Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Mole fraction of Ethanol (1) - Liquid | Mole fraction of Decanedioic acid (2) - Liquid | Solid-liquid equilibrium temperature, K - Liquid |
0.0000 | 0.0000 | 321.95 |
0.0000 | 0.0001 | 327.45 |
0.0000 | 0.0001 | 329.44 |
0.0000 | 0.0001 | 331.61 |
0.0000 | 0.0001 | 334.01 |
0.0000 | 0.0002 | 336.96 |
0.0000 | 0.0002 | 339.68 |
0.0000 | 0.0002 | 341.72 |
0.0000 | 0.0002 | 343.83 |
0.0000 | 0.0003 | 347.40 |
0.0000 | 0.0003 | 350.20 |
0.0825 | 0.0130 | 352.75 |
0.0829 | 0.0083 | 350.15 |
0.0831 | 0.0057 | 348.25 |
0.0832 | 0.0038 | 344.65 |
0.0833 | 0.0027 | 341.55 |
0.0834 | 0.0020 | 337.95 |
0.0834 | 0.0014 | 334.85 |
0.0835 | 0.0011 | 331.95 |
0.0835 | 0.0008 | 328.35 |
0.0835 | 0.0006 | 325.65 |
0.0835 | 0.0004 | 323.55 |
0.0835 | 0.0003 | 319.85 |
0.0835 | 0.0001 | 310.55 |
0.0835 | 0.0002 | 315.65 |
0.0835 | 0.0000 | 302.05 |
0.2557 | 0.0901 | 351.35 |
0.2607 | 0.0724 | 346.55 |
0.2652 | 0.0561 | 342.05 |
0.2696 | 0.0407 | 336.85 |
0.2738 | 0.0257 | 329.75 |
0.2760 | 0.0178 | 324.75 |
0.2780 | 0.0107 | 317.75 |
0.2783 | 0.0096 | 316.25 |
0.2789 | 0.0075 | 312.75 |
0.2791 | 0.0066 | 310.95 |
0.2795 | 0.0052 | 307.75 |
0.2800 | 0.0037 | 302.95 |
0.2802 | 0.0029 | 299.95 |
0.2804 | 0.0022 | 296.45 |
0.2805 | 0.0017 | 293.45 |
0.2807 | 0.0011 | 288.65 |
0.2807 | 0.0012 | 290.15 |
0.5133 | 0.1584 | 353.45 |
0.5171 | 0.1522 | 352.75 |
0.5244 | 0.1402 | 350.35 |
0.5313 | 0.1290 | 347.75 |
0.5457 | 0.1053 | 342.45 |
0.5523 | 0.0945 | 339.25 |
0.5570 | 0.0867 | 337.55 |
0.5656 | 0.0727 | 333.35 |
0.5676 | 0.0694 | 331.55 |
0.5769 | 0.0541 | 325.95 |
0.5834 | 0.0435 | 321.65 |
0.5901 | 0.0326 | 315.35 |
0.5920 | 0.0294 | 313.45 |
0.5949 | 0.0246 | 309.35 |
0.5985 | 0.0187 | 304.05 |
0.6008 | 0.0150 | 300.45 |
0.6027 | 0.0120 | 296.35 |
0.6037 | 0.0102 | 293.85 |
0.6056 | 0.0072 | 288.85 |
0.8824 | 0.1176 | 341.19 |
0.8908 | 0.1092 | 339.11 |
0.9014 | 0.0986 | 336.53 |
0.9102 | 0.0898 | 334.38 |
0.9194 | 0.0806 | 331.73 |
0.9282 | 0.0718 | 328.18 |
0.9359 | 0.0641 | 325.42 |
0.9422 | 0.0578 | 322.90 |
0.9481 | 0.0519 | 320.31 |
0.9563 | 0.0437 | 315.97 |
0.9617 | 0.0383 | 313.21 |
0.9669 | 0.0331 | 309.95 |
0.9710 | 0.0290 | 307.33 |
0.9732 | 0.0268 | 304.52 |
0.9770 | 0.0230 | 301.61 |
0.9808 | 0.0192 | 298.15 |
0.9822 | 0.0178 | 296.45 |
0.9849 | 0.0151 | 293.22 |
0.9877 | 0.0123 | 289.75 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Solvent: Mole fraction of Ethanol (1) - Liquid | Mole fraction of Decanedioic acid (2) - Liquid | Solid-liquid equilibrium temperature, K - Liquid |
0.1435 | 0.0001 | 289.30 |
0.1435 | 0.0001 | 295.54 |
0.1435 | 0.0001 | 295.59 |
0.1435 | 0.0002 | 303.14 |
0.1435 | 0.0004 | 305.49 |
0.1435 | 0.0005 | 308.31 |
0.1435 | 0.0007 | 310.34 |
0.1435 | 0.0009 | 313.16 |
0.1435 | 0.0011 | 317.05 |
0.1435 | 0.0014 | 319.80 |
0.1435 | 0.0019 | 322.49 |
0.1435 | 0.0026 | 325.53 |
0.1435 | 0.0033 | 327.71 |
0.1435 | 0.0051 | 330.68 |
0.1435 | 0.0073 | 334.78 |
0.1435 | 0.0104 | 337.59 |
0.1435 | 0.0143 | 340.74 |
0.1435 | 0.0179 | 343.69 |
0.1435 | 0.0207 | 345.80 |
0.1435 | 0.0257 | 348.68 |
0.1435 | 0.0289 | 350.74 |
0.3697 | 0.0010 | 288.47 |
0.3697 | 0.0018 | 290.55 |
0.3697 | 0.0027 | 292.67 |
0.3697 | 0.0034 | 296.97 |
0.3697 | 0.0042 | 298.05 |
0.3697 | 0.0053 | 300.16 |
0.3697 | 0.0068 | 303.65 |
0.3697 | 0.0086 | 306.66 |
0.3697 | 0.0096 | 309.06 |
0.3697 | 0.0113 | 309.87 |
0.3697 | 0.0144 | 313.70 |
0.3697 | 0.0157 | 316.14 |
0.3697 | 0.0198 | 318.45 |
0.3697 | 0.0241 | 321.57 |
0.3697 | 0.0294 | 325.86 |
0.3697 | 0.0307 | 326.92 |
0.3697 | 0.0362 | 328.87 |
0.3697 | 0.0424 | 331.34 |
0.3697 | 0.0491 | 334.33 |
0.3697 | 0.0556 | 336.44 |
0.3697 | 0.0624 | 338.74 |
0.3697 | 0.0691 | 340.33 |
0.3697 | 0.0736 | 341.96 |
0.3697 | 0.0835 | 344.16 |
0.3697 | 0.0922 | 346.04 |
0.3697 | 0.1002 | 348.01 |
0.3697 | 0.1085 | 350.08 |
0.7981 | 0.0094 | 292.46 |
0.7981 | 0.0145 | 295.74 |
0.7981 | 0.0202 | 300.80 |
0.7981 | 0.0248 | 305.24 |
0.7981 | 0.0297 | 308.56 |
0.7981 | 0.0353 | 311.91 |
0.7981 | 0.0420 | 316.01 |
0.7981 | 0.0503 | 319.91 |
0.7981 | 0.0549 | 321.52 |
0.7981 | 0.0639 | 325.39 |
0.7981 | 0.0733 | 328.73 |
0.7981 | 0.0846 | 332.44 |
0.7981 | 0.0939 | 335.53 |
0.7981 | 0.1046 | 337.88 |
0.7981 | 0.1167 | 340.48 |
0.7981 | 0.1306 | 344.04 |
0.9000 | 0.0270 | 305.77 |
0.9000 | 0.0389 | 313.76 |
0.9000 | 0.0536 | 321.26 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Mole fraction of Ethanol (1) - Liquid | Mole fraction of Decanedioic acid (2) - Liquid | Solid-liquid equilibrium temperature, K - Liquid |
0.0000 | 0.0000 | 321.95 |
0.0000 | 0.0001 | 327.45 |
0.0000 | 0.0001 | 329.44 |
0.0000 | 0.0001 | 331.61 |
0.0000 | 0.0001 | 334.01 |
0.0000 | 0.0002 | 336.96 |
0.0000 | 0.0002 | 339.68 |
0.0000 | 0.0002 | 341.72 |
0.0000 | 0.0002 | 343.83 |
0.0000 | 0.0003 | 347.40 |
0.0000 | 0.0003 | 350.20 |
0.0825 | 0.0130 | 352.75 |
0.0829 | 0.0083 | 350.15 |
0.0831 | 0.0057 | 348.25 |
0.0832 | 0.0038 | 344.65 |
0.0833 | 0.0027 | 341.55 |
0.0834 | 0.0020 | 337.95 |
0.0834 | 0.0014 | 334.85 |
0.0835 | 0.0011 | 331.95 |
0.0835 | 0.0008 | 328.35 |
0.0835 | 0.0006 | 325.65 |
0.0835 | 0.0004 | 323.55 |
0.0835 | 0.0003 | 319.85 |
0.0835 | 0.0001 | 310.55 |
0.0835 | 0.0002 | 315.65 |
0.0835 | 0.0000 | 302.05 |
0.2557 | 0.0901 | 351.35 |
0.2607 | 0.0724 | 346.55 |
0.2652 | 0.0561 | 342.05 |
0.2696 | 0.0407 | 336.85 |
0.2738 | 0.0257 | 329.75 |
0.2760 | 0.0178 | 324.75 |
0.2780 | 0.0107 | 317.75 |
0.2783 | 0.0096 | 316.25 |
0.2789 | 0.0075 | 312.75 |
0.2791 | 0.0066 | 310.95 |
0.2795 | 0.0052 | 307.75 |
0.2800 | 0.0037 | 302.95 |
0.2802 | 0.0029 | 299.95 |
0.2804 | 0.0022 | 296.45 |
0.2805 | 0.0017 | 293.45 |
0.2807 | 0.0011 | 288.65 |
0.2807 | 0.0012 | 290.15 |
0.5133 | 0.1584 | 353.45 |
0.5171 | 0.1522 | 352.75 |
0.5244 | 0.1402 | 350.35 |
0.5313 | 0.1290 | 347.75 |
0.5457 | 0.1053 | 342.45 |
0.5523 | 0.0945 | 339.25 |
0.5570 | 0.0867 | 337.55 |
0.5656 | 0.0727 | 333.35 |
0.5676 | 0.0694 | 331.55 |
0.5769 | 0.0541 | 325.95 |
0.5834 | 0.0435 | 321.65 |
0.5901 | 0.0326 | 315.35 |
0.5920 | 0.0294 | 313.45 |
0.5949 | 0.0246 | 309.35 |
0.5985 | 0.0187 | 304.05 |
0.6008 | 0.0150 | 300.45 |
0.6027 | 0.0120 | 296.35 |
0.6037 | 0.0102 | 293.85 |
0.6056 | 0.0072 | 288.85 |
0.8824 | 0.1176 | 341.19 |
0.8908 | 0.1092 | 339.11 |
0.9014 | 0.0986 | 336.53 |
0.9102 | 0.0898 | 334.38 |
0.9194 | 0.0806 | 331.73 |
0.9282 | 0.0718 | 328.18 |
0.9359 | 0.0641 | 325.42 |
0.9422 | 0.0578 | 322.90 |
0.9481 | 0.0519 | 320.31 |
0.9563 | 0.0437 | 315.97 |
0.9617 | 0.0383 | 313.21 |
0.9669 | 0.0331 | 309.95 |
0.9710 | 0.0290 | 307.33 |
0.9732 | 0.0268 | 304.52 |
0.9770 | 0.0230 | 301.61 |
0.9808 | 0.0192 | 298.15 |
0.9822 | 0.0178 | 296.45 |
0.9849 | 0.0151 | 293.22 |
0.9877 | 0.0123 | 289.75 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Solvent: Mole fraction of Ethanol (1) - Liquid | Mole fraction of Decanedioic acid (2) - Liquid | Solid-liquid equilibrium temperature, K - Liquid |
0.1435 | 0.0001 | 289.30 |
0.1435 | 0.0001 | 295.54 |
0.1435 | 0.0001 | 295.59 |
0.1435 | 0.0002 | 303.14 |
0.1435 | 0.0004 | 305.49 |
0.1435 | 0.0005 | 308.31 |
0.1435 | 0.0007 | 310.34 |
0.1435 | 0.0009 | 313.16 |
0.1435 | 0.0011 | 317.05 |
0.1435 | 0.0014 | 319.80 |
0.1435 | 0.0019 | 322.49 |
0.1435 | 0.0026 | 325.53 |
0.1435 | 0.0033 | 327.71 |
0.1435 | 0.0051 | 330.68 |
0.1435 | 0.0073 | 334.78 |
0.1435 | 0.0104 | 337.59 |
0.1435 | 0.0143 | 340.74 |
0.1435 | 0.0179 | 343.69 |
0.1435 | 0.0207 | 345.80 |
0.1435 | 0.0257 | 348.68 |
0.1435 | 0.0289 | 350.74 |
0.3697 | 0.0010 | 288.47 |
0.3697 | 0.0018 | 290.55 |
0.3697 | 0.0027 | 292.67 |
0.3697 | 0.0034 | 296.97 |
0.3697 | 0.0042 | 298.05 |
0.3697 | 0.0053 | 300.16 |
0.3697 | 0.0068 | 303.65 |
0.3697 | 0.0086 | 306.66 |
0.3697 | 0.0096 | 309.06 |
0.3697 | 0.0113 | 309.87 |
0.3697 | 0.0144 | 313.70 |
0.3697 | 0.0157 | 316.14 |
0.3697 | 0.0198 | 318.45 |
0.3697 | 0.0241 | 321.57 |
0.3697 | 0.0294 | 325.86 |
0.3697 | 0.0307 | 326.92 |
0.3697 | 0.0362 | 328.87 |
0.3697 | 0.0424 | 331.34 |
0.3697 | 0.0491 | 334.33 |
0.3697 | 0.0556 | 336.44 |
0.3697 | 0.0624 | 338.74 |
0.3697 | 0.0691 | 340.33 |
0.3697 | 0.0736 | 341.96 |
0.3697 | 0.0835 | 344.16 |
0.3697 | 0.0922 | 346.04 |
0.3697 | 0.1002 | 348.01 |
0.3697 | 0.1085 | 350.08 |
0.7981 | 0.0094 | 292.46 |
0.7981 | 0.0145 | 295.74 |
0.7981 | 0.0202 | 300.80 |
0.7981 | 0.0248 | 305.24 |
0.7981 | 0.0297 | 308.56 |
0.7981 | 0.0353 | 311.91 |
0.7981 | 0.0420 | 316.01 |
0.7981 | 0.0503 | 319.91 |
0.7981 | 0.0549 | 321.52 |
0.7981 | 0.0639 | 325.39 |
0.7981 | 0.0733 | 328.73 |
0.7981 | 0.0846 | 332.44 |
0.7981 | 0.0939 | 335.53 |
0.7981 | 0.1046 | 337.88 |
0.7981 | 0.1167 | 340.48 |
0.7981 | 0.1306 | 344.04 |
0.9000 | 0.0270 | 305.77 |
0.9000 | 0.0389 | 313.76 |
0.9000 | 0.0536 | 321.26 |