.1000 | 0.0009 |
| 323.00 | 140.44 | 0.1000 | 0.0006 |
| 288.00 | 141.55 | 0.1000 | 0.0010 |
| 288.00 | 158.27 | 0.2500 | 0.0017 |
| 308.00 | 166.17 | 0.2500 | 0.0014 |
| 323.00 | 174.68 | 0.2500 | 0.0013 |
| 298.00 | 175.90 | 0.7500 | 0.0060 |
| 323.00 | 181.37 | 0.7500 | 0.0048 |
| 288.00 | 185.02 | 0.7500 | 0.0073 |
| 288.00 | 185.73 | 0.2500 | 0.0021 |
| 298.00 | 188.46 | 0.9000 | 0.0091 |
| 323.00 | 190.19 | 0.9000 | 0.0063 |
| 298.00 | 190.79 | 0.5000 | 0.0041 |
| 288.00 | 191.50 | 0.9000 | 0.0105 |
| 308.00 | 192.72 | 0.9000 | 0.0079 |
| 288.00 | 197.69 | 0.9000 | 0.0106 |
| 298.00 | 200.22 | 0.2500 | 0.0019 |
| 308.00 | 200.62 | 0.1000 | 0.0011 |
| 323.00 | 201.33 | 0.5000 | 0.0032 |
| 288.00 | 209.34 | 0.5000 | 0.0049 |
| 298.00 | 210.45 | 0.2500 | 0.0020 |
| 288.00 | 215.92 | 0.1000 | 0.0016 |
| 298.00 | 217.04 | 0.1000 | 0.0013 |
| 308.00 | 219.47 | 0.5000 | 0.0039 |
| 288.00 | 220.18 | 0.1000 | 0.0017 |
| 308.00 | 221.70 | 0.7500 | 0.0070 |
| 298.00 | 222.00 | 0.1000 | 0.0014 |
| 323.00 | 228.08 | 0.1000 | 0.0010 |
| 308.00 | 247.74 | 0.9000 | 0.0102 |
| 298.00 | 249.77 | 0.7500 | 0.0089 |
| 323.00 | 251.69 | 0.9000 | 0.0085 |
| 308.00 | 251.89 | 0.2500 | 0.0022 |
| 298.00 | 253.41 | 0.9000 | 0.0121 |
| 298.00 | 253.72 | 0.2500 | 0.0025 |
| 288.00 | 256.05 | 0.9000 | 0.0149 |
| 288.00 | 258.48 | 0.7500 | 0.0107 |
| 323.00 | 258.48 | 0.2500 | 0.0020 |
| 288.00 | 264.15 | 0.2500 | 0.0030 |
| 298.00 | 266.49 | 0.5000 | 0.0058 |
| 308.00 | 266.69 | 0.1000 | 0.0014 |
| 288.00 | 267.09 | 0.5000 | 0.0064 |
| 323.00 | 269.63 | 0.7500 | 0.0073 |
| 288.00 | 271.75 | 0.2500 | 0.0031 |
| 298.00 | 272.56 | 0.1000 | 0.0017 |
| 288.00 | 273.07 | 0.1000 | 0.0021 |
| 323.00 | 274.08 | 0.5000 | 0.0044 |
| 323.00 | 277.73 | 0.1000 | 0.0012 |
| 298.00 | 282.09 | 0.1000 | 0.0018 |
| 288.00 | 282.70 | 0.1000 | 0.0022 |
| 298.00 | 292.02 | 0.2500 | 0.0029 |
| 308.00 | 295.26 | 0.7500 | 0.0095 |
| 323.00 | 311.57 | 0.9000 | 0.0108 |
| 323.00 | 314.11 | 0.2500 | 0.0024 |
| 298.00 | 318.77 | 0.7500 | 0.0118 |
| 288.00 | 319.48 | 0.9000 | 0.0182 |
| 298.00 | 320.80 | 0.9000 | 0.0157 |
| 288.00 | 322.52 | 0.9000 | 0.0190 |
| 308.00 | 325.66 | 0.9000 | 0.0137 |
| 308.00 | 328.29 | 0.5000 | 0.0062 |
| 308.00 | 329.51 | 0.1000 | 0.0018 |
| 288.00 | 329.91 | 0.7500 | 0.0140 |
| 308.00 | 334.37 | 0.2500 | 0.0030 |
| 323.00 | 336.70 | 0.5000 | 0.0054 |
| 298.00 | 342.48 | 0.1000 | 0.0022 |
| 298.00 | 342.68 | 0.1000 | 0.0022 |
| 288.00 | 343.59 | 0.1000 | 0.0027 |
| 288.00 | 346.23 | 0.2500 | 0.0040 |
| 323.00 | 347.55 | 0.7500 | 0.0098 |
| 323.00 | 348.86 | 0.1000 | 0.0015 |
| 298.00 | 349.17 | 0.2500 | 0.0035 |
| 298.00 | 353.52 | 0.5000 | 0.0079 |
| 288.00 | 353.62 | 0.1000 | 0.0028 |
| 288.00 | 354.44 | 0.5000 | 0.0087 |
| 323.00 | 377.13 | 0.2500 | 0.0029 |
| 308.00 | 378.65 | 0.7500 | 0.0120 |
| 298.00 | 382.70 | 0.9000 | 0.0190 |
| 308.00 | 385.95 | 0.2500 | 0.0034 |
| 288.00 | 386.86 | 0.9000 | 0.0222 |
| 323.00 | 387.87 | 0.9000 | 0.0140 |
| 298.00 | 389.49 | 0.2500 | 0.0040 |
| 308.00 | 390.30 | 0.9000 | 0.0168 |
| 288.00 | 396.79 | 0.2500 | 0.0046 |
| 288.00 | 398.71 | 0.7500 | 0.0173 |
| 308.00 | 400.94 | 0.5000 | 0.0077 |
| 298.00 | 403.38 | 0.7500 | 0.0152 |
| 288.00 | 406.21 | 0.1000 | 0.0032 |
| 308.00 | 407.93 | 0.1000 | 0.0022 |
| 288.00 | 408.64 | 0.9000 | 0.0245 |
| 288.00 | 412.29 | 0.1000 | 0.0033 |
| 298.00 | 412.39 | 0.1000 | 0.0027 |
| 298.00 | 416.04 | 0.1000 | 0.0027 |
| 323.00 | 418.88 | 0.7500 | 0.0120 |
| 298.00 | 422.52 | 0.5000 | 0.0095 |
| 298.00 | 424.25 | 0.2500 | 0.0043 |
| 288.00 | 427.79 | 0.2500 | 0.0050 |
| 323.00 | 430.73 | 0.5000 | 0.0072 |
| 323.00 | 431.04 | 0.1000 | 0.0018 |
| 323.00 | 444.21 | 0.2500 | 0.0035 |
| 308.00 | 454.14 | 0.7500 | 0.0153 |
| 288.00 | 461.23 | 0.5000 | 0.0119 |
| 298.00 | 471.57 | 0.2500 | 0.0051 |
| 308.00 | 484.13 | 0.5000 | 0.0092 |
| 288.00 | 491.63 | 0.2500 | 0.0057 |
| 288.00 | 604.81 | 0.2500 | 0.0070 |
Pressure, kPa x Mole fraction [ref]
Operational condition: Temperature, K = 313 (Liquid)
| Fixed | Measured | |||
|---|---|---|---|---|
| Pressure, kPa - Liquid | Mole fraction of Water (3) - Liquid | Mole fraction of Ethanol (2) - Liquid | Mole fraction of Water (3) - Gas | Mole fraction of Ethanol (2) - Gas |
| 10000.00 | 0.1083 | 0.3282 | 0.0641 | 0.2534 |
| 10000.00 | 0.1835 | 0.3890 | 0.0212 | 0.1347 |
| 10000.00 | 0.2985 | 0.3815 | 0.0151 | 0.0911 |
| 10000.00 | 0.4138 | 0.3632 | 0.0151 | 0.0626 |
| 10000.00 | 0.4880 | 0.3364 | 0.0147 | 0.0607 |
| 10000.00 | 0.5479 | 0.3114 | 0.0095 | 0.0527 |
| 10000.00 | 0.6320 | 0.2728 | 0.0097 | 0.0450 |
| 10000.00 | 0.7037 | 0.2312 | 0.0104 | 0.0481 |
| 10000.00 | 0.7514 | 0.1909 | 0.0081 | 0.0310 |
| 10000.00 | 0.7937 | 0.1558 | 0.0069 | 0.0243 |
| 10000.00 | 0.8712 | 0.0945 | 0.0055 | 0.0153 |
| 10000.00 | 0.8888 | 0.0777 | 0.0042 | 0.0138 |
| 20000.00 | 0.1202 | 0.3161 | 0.0747 | 0.2363 |
| 20000.00 | 0.2085 | 0.3726 | 0.0571 | 0.2014 |
| 20000.00 | 0.2765 | 0.3778 | 0.0454 | 0.1663 |
| 20000.00 | 0.3041 | 0.3799 | 0.0347 | 0.1225 |
| 20000.00 | 0.3569 | 0.3655 | 0.0298 | 0.1177 |
| 20000.00 | 0.4636 | 0.3254 | 0.0367 | 0.0962 |
| 20000.00 | 0.5034 | 0.3055 | 0.0243 | 0.0795 |
| 20000.00 | 0.5330 | 0.2918 | 0.0173 | 0.0689 |
| 20000.00 | 0.5636 | 0.2740 | 0.0151 | 0.0600 |
| 20000.00 | 0.6507 | 0.2285 | 0.0188 | 0.0530 |
| 20000.00 | 0.7408 | 0.1668 | 0.0084 | 0.0374 |
| 20000.00 | 0.7666 | 0.1463 | 0.0054 | 0.0277 |
| 20000.00 | 0.7863 | 0.1310 | 0.0088 | 0.0239 |
| 20000.00 | 0.8699 | 0.0800 | 0.0080 | 0.0200 |
| 30000.00 | 0.1584 | 0.3200 | 0.1146 | 0.2607 |
| 30000.00 | 0.2233 | 0.3517 | 0.0964 | 0.2244 |
| 30000.00 | 0.3163 | 0.3487 | 0.0957 | 0.2094 |
| 30000.00 | 0.3821 | 0.3378 | 0.0892 | 0.2056 |
| 30000.00 | 0.4194 | 0.3228 | 0.0483 | 0.1239 |
| 30000.00 | 0.4923 | 0.2988 | 0.0406 | 0.1110 |
| 30000.00 | 0.5864 | 0.2546 | 0.0302 | 0.0868 |
| 30000.00 | 0.6100 | 0.2441 | 0.0274 | 0.0849 |
| 30000.00 | 0.6465 | 0.2217 | 0.0337 | 0.0786 |
| 30000.00 | 0.6836 | 0.1980 | 0.0292 | 0.0706 |
| 30000.00 | 0.7941 | 0.1218 | 0.0153 | 0.0222 |
| 30000.00 | 0.8584 | 0.0725 | 0.0115 | 0.0138 |
Mole fraction [ref]
Operational conditions:
- Temperature, K = 353 (Liquid)
- Pressure, kPa = 12000 (Liquid)
| Fixed | Measured | ||
|---|---|---|---|
| Mole fraction of Carbon dioxide (1) - Liquid | Mole fraction of Water (3) - Liquid | Mole fraction of Water (3) - Gas | Mole fraction of Carbon dioxide (1) - Gas |
| 0.4230 | 0.1050 | 0.0095 | 0.9400 |
| 0.3400 | 0.2200 | 0.0107 | 0.9460 |
| 0.2570 | 0.3280 | 0.0126 | 0.9500 |
| 0.1800 | 0.4630 | 0.0119 | 0.9550 |
Mole fraction of Carbon dioxide (1) [ref]
Operational condition: Solvent: Mole fraction = 0.9 (Liquid)
| Temperature, K - Liquid | Mole fraction of Carbon dioxide (1) - Liquid |
|---|---|
| 318.20 | 0.9230 |
| 328.20 | 0.8260 |
| 338.20 | 0.8250 |
| 348.20 | 0.8200 |
Temperature, K x Pressure, kPa x Mole fraction [ref]
| Fixed | Measured | ||||
|---|---|---|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mole fraction of Carbon dioxide (1) - Liquid | Mole fraction of Ethanol (2) - Liquid | Mole fraction of Ethanol (2) - Gas | Mole fraction of Carbon dioxide (1) - Gas |
| 313.20 | 10000.00 | 0.4120 | 0.3700 | 0.1100 | 0.8580 |
| 313.20 | 15000.00 | 0.0540 | 0.1990 | 0.0500 | 0.9320 |
| 313.20 | 20000.00 | 0.2430 | 0.3460 | 0.1150 | 0.8400 |
| 313.20 | 20000.00 | 0.1500 | 0.3120 | 0.0870 | 0.8820 |
| 313.20 | 20000.00 | 0.0920 | 0.2710 | 0.0740 | 0.9050 |
| 313.20 | 20000.00 | 0.0470 | 0.1780 | 0.0530 | 0.9280 |
| 333.20 | 10000.00 | 0.3250 | 0.4550 | 0.0240 | 0.9700 |
| 333.20 | 10000.00 | 0.2670 | 0.4300 | 0.0220 | 0.9720 |
| 333.20 | 10000.00 | 0.1990 | 0.3900 | 0.0210 | 0.9710 |
| 333.20 | 10000.00 | 0.1270 | 0.3330 | 0.0190 | 0.9740 |
| 333.20 | 10000.00 | 0.0770 | 0.2620 | 0.0170 | 0.9750 |
| 313.20 | 10000.00 | 0.2690 | 0.3800 | 0.0760 | 0.9010 |
| 333.20 | 15000.00 | 0.3930 | 0.3470 | 0.1360 | 0.8130 |
| 333.20 | 15000.00 | 0.2420 | 0.3500 | 0.0940 | 0.8710 |
| 333.20 | 15000.00 | 0.1650 | 0.3210 | 0.0720 | 0.9030 |
| 333.20 | 15000.00 | 0.1020 | 0.2640 | 0.0620 | 0.9150 |
| 333.20 | 15000.00 | 0.0600 | 0.1990 | 0.0490 | 0.9320 |
| 333.20 | 20000.00 | 0.2420 | 0.3140 | 0.1180 | 0.8310 |
| 333.20 | 20000.00 | 0.1300 | 0.2850 | 0.0970 | 0.8640 |
| 333.20 | 20000.00 | 0.0750 | 0.2180 | 0.0750 | 0.8950 |
| 333.20 | 20000.00 | 0.0510 | 0.1740 | 0.0610 | 0.9140 |
| 353.20 | 10000.00 | 0.2510 | 0.5120 | 0.0310 | 0.9620 |
| 313.20 | 10000.00 | 0.1660 | 0.3480 | 0.0580 | 0.9240 |
| 353.20 | 10000.00 | 0.2030 | 0.4660 | 0.0250 | 0.9680 |
| 353.20 | 10000.00 | 0.1560 | 0.4000 | 0.0240 | 0.9670 |
| 353.20 | 10000.00 | 0.1090 | 0.3380 | 0.0220 | 0.9690 |
| 353.20 | 10000.00 | 0.0710 | 0.2630 | 0.0210 | 0.9700 |
| 353.20 | 15000.00 | 0.4190 | 0.3680 | 0.0910 | 0.8820 |
| 353.20 | 15000.00 | 0.2970 | 0.3720 | 0.0710 | 0.9070 |
| 353.20 | 15000.00 | 0.1970 | 0.3350 | 0.0590 | 0.9200 |
| 353.20 | 15000.00 | 0.1290 | 0.2830 | 0.0500 | 0.9310 |
| 353.20 | 15000.00 | 0.0780 | 0.2190 | 0.0450 | 0.9380 |
| 353.20 | 20000.00 | 0.2500 | 0.3140 | 0.1210 | 0.8240 |
| 313.20 | 10000.00 | 0.1010 | 0.2690 | 0.0480 | 0.9390 |
| 353.20 | 20000.00 | 0.1550 | 0.2810 | 0.1000 | 0.8560 |
| 353.20 | 20000.00 | 0.0940 | 0.2330 | 0.0780 | 0.8890 |
| 353.20 | 20000.00 | 0.0600 | 0.1750 | 0.0620 | 0.9120 |
| 313.20 | 10000.00 | 0.0560 | 0.2140 | 0.0400 | 0.9480 |
| 313.20 | 15000.00 | 0.4550 | 0.3260 | 0.1650 | 0.7690 |
| 313.20 | 15000.00 | 0.2470 | 0.3630 | 0.1030 | 0.8620 |
| 313.20 | 15000.00 | 0.1550 | 0.3250 | 0.0800 | 0.8930 |
| 313.20 | 15000.00 | 0.0730 | 0.2760 | 0.0660 | 0.9130 |
Pressure, kPa x Mass fraction [ref]
Operational condition: Temperature, K = 333 (Liquid)
| Fixed | Measured | |||
|---|---|---|---|---|
| Pressure, kPa - Liquid | Mass fraction of Carbon dioxide (1) - Liquid | Mass fraction of Ethanol (2) - Liquid | Mass fraction of Ethanol (2) - Gas | Mass fraction of Carbon dioxide (1) - Gas |
| 10110.00 | 0.0345 | 0.0559 | 0.0090 | 0.9821 |
| 10050.00 | 0.0374 | 0.1457 | 0.0084 | 0.9906 |
| 10220.00 | 0.0399 | 0.1466 | 0.0113 | 0.9859 |
| 10060.00 | 0.0635 | 0.3011 | 0.0136 | 0.9844 |
| 9960.00 | 0.1529 | 0.4859 | 0.0165 | 0.9821 |
| 10200.00 | 0.1628 | 0.4672 | 0.0205 | 0.9789 |
| 10030.00 | 0.3364 | 0.4831 | 0.0218 | 0.9764 |
Critical pressure, kPa [ref]
Operational condition: Solvent: Mole fraction = 0.9 (Liquid)
| Temperature, K - Liquid | Critical pressure, kPa - Liquid |
|---|---|
| 318.20 | 8850.00 |
| 328.20 | 10340.00 |
| 338.20 | 11910.00 |
| 348.20 | 13150.00 |
Critical pressure, kPa [ref]
Operational condition: Solvent: Mole fraction = 0.9 (Liquid)
| Temperature, K - Liquid | Critical pressure, kPa - Liquid |
|---|---|
| 318.20 | 8850.00 |
| 328.20 | 10340.00 |
| 338.20 | 11910.00 |
| 348.20 | 13150.00 |
Vapor or sublimation pressure, kPa [ref]
Operational condition: Solvent: Mole fraction = 0.9 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Carbon dioxide (1) - Liquid | Vapor or sublimation pressure, kPa - Gas |
| 298.20 | 0.2070 | 3120.00 |
| 298.20 | 0.3080 | 4270.00 |
| 298.20 | 0.4030 | 5040.00 |
| 298.20 | 0.5060 | 5500.00 |
| 298.20 | 0.6080 | 5650.00 |
| 298.20 | 0.7000 | 5800.00 |
| 298.20 | 0.7500 | 5840.00 |
| 298.20 | 0.7940 | 5910.00 |
| 298.20 | 0.8240 | 5920.00 |
| 298.20 | 0.8580 | 5960.00 |
| 298.20 | 0.8860 | 5990.00 |
| 298.20 | 0.9170 | 6000.00 |
| 298.20 | 0.9500 | 6130.00 |
| 298.20 | 0.9790 | 6240.00 |
| 308.20 | 0.2070 | 3650.00 |
| 308.20 | 0.3080 | 5050.00 |
| 308.20 | 0.4030 | 5980.00 |
| 308.20 | 0.5060 | 6560.00 |
| 308.20 | 0.6080 | 6790.00 |
| 308.20 | 0.7000 | 7020.00 |
| 308.20 | 0.7500 | 7090.00 |
| 308.20 | 0.7940 | 7200.00 |
| 308.20 | 0.8240 | 7210.00 |
| 308.20 | 0.8580 | 7220.00 |
| 308.20 | 0.8860 | 7270.00 |
| 308.20 | 0.9170 | 7330.00 |
| 308.20 | 0.9500 | 7470.00 |
| 308.20 | 0.9790 | 7580.00 |
| 318.20 | 0.2070 | 4130.00 |
| 318.20 | 0.3080 | 5810.00 |
| 318.20 | 0.4030 | 6930.00 |
| 318.20 | 0.5060 | 7630.00 |
| 318.20 | 0.6080 | 8210.00 |
| 318.20 | 0.7000 | 8450.00 |
| 318.20 | 0.7500 | 8560.00 |
| 318.20 | 0.7940 | 8630.00 |
| 318.20 | 0.8240 | 8680.00 |
| 318.20 | 0.8580 | 8720.00 |
| 318.20 | 0.8860 | 8780.00 |
| 318.20 | 0.9170 | 8850.00 |
| 328.20 | 0.2070 | 4680.00 |
| 328.20 | 0.3080 | 6590.00 |
| 328.20 | 0.4030 | 7890.00 |
| 328.20 | 0.5060 | 8840.00 |
| 328.20 | 0.6080 | 9610.00 |
| 328.20 | 0.7000 | 10010.00 |
| 328.20 | 0.7500 | 10160.00 |
| 328.20 | 0.7940 | 10290.00 |
| 328.20 | 0.8240 | 10340.00 |
| 338.20 | 0.2070 | 5260.00 |
| 338.20 | 0.3080 | 7250.00 |
| 338.20 | 0.4030 | 8830.00 |
| 338.20 | 0.5060 | 10030.00 |
| 338.20 | 0.6080 | 10830.00 |
| 338.20 | 0.7000 | 11420.00 |
| 338.20 | 0.7500 | 11620.00 |
| 338.20 | 0.7940 | 11780.00 |
| 338.20 | 0.8240 | 11910.00 |
| 348.20 | 0.2070 | 5780.00 |
| 348.20 | 0.3080 | 7930.00 |
| 348.20 | 0.4030 | 9720.00 |
| 348.20 | 0.5060 | 11120.00 |
| 348.20 | 0.6080 | 12040.00 |
| 348.20 | 0.7000 | 12760.00 |
| 348.20 | 0.7500 | 12960.00 |
| 348.20 | 0.7940 | 13090.00 |
Vapor or sublimation pressure, kPa [ref]
Operational condition: Solvent: Mole fraction = 0.9 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Carbon dioxide (1) - Gas | Vapor or sublimation pressure, kPa - Gas |
| 318.20 | 0.9500 | 8760.00 |
| 318.20 | 0.9790 | 7250.00 |
| 328.20 | 0.8580 | 10310.00 |
| 328.20 | 0.8860 | 10260.00 |
| 328.20 | 0.9170 | 10180.00 |
| 328.20 | 0.9500 | 9850.00 |
| 328.20 | 0.9790 | 7250.00 |
| 338.20 | 0.8580 | 11810.00 |
| 338.20 | 0.8860 | 11650.00 |
| 338.20 | 0.9170 | 11500.00 |
| 338.20 | 0.9500 | 10430.00 |
| 338.20 | 0.9790 | 7670.00 |
| 348.20 | 0.8240 | 13150.00 |
| 348.20 | 0.8580 | 12910.00 |
| 348.20 | 0.8860 | 12760.00 |
| 348.20 | 0.9170 | 12390.00 |
| 348.20 | 0.9500 | 11100.00 |
| 348.20 | 0.9790 | 7930.00 |
Vapor or sublimation pressure, kPa [ref]
Operational condition: Solvent: Mole fraction = 0.9 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Carbon dioxide (1) - Liquid | Vapor or sublimation pressure, kPa - Gas |
| 298.20 | 0.2070 | 3120.00 |
| 298.20 | 0.3080 | 4270.00 |
| 298.20 | 0.4030 | 5040.00 |
| 298.20 | 0.5060 | 5500.00 |
| 298.20 | 0.6080 | 5650.00 |
| 298.20 | 0.7000 | 5800.00 |
| 298.20 | 0.7500 | 5840.00 |
| 298.20 | 0.7940 | 5910.00 |
| 298.20 | 0.8240 | 5920.00 |
| 298.20 | 0.8580 | 5960.00 |
| 298.20 | 0.8860 | 5990.00 |
| 298.20 | 0.9170 | 6000.00 |
| 298.20 | 0.9500 | 6130.00 |
| 298.20 | 0.9790 | 6240.00 |
| 308.20 | 0.2070 | 3650.00 |
| 308.20 | 0.3080 | 5050.00 |
| 308.20 | 0.4030 | 5980.00 |
| 308.20 | 0.5060 | 6560.00 |
| 308.20 | 0.6080 | 6790.00 |
| 308.20 | 0.7000 | 7020.00 |
| 308.20 | 0.7500 | 7090.00 |
| 308.20 | 0.7940 | 7200.00 |
| 308.20 | 0.8240 | 7210.00 |
| 308.20 | 0.8580 | 7220.00 |
| 308.20 | 0.8860 | 7270.00 |
| 308.20 | 0.9170 | 7330.00 |
| 308.20 | 0.9500 | 7470.00 |
| 308.20 | 0.9790 | 7580.00 |
| 318.20 | 0.2070 | 4130.00 |
| 318.20 | 0.3080 | 5810.00 |
| 318.20 | 0.4030 | 6930.00 |
| 318.20 | 0.5060 | 7630.00 |
| 318.20 | 0.6080 | 8210.00 |
| 318.20 | 0.7000 | 8450.00 |
| 318.20 | 0.7500 | 8560.00 |
| 318.20 | 0.7940 | 8630.00 |
| 318.20 | 0.8240 | 8680.00 |
| 318.20 | 0.8580 | 8720.00 |
| 318.20 | 0.8860 | 8780.00 |
| 318.20 | 0.9170 | 8850.00 |
| 328.20 | 0.2070 | 4680.00 |
| 328.20 | 0.3080 | 6590.00 |
| 328.20 | 0.4030 | 7890.00 |
| 328.20 | 0.5060 | 8840.00 |
| 328.20 | 0.6080 | 9610.00 |
| 328.20 | 0.7000 | 10010.00 |
| 328.20 | 0.7500 | 10160.00 |
| 328.20 | 0.7940 | 10290.00 |
| 328.20 | 0.8240 | 10340.00 |
| 338.20 | 0.2070 | 5260.00 |
| 338.20 | 0.3080 | 7250.00 |
| 338.20 | 0.4030 | 8830.00 |
| 338.20 | 0.5060 | 10030.00 |
| 338.20 | 0.6080 | 10830.00 |
| 338.20 | 0.7000 | 11420.00 |
| 338.20 | 0.7500 | 11620.00 |
| 338.20 | 0.7940 | 11780.00 |
| 338.20 | 0.8240 | 11910.00 |
| 348.20 | 0.2070 | 5780.00 |
| 348.20 | 0.3080 | 7930.00 |
| 348.20 | 0.4030 | 9720.00 |
| 348.20 | 0.5060 | 11120.00 |
| 348.20 | 0.6080 | 12040.00 |
| 348.20 | 0.7000 | 12760.00 |
| 348.20 | 0.7500 | 12960.00 |
| 348.20 | 0.7940 | 13090.00 |
Vapor or sublimation pressure, kPa [ref]
Operational condition: Solvent: Mole fraction = 0.9 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Carbon dioxide (1) - Gas | Vapor or sublimation pressure, kPa - Gas |
| 318.20 | 0.9500 | 8760.00 |
| 318.20 | 0.9790 | 7250.00 |
| 328.20 | 0.8580 | 10310.00 |
| 328.20 | 0.8860 | 10260.00 |
| 328.20 | 0.9170 | 10180.00 |
| 328.20 | 0.9500 | 9850.00 |
| 328.20 | 0.9790 | 7250.00 |
| 338.20 | 0.8580 | 11810.00 |
| 338.20 | 0.8860 | 11650.00 |
| 338.20 | 0.9170 | 11500.00 |
| 338.20 | 0.9500 | 10430.00 |
| 338.20 | 0.9790 | 7670.00 |
| 348.20 | 0.8240 | 13150.00 |
| 348.20 | 0.8580 | 12910.00 |
| 348.20 | 0.8860 | 12760.00 |
| 348.20 | 0.9170 | 12390.00 |
| 348.20 | 0.9500 | 11100.00 |
| 348.20 | 0.9790 | 7930.00 |
Sources
- Solubility of carbon dioxide in binary and ternary mixtures with ethanol and water
- Measurement and modelling of the ternary phase equilibria for high pressure carbon dioxide ethanol water mixtures
- Measurements of vapor-liquid equilibrium in both binary carbon dioxide-ethanol and ternary carbon dioxide-ethanol-water systemswith a newly developed flow-type apparatus
- Phase equilibria of ternary systems of carbon dioxide + ethanol, dimethyl sulfoxide, or N,N-dimethyl formamide + water at elevated pressures including near critical regions
- Measurement and correlation of vapor-liquid distribution coefficients of flavonoids in high pressure carbon dioxide - ethanol - water systems
- High-pressure (vapour + liquid) equilibria for ternary systems composed by {(E)-2-hexenal or hexanal + carbon dioxide + water}: Partition coefficient measurement