- Name
- Benzene
- InChI
- InChI=1S/C6H6/c1-2-4-6-5-3-1/h1-6H
- InChI Key
- UHOVQNZJYSORNB-UHFFFAOYSA-N
- Formula
- C6H6
- SMILES
- c1ccccc1
- Mol. Weight (g/mol)
- 78.11
- CAS
- 71-43-2
- Name
- Tridecane
- InChI
- InChI=1S/C13H28/c1-3-5-7-9-11-13-12-10-8-6-4-2/h3-13H2,1-2H3
- InChI Key
- IIYFAKIEWZDVMP-UHFFFAOYSA-N
- Formula
- C13H28
- SMILES
- CCCCCCCCCCCCC
- Mol. Weight (g/mol)
- 184.36
- CAS
- 629-50-5
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Datasets
Vapor or sublimation pressure, kPa [ref]
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Tridecane (2) - Liquid | Vapor or sublimation pressure, kPa - Liquid |
| 293.15 | 0.0000 | 53620.00 |
| 293.15 | 0.0210 | 60310.00 |
| 293.15 | 0.0967 | 90350.00 |
| 293.15 | 0.1788 | 115270.00 |
| 293.15 | 0.2642 | 148190.00 |
| 293.15 | 0.3379 | 180660.00 |
| 293.15 | 0.3723 | 198150.00 |
| 293.15 | 0.4196 | 216440.00 |
| 293.15 | 0.4735 | 228840.00 |
| 293.15 | 0.5008 | 220050.00 |
| 293.15 | 0.5762 | 208350.00 |
| 293.15 | 0.6587 | 196050.00 |
| 293.15 | 0.7373 | 179340.00 |
| 293.15 | 0.8164 | 167280.00 |
| 293.15 | 0.9024 | 150680.00 |
| 293.15 | 1.0000 | 133010.00 |
| 303.15 | 0.0000 | 92220.00 |
| 303.15 | 0.0210 | 100130.00 |
| 303.15 | 0.0967 | 128040.00 |
| 303.15 | 0.1788 | 161600.00 |
| 303.15 | 0.2642 | 203150.00 |
| 303.15 | 0.3379 | 248680.00 |
| 303.15 | 0.3723 | 266090.00 |
| 303.15 | 0.4196 | 285750.00 |
| 303.15 | 0.4735 | 304200.00 |
| 303.15 | 0.5008 | 293270.00 |
| 303.15 | 0.5762 | 278330.00 |
| 303.15 | 0.6587 | 261160.00 |
| 303.15 | 0.7373 | 248940.00 |
| 303.15 | 0.8164 | 231950.00 |
| 303.15 | 0.9024 | 215720.00 |
| 303.15 | 1.0000 | 197130.00 |
| 313.15 | 0.0000 | 133290.00 |
| 313.15 | 0.0210 | 142240.00 |
| 313.15 | 0.0967 | 170060.00 |
| 313.15 | 0.1788 | 211900.00 |
| 313.15 | 0.2642 | 252180.00 |
| 313.15 | 0.3379 | 310160.00 |
| 313.15 | 0.3723 | 335840.00 |
| 313.15 | 0.4196 | 360880.00 |
| 313.15 | 0.4735 | 381570.00 |
| 313.15 | 0.5008 | 371100.00 |
| 313.15 | 0.5762 | 354750.00 |
| 313.15 | 0.6587 | 333950.00 |
| 313.15 | 0.7373 | 319490.00 |
| 313.15 | 0.8164 | 302670.00 |
| 313.15 | 0.9024 | 286000.00 |
| 313.15 | 1.0000 | 265400.00 |
| 323.15 | 0.0000 | 176820.00 |
| 323.15 | 0.0210 | 186640.00 |
| 323.15 | 0.0967 | 216430.00 |
| 323.15 | 0.1788 | 266170.00 |
| 323.15 | 0.2642 | 314130.00 |
| 323.15 | 0.3379 | 366160.00 |
| 323.15 | 0.3723 | 407470.00 |
| 323.15 | 0.4196 | 441820.00 |
| 323.15 | 0.4735 | 469990.00 |
| 323.15 | 0.5008 | 458840.00 |
| 323.15 | 0.5762 | 437600.00 |
| 323.15 | 0.6587 | 414440.00 |
| 323.15 | 0.7373 | 399820.00 |
| 323.15 | 0.8164 | 379420.00 |
| 323.15 | 0.9024 | 361540.00 |
| 323.15 | 1.0000 | 337830.00 |
| 333.15 | 0.0000 | 222810.00 |
| 333.15 | 0.0210 | 233320.00 |
| 333.15 | 0.0967 | 267130.00 |
| 333.15 | 0.1788 | 324420.00 |
| 333.15 | 0.2642 | 382700.00 |
| 333.15 | 0.3379 | 453840.00 |
| 333.15 | 0.3723 | 497950.00 |
| 333.15 | 0.4196 | 528580.00 |
| 333.15 | 0.4735 | 565480.00 |
| 333.15 | 0.5008 | 553650.00 |
| 333.15 | 0.5762 | 526900.00 |
| 333.15 | 0.6587 | 502620.00 |
| 333.15 | 0.7373 | 481100.00 |
| 333.15 | 0.8164 | 462220.00 |
| 333.15 | 0.9024 | 442330.00 |
| 333.15 | 1.0000 | 414420.00 |
| 343.15 | 0.0000 | 271270.00 |
| 343.15 | 0.0210 | 282300.00 |
| 343.15 | 0.0967 | 322180.00 |
| 343.15 | 0.1788 | 386630.00 |
| 343.15 | 0.2642 | 457910.00 |
| 343.15 | 0.3379 | 540640.00 |
| 343.15 | 0.3723 | 585480.00 |
| 343.15 | 0.4196 | 621150.00 |
| 343.15 | 0.4735 | 680100.00 |
| 343.15 | 0.5008 | 660410.00 |
| 343.15 | 0.5762 | 622640.00 |
| 343.15 | 0.6587 | 598500.00 |
| 343.15 | 0.7373 | 566270.00 |
| 343.15 | 0.8164 | 551050.00 |
| 343.15 | 0.9024 | 528380.00 |
| 343.15 | 1.0000 | 495180.00 |
Vapor or sublimation pressure, kPa [ref]
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Tridecane (2) - Liquid | Vapor or sublimation pressure, kPa - Liquid |
| 293.15 | 0.0000 | 53620.00 |
| 293.15 | 0.0210 | 60310.00 |
| 293.15 | 0.0967 | 90350.00 |
| 293.15 | 0.1788 | 115270.00 |
| 293.15 | 0.2642 | 148190.00 |
| 293.15 | 0.3379 | 180660.00 |
| 293.15 | 0.3723 | 198150.00 |
| 293.15 | 0.4196 | 216440.00 |
| 293.15 | 0.4735 | 228840.00 |
| 293.15 | 0.5008 | 220050.00 |
| 293.15 | 0.5762 | 208350.00 |
| 293.15 | 0.6587 | 196050.00 |
| 293.15 | 0.7373 | 179340.00 |
| 293.15 | 0.8164 | 167280.00 |
| 293.15 | 0.9024 | 150680.00 |
| 293.15 | 1.0000 | 133010.00 |
| 303.15 | 0.0000 | 92220.00 |
| 303.15 | 0.0210 | 100130.00 |
| 303.15 | 0.0967 | 128040.00 |
| 303.15 | 0.1788 | 161600.00 |
| 303.15 | 0.2642 | 203150.00 |
| 303.15 | 0.3379 | 248680.00 |
| 303.15 | 0.3723 | 266090.00 |
| 303.15 | 0.4196 | 285750.00 |
| 303.15 | 0.4735 | 304200.00 |
| 303.15 | 0.5008 | 293270.00 |
| 303.15 | 0.5762 | 278330.00 |
| 303.15 | 0.6587 | 261160.00 |
| 303.15 | 0.7373 | 248940.00 |
| 303.15 | 0.8164 | 231950.00 |
| 303.15 | 0.9024 | 215720.00 |
| 303.15 | 1.0000 | 197130.00 |
| 313.15 | 0.0000 | 133290.00 |
| 313.15 | 0.0210 | 142240.00 |
| 313.15 | 0.0967 | 170060.00 |
| 313.15 | 0.1788 | 211900.00 |
| 313.15 | 0.2642 | 252180.00 |
| 313.15 | 0.3379 | 310160.00 |
| 313.15 | 0.3723 | 335840.00 |
| 313.15 | 0.4196 | 360880.00 |
| 313.15 | 0.4735 | 381570.00 |
| 313.15 | 0.5008 | 371100.00 |
| 313.15 | 0.5762 | 354750.00 |
| 313.15 | 0.6587 | 333950.00 |
| 313.15 | 0.7373 | 319490.00 |
| 313.15 | 0.8164 | 302670.00 |
| 313.15 | 0.9024 | 286000.00 |
| 313.15 | 1.0000 | 265400.00 |
| 323.15 | 0.0000 | 176820.00 |
| 323.15 | 0.0210 | 186640.00 |
| 323.15 | 0.0967 | 216430.00 |
| 323.15 | 0.1788 | 266170.00 |
| 323.15 | 0.2642 | 314130.00 |
| 323.15 | 0.3379 | 366160.00 |
| 323.15 | 0.3723 | 407470.00 |
| 323.15 | 0.4196 | 441820.00 |
| 323.15 | 0.4735 | 469990.00 |
| 323.15 | 0.5008 | 458840.00 |
| 323.15 | 0.5762 | 437600.00 |
| 323.15 | 0.6587 | 414440.00 |
| 323.15 | 0.7373 | 399820.00 |
| 323.15 | 0.8164 | 379420.00 |
| 323.15 | 0.9024 | 361540.00 |
| 323.15 | 1.0000 | 337830.00 |
| 333.15 | 0.0000 | 222810.00 |
| 333.15 | 0.0210 | 233320.00 |
| 333.15 | 0.0967 | 267130.00 |
| 333.15 | 0.1788 | 324420.00 |
| 333.15 | 0.2642 | 382700.00 |
| 333.15 | 0.3379 | 453840.00 |
| 333.15 | 0.3723 | 497950.00 |
| 333.15 | 0.4196 | 528580.00 |
| 333.15 | 0.4735 | 565480.00 |
| 333.15 | 0.5008 | 553650.00 |
| 333.15 | 0.5762 | 526900.00 |
| 333.15 | 0.6587 | 502620.00 |
| 333.15 | 0.7373 | 481100.00 |
| 333.15 | 0.8164 | 462220.00 |
| 333.15 | 0.9024 | 442330.00 |
| 333.15 | 1.0000 | 414420.00 |
| 343.15 | 0.0000 | 271270.00 |
| 343.15 | 0.0210 | 282300.00 |
| 343.15 | 0.0967 | 322180.00 |
| 343.15 | 0.1788 | 386630.00 |
| 343.15 | 0.2642 | 457910.00 |
| 343.15 | 0.3379 | 540640.00 |
| 343.15 | 0.3723 | 585480.00 |
| 343.15 | 0.4196 | 621150.00 |
| 343.15 | 0.4735 | 680100.00 |
| 343.15 | 0.5008 | 660410.00 |
| 343.15 | 0.5762 | 622640.00 |
| 343.15 | 0.6587 | 598500.00 |
| 343.15 | 0.7373 | 566270.00 |
| 343.15 | 0.8164 | 551050.00 |
| 343.15 | 0.9024 | 528380.00 |
| 343.15 | 1.0000 | 495180.00 |
Solid-liquid equilibrium temperature, K [ref]
Operational condition: Pressure, kPa = 100 (Liquid)
| Mole fraction of Tridecane (2) - Liquid | Solid-liquid equilibrium temperature, K - Liquid |
|---|---|
| 0.5019 | 257.02 |
| 0.5309 | 258.05 |
| 0.5496 | 258.62 |
| 0.5692 | 258.99 |
| 0.5910 | 259.35 |
| 0.6135 | 260.01 |
| 0.6300 | 260.55 |
| 0.6702 | 261.65 |
| 0.7087 | 262.57 |
| 0.7418 | 263.32 |
| 0.7733 | 264.17 |
| 0.8022 | 264.83 |
| 0.8633 | 266.27 |
| 0.8893 | 266.92 |
| 0.9229 | 267.51 |
| 0.9489 | 268.15 |
| 1.0000 | 269.01 |
Solid-liquid equilibrium temperature, K [ref]
Operational condition: Pressure, kPa = 100 (Liquid)
| Mole fraction of Tridecane (2) - Liquid | Solid-liquid equilibrium temperature, K - Liquid |
|---|---|
| 0.4757 | 255.71 |
| 0.4836 | 256.30 |
Solid-liquid equilibrium temperature, K [ref]
Operational condition: Pressure, kPa = 100 (Liquid)
| Mole fraction of Tridecane (2) - Liquid | Solid-liquid equilibrium temperature, K - Liquid |
|---|---|
| 0.0000 | 279.05 |
| 0.0323 | 277.80 |
| 0.0407 | 277.27 |
| 0.0492 | 276.68 |
| 0.0588 | 276.17 |
| 0.0682 | 275.68 |
| 0.0861 | 274.67 |
| 0.1042 | 273.70 |
| 0.1201 | 273.06 |
| 0.1351 | 272.32 |
| 0.1517 | 271.44 |
| 0.1745 | 270.49 |
| 0.1960 | 269.57 |
| 0.2210 | 268.36 |
| 0.2504 | 266.91 |
| 0.2804 | 265.90 |
| 0.2966 | 265.01 |
| 0.3242 | 263.50 |
| 0.3618 | 261.45 |
| 0.3955 | 259.65 |
| 0.4226 | 258.04 |
| 0.4381 | 257.11 |
| 0.4592 | 256.23 |
Solid-liquid equilibrium temperature, K [ref]
Operational condition: Pressure, kPa = 100 (Liquid)
| Mole fraction of Tridecane (2) - Liquid | Solid-liquid equilibrium temperature, K - Liquid |
|---|---|
| 0.5019 | 257.02 |
| 0.5309 | 258.05 |
| 0.5496 | 258.62 |
| 0.5692 | 258.99 |
| 0.5910 | 259.35 |
| 0.6135 | 260.01 |
| 0.6300 | 260.55 |
| 0.6702 | 261.65 |
| 0.7087 | 262.57 |
| 0.7418 | 263.32 |
| 0.7733 | 264.17 |
| 0.8022 | 264.83 |
| 0.8633 | 266.27 |
| 0.8893 | 266.92 |
| 0.9229 | 267.51 |
| 0.9489 | 268.15 |
| 1.0000 | 269.01 |
Solid-liquid equilibrium temperature, K [ref]
Operational condition: Pressure, kPa = 100 (Liquid)
| Mole fraction of Tridecane (2) - Liquid | Solid-liquid equilibrium temperature, K - Liquid |
|---|---|
| 0.4757 | 255.71 |
| 0.4836 | 256.30 |
Solid-liquid equilibrium temperature, K [ref]
Operational condition: Pressure, kPa = 100 (Liquid)
| Mole fraction of Tridecane (2) - Liquid | Solid-liquid equilibrium temperature, K - Liquid |
|---|---|
| 0.0000 | 279.05 |
| 0.0323 | 277.80 |
| 0.0407 | 277.27 |
| 0.0492 | 276.68 |
| 0.0588 | 276.17 |
| 0.0682 | 275.68 |
| 0.0861 | 274.67 |
| 0.1042 | 273.70 |
| 0.1201 | 273.06 |
| 0.1351 | 272.32 |
| 0.1517 | 271.44 |
| 0.1745 | 270.49 |
| 0.1960 | 269.57 |
| 0.2210 | 268.36 |
| 0.2504 | 266.91 |
| 0.2804 | 265.90 |
| 0.2966 | 265.01 |
| 0.3242 | 263.50 |
| 0.3618 | 261.45 |
| 0.3955 | 259.65 |
| 0.4226 | 258.04 |
| 0.4381 | 257.11 |
| 0.4592 | 256.23 |