Property | Value | Unit | Source |
---|---|---|---|
ω | 0.2580 | KDB | |
AP | 322.950 | K | KDB |
ΔcH°liquid | [-5876.60; -5875.80] | kJ/mol |
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ΔcH°liquid | -5876.60 ± 0.92 | kJ/mol | NIST |
ΔcH°liquid | -5875.80 ± 1.10 | kJ/mol | NIST |
ΔfG° | 47.35 | kJ/mol | KDB |
Δc,grossH | 5875.76 | kJ/mol | KDB |
Δc,netH | 5479.660 | kJ/mol | KDB |
ΔfH°gas | [-193.40; -192.40] | kJ/mol |
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ΔfH°gas | -193.40 | kJ/mol | KDB |
ΔfH°gas | -192.40 | kJ/mol | NIST |
ΔfH°gas | -193.30 ± 1.30 | kJ/mol | NIST |
ΔfH°liquid | [-238.40; -237.50] | kJ/mol |
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ΔfH°liquid | -237.50 ± 1.10 | kJ/mol | NIST |
ΔfH°liquid | -238.40 ± 1.30 | kJ/mol | NIST |
ΔfusH° | 10.90 | kJ/mol | Joback Calculated Property |
ΔvapH° | [42.80; 45.20] | kJ/mol |
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ΔvapH° | 45.10 | kJ/mol | NIST |
ΔvapH° | Outlier 42.80 ± 0.50 | kJ/mol | NIST |
ΔvapH° | 44.70 ± 0.40 | kJ/mol | NIST |
ΔvapH° | 44.70 ± 0.40 | kJ/mol | NIST |
ΔvapH° | 45.20 | kJ/mol | NIST |
ΔvapH° | 45.15 | kJ/mol | NIST |
ΔvapH° | 45.10 | kJ/mol | NIST |
ΔvapH° | 45.20 | kJ/mol | NIST |
ΔvapH° | 45.08 | kJ/mol | NIST |
ΔvapH° | 45.10 | kJ/mol | NIST |
IE | 9.46 | eV | NIST |
log10WS | -3.24 | Crippen Calculated Property | |
logPoct/wat | 3.367 | Crippen Calculated Property | |
McVol | 126.810 | ml/mol | McGowan Calculated Property |
Pc | [2800.00; 2860.00] | kPa |
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Pc | 2800.00 | kPa | KDB |
Pc | 2860.00 | kPa | Critica... |
Inp | [915.00; 962.10] |
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|
Inp | 938.00 | NIST | |
Inp | 951.00 | NIST | |
Inp | 926.00 | NIST | |
Inp | Outlier 952.30 | NIST | |
Inp | Outlier 962.10 | NIST | |
Inp | 936.00 | NIST | |
Inp | 936.40 | NIST | |
Inp | 947.00 | NIST | |
Inp | 931.00 | NIST | |
Inp | 937.00 | NIST | |
Inp | 940.00 | NIST | |
Inp | 934.00 | NIST | |
Inp | 938.00 | NIST | |
Inp | 942.00 | NIST | |
Inp | 945.00 | NIST | |
Inp | 943.00 | NIST | |
Inp | 946.00 | NIST | |
Inp | 948.00 | NIST | |
Inp | 950.00 | NIST | |
Inp | 952.00 | NIST | |
Inp | 944.00 | NIST | |
Inp | 932.00 | NIST | |
Inp | 925.00 | NIST | |
Inp | 928.00 | NIST | |
Inp | 930.00 | NIST | |
Inp | 933.00 | NIST | |
Inp | 937.00 | NIST | |
Inp | 925.00 | NIST | |
Inp | 944.00 | NIST | |
Inp | 931.00 | NIST | |
Inp | 944.00 | NIST | |
Inp | 925.00 | NIST | |
Inp | 926.00 | NIST | |
Inp | 923.00 | NIST | |
Inp | 931.00 | NIST | |
Inp | 935.00 | NIST | |
Inp | 923.00 | NIST | |
Inp | 950.00 | NIST | |
Inp | 928.00 | NIST | |
Inp | 938.00 | NIST | |
Inp | 934.00 | NIST | |
Inp | 941.00 | NIST | |
Inp | 930.50 | NIST | |
Inp | 927.10 | NIST | |
Inp | 926.40 | NIST | |
Inp | 924.20 | NIST | |
Inp | 927.10 | NIST | |
Inp | 929.10 | NIST | |
Inp | 936.40 | NIST | |
Inp | 926.40 | NIST | |
Inp | 916.00 | NIST | |
Inp | 924.20 | NIST | |
Inp | 927.10 | NIST | |
Inp | 929.10 | NIST | |
Inp | 927.10 | NIST | |
Inp | 926.40 | NIST | |
Inp | 925.22 | NIST | |
Inp | 920.09 | NIST | |
Inp | 923.67 | NIST | |
Inp | 925.93 | NIST | |
Inp | 925.46 | NIST | |
Inp | 929.15 | NIST | |
Inp | 931.59 | NIST | |
Inp | 923.00 | NIST | |
Inp | 933.00 | NIST | |
Inp | 950.33 | NIST | |
Inp | 927.00 | NIST | |
Inp | 936.00 | NIST | |
Inp | 935.00 | NIST | |
Inp | 930.00 | NIST | |
Inp | 944.00 | NIST | |
Inp | 938.00 | NIST | |
Inp | 939.00 | NIST | |
Inp | 922.00 | NIST | |
Inp | 915.00 | NIST | |
Inp | 931.00 | NIST | |
Inp | 937.00 | NIST | |
Inp | 937.00 | NIST | |
Inp | 933.00 | NIST | |
Inp | 921.00 | NIST | |
Inp | 923.00 | NIST | |
I | [982.00; 1019.00] |
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|
I | 1019.00 | NIST | |
I | 998.00 | NIST | |
I | 1003.00 | NIST | |
I | 1008.00 | NIST | |
I | 1019.00 | NIST | |
I | 982.00 | NIST | |
I | 982.00 | NIST | |
S°gas | 419.86 | J/mol×K | NIST |
S°liquid | 311.88 | J/mol×K | NIST |
Tboil | 429.90 | K | KDB |
Tc | [630.80; 639.00] | K |
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Tc | 639.00 | K | KDB |
Tc | 630.80 | K | Gas-Liq... |
Tfus | [178.06; 178.70] | K |
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Tfus | 178.70 | K | KDB |
Tfus | 178.09 ± 0.20 | K | NIST |
Tfus | 178.19 ± 0.02 | K | NIST |
Tfus | 178.06 ± 0.10 | K | NIST |
Ttriple | 178.25 ± 0.02 | K | NIST |
Vc | 0.472 | m3/kmol | KDB |
Zc | 0.2490130 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [255.25; 353.84] | J/mol×K | [424.87; 623.81] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 260 280 300 320 340 360 450 500 550 600 | ||||
Cp,gas | 255.25 | J/mol×K | 424.87 | Joback Calculated Property |
Cp,gas | 273.81 | J/mol×K | 458.03 | Joback Calculated Property |
Cp,gas | 291.49 | J/mol×K | 491.18 | Joback Calculated Property |
Cp,gas | 308.31 | J/mol×K | 524.34 | Joback Calculated Property |
Cp,gas | 324.30 | J/mol×K | 557.50 | Joback Calculated Property |
Cp,gas | 339.46 | J/mol×K | 590.65 | Joback Calculated Property |
Cp,gas | 353.84 | J/mol×K | 623.81 | Joback Calculated Property |
Cp,liquid | 242.04 | J/mol×K | 298.15 | NIST |
η | [0.0002741; 0.0085410] | Pa×s | [198.57; 424.87] | ![]() |
T(K) Dynamic viscosity (Pa×s) 0 2.00e-3 4.00e-3 6.00e-3 8.00e-3 200 300 400 | ||||
η | 0.0085410 | Pa×s | 198.57 | Joback Calculated Property |
η | 0.0030472 | Pa×s | 236.29 | Joback Calculated Property |
η | 0.0014438 | Pa×s | 274.00 | Joback Calculated Property |
η | 0.0008196 | Pa×s | 311.72 | Joback Calculated Property |
η | 0.0005258 | Pa×s | 349.44 | Joback Calculated Property |
η | 0.0003678 | Pa×s | 387.15 | Joback Calculated Property |
η | 0.0002741 | Pa×s | 424.87 | Joback Calculated Property |
ΔfusH | [10.37; 13.07] | kJ/mol | [178.00; 178.30] | ![]() |
ΔfusH | 10.60 | kJ/mol | 178.00 | NIST |
ΔfusH | 13.07 | kJ/mol | 178.25 | NIST |
ΔfusH | 10.37 | kJ/mol | 178.30 | NIST |
ΔfusH | 10.37 | kJ/mol | 178.30 | NIST |
ΔvapH | [36.07; 41.70] | kJ/mol | [388.50; 429.90] | ![]() |
ΔvapH | 41.70 | kJ/mol | 388.50 | NIST |
ΔvapH | 36.07 | kJ/mol | 429.90 | KDB |
n0 | 1.43478 | 298.15 | KDB | |
ρl | [738.00; 797.42] | kg/m3 | [288.15; 363.15] | ![]() |
T(K) Liquid Density (kg/m3) 740 750 760 770 780 790 800 300 320 340 360 | ||||
ρl | 797.42 | kg/m3 | 288.15 | Thermop... |
ρl | 793.00 | kg/m3 | 293.00 | KDB |
ρl | 793.54 | kg/m3 | 293.15 | Densiti... |
ρl | 793.53 | kg/m3 | 293.15 | Thermop... |
ρl | 789.63 | kg/m3 | 298.15 | Thermop... |
ρl | 785.72 | kg/m3 | 303.15 | Thermop... |
ρl | 785.73 | kg/m3 | 303.15 | Densiti... |
ρl | 777.88 | kg/m3 | 313.15 | Thermop... |
ρl | 777.90 | kg/m3 | 313.15 | Densiti... |
ρl | 770.00 | kg/m3 | 323.15 | Thermop... |
ρl | 770.04 | kg/m3 | 323.15 | Densiti... |
ρl | 762.09 | kg/m3 | 333.15 | Thermop... |
ρl | 762.12 | kg/m3 | 333.15 | Densiti... |
ρl | 754.20 | kg/m3 | 343.15 | Densiti... |
ρl | 746.10 | kg/m3 | 353.15 | Densiti... |
ρl | 738.00 | kg/m3 | 363.15 | Densiti... |
ΔfusS | 58.19 | J/mol×K | 178.25 | NIST |
γ | 0.03 | N/m | 298.20 | KDB |
Fixed | Measured | |
---|---|---|
Pressure, kPa - Gas | Temperature, K - Gas | Thermal conductivity, W/m/K - Gas |
83.00 | 481.25 | 0.0276 |
83.00 | 481.94 | 0.0281 |
83.00 | 482.22 | 0.0282 |
84.00 | 481.45 | 0.0279 |
84.00 | 481.68 | 0.0280 |
88.00 | 453.61 | 0.0248 |
89.00 | 453.38 | 0.0247 |
89.00 | 453.87 | 0.0249 |
89.00 | 454.16 | 0.0250 |
90.00 | 454.48 | 0.0251 |
91.00 | 543.05 | 0.0361 |
91.00 | 543.18 | 0.0364 |
91.00 | 543.33 | 0.0367 |
91.00 | 543.51 | 0.0367 |
91.00 | 543.71 | 0.0367 |
120.00 | 510.63 | 0.0315 |
121.00 | 510.81 | 0.0317 |
121.00 | 511.02 | 0.0319 |
121.00 | 511.26 | 0.0319 |
124.00 | 603.12 | 0.0448 |
124.00 | 603.25 | 0.0448 |
125.00 | 603.40 | 0.0450 |
125.00 | 603.55 | 0.0448 |
125.00 | 603.73 | 0.0447 |
131.00 | 481.93 | 0.0283 |
131.00 | 482.21 | 0.0283 |
131.00 | 573.95 | 0.0403 |
132.00 | 481.23 | 0.0280 |
132.00 | 481.43 | 0.0282 |
132.00 | 481.66 | 0.0283 |
132.00 | 573.62 | 0.0403 |
132.00 | 573.78 | 0.0403 |
150.00 | 453.32 | 0.0246 |
150.00 | 453.55 | 0.0248 |
151.00 | 453.82 | 0.0249 |
151.00 | 603.10 | 0.0461 |
151.00 | 603.16 | 0.0462 |
151.00 | 603.22 | 0.0461 |
151.00 | 603.29 | 0.0461 |
151.00 | 603.36 | 0.0459 |
152.00 | 603.43 | 0.0459 |
152.00 | 603.49 | 0.0458 |
153.00 | 454.11 | 0.0250 |
153.00 | 603.56 | 0.0461 |
154.00 | 454.43 | 0.0251 |
154.00 | 603.63 | 0.0462 |
154.00 | 603.71 | 0.0463 |
162.00 | 453.23 | 0.0249 |
163.00 | 453.47 | 0.0250 |
163.00 | 453.73 | 0.0251 |
164.00 | 454.03 | 0.0251 |
164.00 | 454.35 | 0.0252 |
191.00 | 481.24 | 0.0289 |
192.00 | 481.44 | 0.0289 |
193.00 | 481.65 | 0.0290 |
193.00 | 481.89 | 0.0290 |
193.00 | 482.17 | 0.0290 |
213.00 | 511.24 | 0.0323 |
214.00 | 510.62 | 0.0318 |
214.00 | 510.81 | 0.0319 |
214.00 | 511.02 | 0.0321 |
222.00 | 543.02 | 0.0365 |
224.00 | 543.16 | 0.0370 |
226.00 | 543.32 | 0.0371 |
227.00 | 543.49 | 0.0371 |
228.00 | 543.70 | 0.0369 |
248.00 | 481.29 | 0.0288 |
248.00 | 481.48 | 0.0288 |
249.00 | 481.69 | 0.0290 |
250.00 | 481.92 | 0.0290 |
251.00 | 482.18 | 0.0291 |
259.00 | 573.47 | 0.0405 |
260.00 | 573.61 | 0.0406 |
261.00 | 573.77 | 0.0408 |
262.00 | 573.95 | 0.0408 |
287.00 | 603.17 | 0.0467 |
289.00 | 603.28 | 0.0470 |
290.00 | 603.41 | 0.0473 |
291.00 | 603.57 | 0.0472 |
310.00 | 481.26 | 0.0290 |
310.00 | 481.45 | 0.0292 |
310.00 | 481.65 | 0.0293 |
310.00 | 481.88 | 0.0295 |
310.00 | 482.13 | 0.0296 |
312.00 | 510.40 | 0.0330 |
312.00 | 510.56 | 0.0331 |
312.00 | 510.74 | 0.0332 |
312.00 | 510.96 | 0.0332 |
312.00 | 511.19 | 0.0331 |
320.00 | 543.01 | 0.0372 |
321.00 | 543.15 | 0.0376 |
322.00 | 543.31 | 0.0376 |
322.00 | 543.49 | 0.0374 |
322.00 | 543.70 | 0.0372 |
411.00 | 573.71 | 0.0420 |
412.00 | 510.73 | 0.0337 |
412.00 | 573.43 | 0.0417 |
412.00 | 573.56 | 0.0420 |
413.00 | 510.38 | 0.0340 |
413.00 | 510.55 | 0.0339 |
413.00 | 510.93 | 0.0338 |
413.00 | 511.14 | 0.0338 |
413.00 | 573.30 | 0.0416 |
413.00 | 573.86 | 0.0420 |
428.00 | 542.99 | 0.0380 |
428.00 | 543.65 | 0.0380 |
429.00 | 543.13 | 0.0383 |
429.00 | 543.28 | 0.0385 |
429.00 | 543.46 | 0.0380 |
502.00 | 603.20 | 0.0457 |
503.00 | 603.33 | 0.0460 |
504.00 | 603.46 | 0.0464 |
504.00 | 603.61 | 0.0466 |
508.00 | 510.36 | 0.0349 |
508.00 | 510.51 | 0.0348 |
509.00 | 510.68 | 0.0348 |
510.00 | 510.86 | 0.0347 |
511.00 | 511.07 | 0.0347 |
514.00 | 542.99 | 0.0387 |
515.00 | 543.11 | 0.0389 |
516.00 | 543.24 | 0.0391 |
517.00 | 543.39 | 0.0390 |
518.00 | 543.56 | 0.0391 |
562.00 | 573.29 | 0.0427 |
562.00 | 573.41 | 0.0426 |
563.00 | 573.52 | 0.0429 |
565.00 | 573.64 | 0.0433 |
567.00 | 573.77 | 0.0437 |
656.00 | 542.99 | 0.0380 |
656.00 | 543.13 | 0.0380 |
657.00 | 543.27 | 0.0382 |
658.00 | 543.42 | 0.0385 |
659.00 | 543.58 | 0.0388 |
Reference |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.64] | kPa | [310.03; 459.04] |
The Yaw...
![]() |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.40078e+01 | |||
Coefficient B | -3.53909e+03 | |||
Coefficient C | -5.20770e+01 | |||
Temperature range, min. | 310.03 | |||
Temperature range, max. | 459.04 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 450 | ||||
Pvap | 1.33 | kPa | 310.03 | Calculated Property |
Pvap | 3.05 | kPa | 326.59 | Calculated Property |
Pvap | 6.35 | kPa | 343.14 | Calculated Property |
Pvap | 12.22 | kPa | 359.70 | Calculated Property |
Pvap | 21.99 | kPa | 376.26 | Calculated Property |
Pvap | 37.38 | kPa | 392.81 | Calculated Property |
Pvap | 60.49 | kPa | 409.37 | Calculated Property |
Pvap | 93.80 | kPa | 425.93 | Calculated Property |
Pvap | 140.14 | kPa | 442.48 | Calculated Property |
Pvap | 202.64 | kPa | 459.04 | Calculated Property |
Pvap | [8.61e-07; 2772.59] | kPa | [178.28; 639.15] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 7.62408e+01 | |||
Coefficient B | -7.87048e+03 | |||
Coefficient C | -8.90935e+00 | |||
Coefficient D | 3.80979e-06 | |||
Temperature range, min. | 178.28 | |||
Temperature range, max. | 639.15 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 200 400 600 | ||||
Pvap | 8.61e-07 | kPa | 178.28 | Calculated Property |
Pvap | 1.87e-03 | kPa | 229.49 | Calculated Property |
Pvap | 0.18 | kPa | 280.70 | Calculated Property |
Pvap | 3.42 | kPa | 331.90 | Calculated Property |
Pvap | 26.07 | kPa | 383.11 | Calculated Property |
Pvap | 112.69 | kPa | 434.32 | Calculated Property |
Pvap | 337.75 | kPa | 485.53 | Calculated Property |
Pvap | 792.32 | kPa | 536.73 | Calculated Property |
Pvap | 1571.31 | kPa | 587.94 | Calculated Property |
Pvap | 2772.59 | kPa | 639.15 | Calculated Property |
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