Property | Value | Unit | Source |
---|---|---|---|
ΔcH°liquid | [-2715.17; -2672.50] | kJ/mol | |
ΔcH°liquid | -2715.17 ± 0.69 | kJ/mol | NIST |
ΔcH°liquid | -2672.50 | kJ/mol | NIST |
ΔfG° | -347.70 | kJ/mol | Joback Calculated Property |
ΔfH°gas | [-642.40; -637.90] | kJ/mol | |
ΔfH°gas | -637.90 ± 0.80 | kJ/mol | NIST |
ΔfH°gas | -642.40 ± 2.20 | kJ/mol | NIST |
ΔfH°liquid | [-724.17; -681.50] | kJ/mol | |
ΔfH°liquid | -681.50 ± 0.80 | kJ/mol | NIST |
ΔfH°liquid | -724.17 | kJ/mol | NIST |
ΔfusH° | 12.68 | kJ/mol | Joback Calculated Property |
ΔvapH° | [39.10; 81.80] | kJ/mol | |
ΔvapH° | 43.60 | kJ/mol | NIST |
ΔvapH° | 44.40 ± 0.20 | kJ/mol | NIST |
ΔvapH° | 43.60 ± 0.20 | kJ/mol | NIST |
ΔvapH° | 43.60 ± 0.15 | kJ/mol | NIST |
ΔvapH° | 43.60 | kJ/mol | NIST |
ΔvapH° | 39.10 | kJ/mol | NIST |
ΔvapH° | Outlier 81.80 | kJ/mol | NIST |
log10WS | -0.84 | Crippen Calculated Property | |
logPoct/wat | 1.179 | Crippen Calculated Property | |
McVol | 94.620 | ml/mol | McGowan Calculated Property |
NFPA Fire | 3 | KDB | |
NFPA Safety | 1 | KDB | |
Pc | 3589.94 | kPa | Joback Calculated Property |
Inp | [747.00; 785.00] | ||
Inp | 747.00 | NIST | |
Inp | 747.00 | NIST | |
Inp | 761.00 | NIST | |
Inp | 784.00 | NIST | |
Inp | 765.00 | NIST | |
Inp | 769.00 | NIST | |
Inp | 769.00 | NIST | |
Inp | 768.00 | NIST | |
Inp | 785.00 | NIST | |
Inp | 765.00 | NIST | |
Inp | 765.00 | NIST | |
Inp | 768.00 | NIST | |
Inp | 747.00 | NIST | |
I | [1083.00; 1116.00] | ||
I | Outlier 1083.00 | NIST | |
I | Outlier 1083.00 | NIST | |
I | 1100.00 | NIST | |
I | 1101.00 | NIST | |
I | 1116.00 | NIST | |
I | 1103.00 | NIST | |
I | 1104.00 | NIST | |
I | 1099.00 | NIST | |
I | 1102.00 | NIST | |
I | 1105.00 | NIST | |
I | 1105.00 | NIST | |
I | 1100.00 | NIST | |
I | 1099.00 | NIST | |
Tboil | [399.32; 399.65] | K | |
Tboil | 399.65 | K | KDB |
Tboil | 399.32 | K | VLE of ... |
Tboil | 399.32 | K | Isobari... |
Tboil | 399.60 | K | Vapor-L... |
Tc | 578.10 | K | Measure... |
Tfus | [195.86; 230.15] | K | |
Tfus | 230.15 | K | KDB |
Tfus | 195.86 | K | Efficie... |
Tfus | 196.40 | K | Vapor P... |
Vc | 0.357 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [184.32; 231.33] | J/mol×K | [412.51; 591.12] | |
T(K) Ideal gas heat capacity (J/mol×K) 180 190 200 210 220 230 450 500 550 | ||||
Cp,gas | 184.32 | J/mol×K | 412.51 | Joback Calculated Property |
Cp,gas | 192.64 | J/mol×K | 442.28 | Joback Calculated Property |
Cp,gas | 200.78 | J/mol×K | 472.05 | Joback Calculated Property |
Cp,gas | 208.73 | J/mol×K | 501.81 | Joback Calculated Property |
Cp,gas | 216.48 | J/mol×K | 531.58 | Joback Calculated Property |
Cp,gas | 224.02 | J/mol×K | 561.35 | Joback Calculated Property |
Cp,gas | 231.33 | J/mol×K | 591.12 | Joback Calculated Property |
Cp,liquid | [182.00; 254.40] | J/mol×K | [288.15; 373.15] | |
T(K) Liquid phase heat capacity (J/mol×K) 180 200 220 240 260 300 320 340 360 | ||||
Cp,liquid | 210.20 | J/mol×K | 288.15 | Densiti... |
Cp,liquid | 219.90 | J/mol×K | 293.15 | Excess ... |
Cp,liquid | 211.49 | J/mol×K | 293.15 | Densiti... |
Cp,liquid | 210.90 | J/mol×K | 294.20 | NIST |
Cp,liquid | 210.90 | J/mol×K | 294.70 | NIST |
Cp,liquid | 182.00 | J/mol×K | 298.00 | NIST |
Cp,liquid | 221.20 | J/mol×K | 298.15 | Excess ... |
Cp,liquid | 212.46 | J/mol×K | 298.15 | Densiti... |
Cp,liquid | 222.30 | J/mol×K | 303.15 | Excess ... |
Cp,liquid | 213.83 | J/mol×K | 303.15 | Densiti... |
Cp,liquid | 214.89 | J/mol×K | 308.15 | Densiti... |
Cp,liquid | 223.40 | J/mol×K | 308.15 | Excess ... |
Cp,liquid | 215.80 | J/mol×K | 313.15 | Densiti... |
Cp,liquid | 225.30 | J/mol×K | 313.15 | Excess ... |
Cp,liquid | 226.60 | J/mol×K | 318.15 | Excess ... |
Cp,liquid | 218.55 | J/mol×K | 318.15 | Densiti... |
Cp,liquid | 220.32 | J/mol×K | 323.15 | Densiti... |
Cp,liquid | 228.40 | J/mol×K | 323.15 | Excess ... |
Cp,liquid | 230.80 | J/mol×K | 328.15 | Excess ... |
Cp,liquid | 232.00 | J/mol×K | 333.15 | Excess ... |
Cp,liquid | 234.60 | J/mol×K | 338.15 | Excess ... |
Cp,liquid | 237.60 | J/mol×K | 343.15 | Excess ... |
Cp,liquid | 240.30 | J/mol×K | 348.15 | Excess ... |
Cp,liquid | 242.50 | J/mol×K | 353.15 | Excess ... |
Cp,liquid | 245.50 | J/mol×K | 358.15 | Excess ... |
Cp,liquid | 248.90 | J/mol×K | 363.15 | Excess ... |
Cp,liquid | 251.30 | J/mol×K | 368.15 | Excess ... |
Cp,liquid | 254.40 | J/mol×K | 373.15 | Excess ... |
η | [0.0003580; 0.0008640] | Pa×s | [288.15; 363.15] | |
T(K) Dynamic viscosity (Pa×s) 4.00e-4 5.00e-4 6.00e-4 7.00e-4 8.00e-4 9.00e-4 300 320 340 360 | ||||
η | 0.0008640 | Pa×s | 288.15 | Densiti... |
η | 0.0008010 | Pa×s | 293.15 | Densiti... |
η | 0.0008030 | Pa×s | 293.15 | Densiti... |
η | 0.0008000 | Pa×s | 293.15 | Density... |
η | 0.0008000 | Pa×s | 293.15 | Densiti... |
η | 0.0008090 | Pa×s | 293.15 | Density... |
η | 0.0007460 | Pa×s | 298.15 | Density... |
η | 0.0007500 | Pa×s | 298.15 | Density... |
η | 0.0007460 | Pa×s | 298.15 | Densiti... |
η | 0.0007570 | Pa×s | 298.15 | Densiti... |
η | 0.0006950 | Pa×s | 303.15 | Density... |
η | 0.0007000 | Pa×s | 303.15 | Densiti... |
η | 0.0007020 | Pa×s | 303.15 | Density... |
η | 0.0006950 | Pa×s | 303.15 | Densiti... |
η | 0.0006580 | Pa×s | 308.15 | Density... |
η | 0.0006100 | Pa×s | 313.15 | Densiti... |
η | 0.0006180 | Pa×s | 313.15 | Density... |
η | 0.0006100 | Pa×s | 313.15 | Density... |
η | 0.0006160 | Pa×s | 313.15 | Densiti... |
η | 0.0005410 | Pa×s | 323.15 | Density... |
η | 0.0005410 | Pa×s | 323.15 | Densiti... |
η | 0.0004830 | Pa×s | 333.15 | Density... |
η | 0.0004830 | Pa×s | 333.15 | Densiti... |
η | 0.0004350 | Pa×s | 343.15 | Densiti... |
η | 0.0004350 | Pa×s | 343.15 | Density... |
η | 0.0003930 | Pa×s | 353.15 | Density... |
η | 0.0003930 | Pa×s | 353.15 | Densiti... |
η | 0.0003580 | Pa×s | 363.15 | Density... |
η | 0.0003580 | Pa×s | 363.15 | Densiti... |
ΔfusH | 9.24 | kJ/mol | 198.20 | NIST |
ΔvapH | [39.10; 44.30] | kJ/mol | [331.00; 377.50] | |
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 39 40 41 42 43 44 340 360 | ||||
ΔvapH | 44.30 | kJ/mol | 331.00 | NIST |
ΔvapH | 39.10 | kJ/mol | 338.00 | NIST |
ΔvapH | 40.90 | kJ/mol | 354.00 | NIST |
ΔvapH | 42.30 | kJ/mol | 371.00 | NIST |
ΔvapH | 39.70 | kJ/mol | 377.50 | NIST |
Pvap | [0.29; 361.00] | kPa | [273.10; 452.20] | |
T(K) Vapor pressure (kPa) 0 50 100 150 200 250 300 350 300 350 400 450 | ||||
Pvap | 0.29 | kPa | 273.10 | Vapour ... |
Pvap | 0.29 | kPa | 273.30 | Vapour ... |
Pvap | 0.30 | kPa | 274.00 | Vapour ... |
Pvap | 0.31 | kPa | 274.00 | Vapour ... |
Pvap | 0.33 | kPa | 275.00 | Vapour ... |
Pvap | 0.35 | kPa | 276.20 | Vapour ... |
Pvap | 0.36 | kPa | 276.50 | Vapour ... |
Pvap | 0.38 | kPa | 277.10 | Vapour ... |
Pvap | 0.40 | kPa | 277.96 | Low pre... |
Pvap | 0.41 | kPa | 278.10 | Vapour ... |
Pvap | 0.41 | kPa | 278.20 | Vapour ... |
Pvap | 0.52 | kPa | 282.06 | Low pre... |
Pvap | 0.56 | kPa | 282.40 | Vapour ... |
Pvap | 0.58 | kPa | 283.10 | Vapour ... |
Pvap | 0.56 | kPa | 283.30 | Vapour ... |
Pvap | 0.63 | kPa | 285.00 | Vapour ... |
Pvap | 0.67 | kPa | 286.15 | Low pre... |
Pvap | 0.78 | kPa | 286.80 | Vapour ... |
Pvap | 0.80 | kPa | 288.15 | Low pre... |
Pvap | 0.79 | kPa | 288.20 | Vapour ... |
Pvap | 0.83 | kPa | 288.30 | Vapour ... |
Pvap | 0.78 | kPa | 288.40 | Vapour ... |
Pvap | 1.02 | kPa | 291.80 | Vapour ... |
Pvap | 1.05 | kPa | 293.00 | Vapour ... |
Pvap | 1.03 | kPa | 293.10 | Vapour ... |
Pvap | 1.04 | kPa | 293.10 | Vapour ... |
Pvap | 1.04 | kPa | 293.10 | Vapour ... |
Pvap | 1.03 | kPa | 293.15 | Low pre... |
Pvap | 1.08 | kPa | 293.20 | Vapour ... |
Pvap | 1.06 | kPa | 293.30 | Vapour ... |
Pvap | 1.45 | kPa | 296.80 | Vapour ... |
Pvap | 1.49 | kPa | 298.00 | Vapour ... |
Pvap | 1.52 | kPa | 298.10 | Vapour ... |
Pvap | 1.45 | kPa | 298.10 | Vapour ... |
Pvap | 1.41 | kPa | 298.15 | Low pre... |
Pvap | 1.54 | kPa | 298.20 | Vapour ... |
Pvap | 1.91 | kPa | 301.80 | Vapour ... |
Pvap | 2.01 | kPa | 303.00 | Vapour ... |
Pvap | 2.02 | kPa | 303.10 | Vapour ... |
Pvap | 2.06 | kPa | 303.10 | Vapour ... |
Pvap | 1.84 | kPa | 303.15 | Low pre... |
Pvap | 1.99 | kPa | 303.15 | Measure... |
Pvap | 1.95 | kPa | 303.15 | Measure... |
Pvap | 1.99 | kPa | 303.30 | Vapour ... |
Pvap | 2.35 | kPa | 306.64 | Low pre... |
Pvap | 2.45 | kPa | 306.80 | Vapour ... |
Pvap | 2.69 | kPa | 307.80 | Vapour ... |
Pvap | 2.65 | kPa | 308.15 | Measure... |
Pvap | 2.61 | kPa | 308.15 | Measure... |
Pvap | 2.69 | kPa | 308.20 | Vapour ... |
Pvap | 2.64 | kPa | 308.20 | Vapour ... |
Pvap | 2.67 | kPa | 308.20 | Vapour ... |
Pvap | 3.01 | kPa | 310.74 | Low pre... |
Pvap | 3.07 | kPa | 310.90 | Vapour ... |
Pvap | 3.45 | kPa | 313.15 | Measure... |
Pvap | 3.43 | kPa | 313.15 | Measure... |
Pvap | 3.65 | kPa | 313.30 | Vapour ... |
Pvap | 3.96 | kPa | 315.00 | Vapour ... |
Pvap | 3.95 | kPa | 315.20 | Vapour ... |
Pvap | 4.58 | kPa | 318.15 | Low pre... |
Pvap | 4.51 | kPa | 318.15 | Measure... |
Pvap | 4.46 | kPa | 318.15 | Measure... |
Pvap | 5.83 | kPa | 323.15 | Measure... |
Pvap | 5.75 | kPa | 323.15 | Measure... |
Pvap | 6.17 | kPa | 323.15 | Low pre... |
Pvap | 7.16 | kPa | 328.15 | Low pre... |
Pvap | 9.09 | kPa | 333.15 | Low pre... |
Pvap | 11.56 | kPa | 338.15 | Low pre... |
Pvap | 13.78 | kPa | 343.15 | Low pre... |
Pvap | 13.80 | kPa | 343.77 | Density... |
Pvap | 16.09 | kPa | 348.15 | Low pre... |
Pvap | 19.30 | kPa | 351.67 | Density... |
Pvap | 20.83 | kPa | 353.15 | Low pre... |
Pvap | 20.74 | kPa | 353.15 | Isother... |
Pvap | 22.56 | kPa | 354.68 | Phase E... |
Pvap | 22.70 | kPa | 355.63 | Density... |
Pvap | 25.03 | kPa | 357.44 | Phase E... |
Pvap | 26.00 | kPa | 358.29 | Density... |
Pvap | 27.54 | kPa | 359.95 | Phase E... |
Pvap | 29.99 | kPa | 362.26 | Phase E... |
Pvap | 30.23 | kPa | 363.15 | Isother... |
Pvap | 31.30 | kPa | 363.84 | Density... |
Pvap | 32.51 | kPa | 364.46 | Phase E... |
Pvap | 35.05 | kPa | 366.57 | Phase E... |
Pvap | 35.20 | kPa | 366.98 | Density... |
Pvap | 37.52 | kPa | 368.45 | Phase E... |
Pvap | 39.10 | kPa | 369.75 | Density... |
Pvap | 40.03 | kPa | 370.28 | Phase E... |
Pvap | 42.49 | kPa | 372.04 | Phase E... |
Pvap | 42.80 | kPa | 372.28 | Density... |
Pvap | 45.10 | kPa | 373.00 | Isother... |
Pvap | 45.05 | kPa | 373.73 | Phase E... |
Pvap | 46.50 | kPa | 374.61 | Density... |
Pvap | 47.47 | kPa | 375.26 | Phase E... |
Pvap | 50.04 | kPa | 376.81 | Phase E... |
Pvap | 50.50 | kPa | 377.05 | Density... |
Pvap | 52.46 | kPa | 378.22 | Phase E... |
Pvap | 55.00 | kPa | 379.59 | Density... |
Pvap | 55.03 | kPa | 379.67 | Phase E... |
Pvap | 57.56 | kPa | 381.03 | Phase E... |
Pvap | 58.80 | kPa | 381.49 | Density... |
Pvap | 59.95 | kPa | 382.32 | Phase E... |
Pvap | 63.10 | kPa | 383.37 | Density... |
Pvap | 63.50 | kPa | 383.57 | Density... |
Pvap | 62.52 | kPa | 383.60 | Phase E... |
Pvap | 64.97 | kPa | 384.81 | Phase E... |
Pvap | 67.44 | kPa | 385.98 | Phase E... |
Pvap | 68.50 | kPa | 386.18 | Density... |
Pvap | 70.02 | kPa | 387.13 | Phase E... |
Pvap | 72.80 | kPa | 387.61 | Density... |
Pvap | 72.51 | kPa | 388.28 | Phase E... |
Pvap | 74.96 | kPa | 389.32 | Phase E... |
Pvap | 78.50 | kPa | 390.35 | Density... |
Pvap | 77.43 | kPa | 390.35 | Phase E... |
Pvap | 79.97 | kPa | 391.39 | Phase E... |
Pvap | 84.00 | kPa | 392.39 | Density... |
Pvap | 82.52 | kPa | 392.45 | Phase E... |
Pvap | 84.84 | kPa | 393.34 | Phase E... |
Pvap | 88.20 | kPa | 393.93 | Density... |
Pvap | 87.52 | kPa | 394.36 | Phase E... |
Pvap | 89.81 | kPa | 395.23 | Phase E... |
Pvap | 93.40 | kPa | 395.72 | Density... |
Pvap | 92.53 | kPa | 396.21 | Phase E... |
Pvap | 94.89 | kPa | 397.03 | Phase E... |
Pvap | 97.54 | kPa | 397.96 | Phase E... |
Pvap | 101.50 | kPa | 398.28 | Density... |
Pvap | 100.03 | kPa | 398.81 | Phase E... |
Pvap | 101.38 | kPa | 399.27 | Phase E... |
Pvap | 101.30 | kPa | 399.60 | Vapor-L... |
Pvap | 143.00 | kPa | 412.50 | Isother... |
Pvap | 361.00 | kPa | 452.20 | Isother... |
n0 | [1.38210; 1.38450] | [293.15; 298.15] | ||
T(K) Refractive Index 1.38 1.38 1.38 1.38 1.38 1.38 294 296 298 | ||||
n0 | 1.38300 | 293.15 | Vapor l... | |
n0 | 1.38450 | 293.15 | Densiti... | |
n0 | 1.38450 | 293.15 | Densiti... | |
n0 | 1.38280 | 298.15 | Propert... | |
n0 | 1.38210 | 298.15 | Isobari... | |
n0 | 1.38300 | 298.15 | Viscosi... | |
ρl | [935.08; 980.49] | kg/m3 | [288.15; 328.15] | |
T(K) Liquid Density (kg/m3) 940 950 960 970 980 290 300 310 320 | ||||
ρl | 980.29 | kg/m3 | 288.15 | Permitt... |
ρl | 980.49 | kg/m3 | 288.15 | Excess ... |
ρl | 974.91 | kg/m3 | 293.15 | Excess ... |
ρl | 974.57 | kg/m3 | 293.15 | Permitt... |
ρl | 974.90 | kg/m3 | 293.15 | Density... |
ρl | 969.32 | kg/m3 | 298.15 | Influen... |
ρl | 969.12 | kg/m3 | 298.15 | Densiti... |
ρl | 969.23 | kg/m3 | 298.15 | Excess ... |
ρl | 970.00 | kg/m3 | 298.15 | Low pre... |
ρl | 969.10 | kg/m3 | 298.15 | Thermop... |
ρl | 969.10 | kg/m3 | 298.15 | Dynamic... |
ρl | 969.10 | kg/m3 | 298.15 | Viscosi... |
ρl | 967.83 | kg/m3 | 298.15 | Isobari... |
ρl | 969.30 | kg/m3 | 298.15 | Excess ... |
ρl | 969.18 | kg/m3 | 298.15 | Solid-l... |
ρl | 969.00 | kg/m3 | 298.15 | Isobari... |
ρl | 969.30 | kg/m3 | 298.15 | Density... |
ρl | 969.07 | kg/m3 | 298.15 | Permitt... |
ρl | 969.08 | kg/m3 | 298.15 | Evaluat... |
ρl | 963.70 | kg/m3 | 303.15 | Density... |
ρl | 963.66 | kg/m3 | 303.15 | Excess ... |
ρl | 963.60 | kg/m3 | 303.15 | Permitt... |
ρl | 963.50 | kg/m3 | 303.15 | Thermop... |
ρl | 958.00 | kg/m3 | 308.15 | Density... |
ρl | 958.00 | kg/m3 | 308.15 | Excess ... |
ρl | 957.80 | kg/m3 | 308.15 | Thermop... |
ρl | 957.90 | kg/m3 | 308.15 | Excess ... |
ρl | 957.98 | kg/m3 | 308.15 | Permitt... |
ρl | 952.43 | kg/m3 | 313.15 | Densiti... |
ρl | 952.40 | kg/m3 | 313.15 | Density... |
ρl | 952.10 | kg/m3 | 313.15 | Thermop... |
ρl | 952.32 | kg/m3 | 313.15 | Excess ... |
ρl | 952.15 | kg/m3 | 313.15 | Densiti... |
ρl | 946.70 | kg/m3 | 318.15 | Density... |
ρl | 947.67 | kg/m3 | 318.15 | Permitt... |
ρl | 946.40 | kg/m3 | 318.15 | Thermop... |
ρl | 946.60 | kg/m3 | 318.15 | Excess ... |
ρl | 940.86 | kg/m3 | 323.15 | Excess ... |
ρl | 940.70 | kg/m3 | 323.15 | Thermop... |
ρl | 940.90 | kg/m3 | 323.15 | Density... |
ρl | 935.08 | kg/m3 | 328.15 | Excess ... |
ρl | 935.12 | kg/m3 | 328.15 | Permitt... |
ρl | 935.20 | kg/m3 | 328.15 | Density... |
csound,fluid | 1178.00 | m/s | 298.15 | Vapor l... |
γ | [0.02; 0.03] | N/m | [273.18; 373.17] | |
T(K) Surface Tension (N/m) 0.02 0.02 0.02 0.02 0.03 0.03 0.03 300 350 | ||||
γ | 0.03 | N/m | 273.18 | Surface... |
γ | 0.03 | N/m | 278.18 | Surface... |
γ | 0.03 | N/m | 283.18 | Surface... |
γ | 0.03 | N/m | 288.18 | Surface... |
γ | 0.03 | N/m | 293.16 | Surface... |
γ | 0.03 | N/m | 298.10 | Surface... |
γ | 0.03 | N/m | 298.15 | Surface... |
γ | 0.03 | N/m | 303.17 | Surface... |
γ | 0.03 | N/m | 308.11 | Surface... |
γ | 0.02 | N/m | 308.15 | Surface... |
γ | 0.02 | N/m | 313.19 | Surface... |
γ | 0.02 | N/m | 318.16 | Surface... |
γ | 0.02 | N/m | 323.16 | Surface... |
γ | 0.02 | N/m | 328.12 | Surface... |
γ | 0.02 | N/m | 333.18 | Surface... |
γ | 0.02 | N/m | 338.17 | Surface... |
γ | 0.02 | N/m | 343.17 | Surface... |
γ | 0.02 | N/m | 348.17 | Surface... |
γ | 0.02 | N/m | 353.19 | Surface... |
γ | 0.02 | N/m | 358.18 | Surface... |
γ | 0.02 | N/m | 363.16 | Surface... |
γ | 0.02 | N/m | 368.18 | Surface... |
γ | 0.02 | N/m | 373.17 | Surface... |
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
288.15 | 100.00 | 980.3 |
288.15 | 5000.00 | 984.5 |
288.15 | 10000.00 | 988.6 |
288.15 | 20000.00 | 996.3 |
288.15 | 30000.00 | 1003.6 |
288.15 | 40000.00 | 1010.5 |
298.15 | 100.00 | 968.9 |
298.15 | 5000.00 | 973.8 |
298.15 | 10000.00 | 977.8 |
298.15 | 20000.00 | 986.0 |
298.15 | 30000.00 | 993.6 |
298.15 | 40000.00 | 1000.8 |
308.15 | 100.00 | 957.7 |
308.15 | 5000.00 | 962.4 |
308.15 | 10000.00 | 967.1 |
308.15 | 20000.00 | 975.7 |
308.15 | 30000.00 | 983.8 |
308.15 | 40000.00 | 991.3 |
Reference |
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
298.15 | 100.00 | 969.3 |
Reference |
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
298.15 | 100.00 | 969.4 |
Reference |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [3.67e-03; 3396.12] | kPa | [230.15; 576.00] | KDB Vap... |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 1.76598e+02 | |||
Coefficient B | -1.16692e+04 | |||
Coefficient C | -2.43764e+01 | |||
Coefficient D | 2.02849e-05 | |||
Temperature range, min. | 230.15 | |||
Temperature range, max. | 576.00 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 300 400 500 | ||||
Pvap | 3.67e-03 | kPa | 230.15 | Calculated Property |
Pvap | 0.18 | kPa | 268.58 | Calculated Property |
Pvap | 2.46 | kPa | 307.01 | Calculated Property |
Pvap | 15.84 | kPa | 345.43 | Calculated Property |
Pvap | 62.89 | kPa | 383.86 | Calculated Property |
Pvap | 183.16 | kPa | 422.29 | Calculated Property |
Pvap | 437.25 | kPa | 460.72 | Calculated Property |
Pvap | 921.36 | kPa | 499.14 | Calculated Property |
Pvap | 1803.01 | kPa | 537.57 | Calculated Property |
Pvap | 3396.12 | kPa | 576.00 | Calculated Property |
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