Property | Value | Unit | Source |
---|---|---|---|
ΔcH°liquid | -2534.80 ± 1.90 | kJ/mol | NIST |
ΔfG° | -41.06 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -183.40 ± 1.90 | kJ/mol | NIST |
ΔfH°liquid | [-229.80; -229.50] | kJ/mol |
![]() |
ΔfH°liquid | -229.80 ± 1.90 | kJ/mol | NIST |
ΔfH°liquid | -229.50 | kJ/mol | NIST |
ΔfusH° | 14.51 | kJ/mol | Joback Calculated Property |
ΔvapH° | 33.27 | kJ/mol | Joback Calculated Property |
IE | 11.03 | eV | NIST |
log10WS | -1.80 | Crippen Calculated Property | |
logPoct/wat | 2.244 | Crippen Calculated Property | |
McVol | 91.700 | ml/mol | McGowan Calculated Property |
Pc | 3560.02 | kPa | Joback Calculated Property |
Inp | [867.40; 898.10] |
![]() |
|
Inp | 867.40 | NIST | |
Inp | 895.00 | NIST | |
Inp | 874.00 | NIST | |
Inp | 874.00 | NIST | |
Inp | 874.00 | NIST | |
Inp | 874.00 | NIST | |
Inp | 898.10 | NIST | |
Inp | 894.10 | NIST | |
Tboil | 428.15 | K | KDB |
Tc | 547.67 | K | Joback Calculated Property |
Tfus | 234.50 ± 0.40 | K | NIST |
Vc | 0.357 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [141.67; 181.25] | J/mol×K | [365.78; 547.67] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 140 150 160 170 180 400 450 500 550 | ||||
Cp,gas | 141.67 | J/mol×K | 365.78 | Joback Calculated Property |
Cp,gas | 149.02 | J/mol×K | 396.09 | Joback Calculated Property |
Cp,gas | 156.05 | J/mol×K | 426.41 | Joback Calculated Property |
Cp,gas | 162.78 | J/mol×K | 456.72 | Joback Calculated Property |
Cp,gas | 169.22 | J/mol×K | 487.04 | Joback Calculated Property |
Cp,gas | 175.37 | J/mol×K | 517.35 | Joback Calculated Property |
Cp,gas | 181.25 | J/mol×K | 547.67 | Joback Calculated Property |
Cp,liquid | [183.59; 184.00] | J/mol×K | [298.15; 298.15] | ![]() |
Cp,liquid | 184.00 | J/mol×K | 298.15 | NIST |
Cp,liquid | 183.59 | J/mol×K | 298.15 | NIST |
η | [0.0003469; 0.0041179] | Pa×s | [194.68; 365.78] | ![]() |
T(K) Dynamic viscosity (Pa×s) 0 5.00e-4 1.00e-3 1.50e-3 2.00e-3 2.50e-3 3.00e-3 3.50e-3 4.00e-3 200 250 300 350 | ||||
η | 0.0041179 | Pa×s | 194.68 | Joback Calculated Property |
η | 0.0020950 | Pa×s | 223.20 | Joback Calculated Property |
η | 0.0012422 | Pa×s | 251.71 | Joback Calculated Property |
η | 0.0008192 | Pa×s | 280.23 | Joback Calculated Property |
η | 0.0005835 | Pa×s | 308.75 | Joback Calculated Property |
η | 0.0004401 | Pa×s | 337.26 | Joback Calculated Property |
η | 0.0003469 | Pa×s | 365.78 | Joback Calculated Property |
ΔvapH | 43.40 | kJ/mol | 380.50 | NIST |
Pvap | [2.21; 2.21] | kPa | [323.15; 323.15] | ![]() |
Pvap | 2.21 | kPa | 323.15 | Excess ... |
Pvap | 2.21 | kPa | 323.15 | Excess ... |
n0 | [1.45190; 1.45220] | [298.15; 298.15] | ![]() |
|
n0 | 1.45200 | 298.15 | Thermod... | |
n0 | 1.45190 | 298.15 | Isother... | |
n0 | 1.45220 | 298.15 | Isother... | |
ρl | [1110.54; 1143.49] | kg/m3 | [288.15; 318.15] | ![]() |
T(K) Liquid Density (kg/m3) 1110 1115 1120 1125 1130 1135 1140 1145 290 300 310 | ||||
ρl | 1143.43 | kg/m3 | 288.15 | Densiti... |
ρl | 1143.49 | kg/m3 | 288.15 | Densiti... |
ρl | 1135.00 | kg/m3 | 298.15 | Volumet... |
ρl | 1133.94 | kg/m3 | 298.15 | Volumet... |
ρl | 1132.50 | kg/m3 | 298.15 | Densiti... |
ρl | 1132.57 | kg/m3 | 298.15 | Densiti... |
ρl | 1121.61 | kg/m3 | 308.15 | Densiti... |
ρl | 1123.00 | kg/m3 | 308.15 | Volumet... |
ρl | 1121.54 | kg/m3 | 308.15 | Densiti... |
ρl | 1110.61 | kg/m3 | 318.15 | Densiti... |
ρl | 1112.00 | kg/m3 | 318.15 | Volumet... |
ρl | 1110.54 | kg/m3 | 318.15 | Densiti... |
csound,fluid | [1215.66; 1286.64] | m/s | [298.15; 318.15] | ![]() |
csound,fluid | 1286.64 | m/s | 298.15 | Speeds ... |
csound,fluid | 1251.00 | m/s | 308.15 | Speeds ... |
csound,fluid | 1215.66 | m/s | 318.15 | Speeds ... |
γ | [0.03; 0.03] | N/m | [293.15; 313.15] | ![]() |
T(K) Surface Tension (N/m) 0.03 0.03 0.03 0.03 0.03 295 300 305 310 | ||||
γ | 0.03 | N/m | 293.15 | The add... |
γ | 0.03 | N/m | 298.15 | The add... |
γ | 0.03 | N/m | 303.15 | The add... |
γ | 0.03 | N/m | 308.15 | The add... |
γ | 0.03 | N/m | 313.15 | The add... |
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
288.15 | 100.00 | 1143.7 |
288.15 | 500.00 | 1144.1 |
288.15 | 1000.00 | 1144.5 |
288.15 | 1500.00 | 1144.8 |
288.15 | 2000.00 | 1145.2 |
288.15 | 2500.00 | 1145.5 |
288.15 | 3000.00 | 1145.9 |
288.15 | 3600.00 | 1146.4 |
288.15 | 4100.00 | 1146.7 |
288.15 | 4600.00 | 1147.0 |
288.15 | 5100.00 | 1147.4 |
288.15 | 5600.00 | 1147.7 |
288.15 | 6100.00 | 1148.1 |
288.15 | 6600.00 | 1148.5 |
288.15 | 7100.00 | 1148.9 |
288.15 | 7600.00 | 1149.2 |
288.15 | 8100.00 | 1149.5 |
288.15 | 8600.00 | 1149.9 |
288.15 | 9200.00 | 1150.3 |
288.15 | 9600.00 | 1150.7 |
288.15 | 10100.00 | 1151.0 |
288.15 | 10600.00 | 1151.3 |
288.15 | 11100.00 | 1151.7 |
288.15 | 11600.00 | 1152.0 |
288.15 | 12100.00 | 1152.4 |
288.15 | 12600.00 | 1152.7 |
288.15 | 13100.00 | 1153.1 |
288.15 | 13500.00 | 1153.3 |
288.15 | 14200.00 | 1153.8 |
288.15 | 14700.00 | 1154.1 |
288.15 | 15200.00 | 1154.4 |
288.15 | 15700.00 | 1154.8 |
288.15 | 16300.00 | 1155.2 |
288.15 | 16800.00 | 1155.6 |
288.15 | 17300.00 | 1155.9 |
288.15 | 17800.00 | 1156.2 |
288.15 | 18300.00 | 1156.5 |
288.15 | 18800.00 | 1156.8 |
288.15 | 19100.00 | 1157.1 |
288.15 | 19700.00 | 1157.4 |
288.15 | 20200.00 | 1157.8 |
298.15 | 100.00 | 1133.7 |
298.15 | 500.00 | 1134.0 |
298.15 | 1000.00 | 1134.4 |
298.15 | 1500.00 | 1134.8 |
298.15 | 2000.00 | 1135.2 |
298.15 | 2500.00 | 1135.6 |
298.15 | 3100.00 | 1136.1 |
298.15 | 3600.00 | 1136.4 |
298.15 | 4100.00 | 1136.8 |
298.15 | 4600.00 | 1137.2 |
298.15 | 5100.00 | 1137.6 |
298.15 | 5600.00 | 1137.9 |
298.15 | 6100.00 | 1138.4 |
298.15 | 6600.00 | 1138.7 |
298.15 | 7100.00 | 1139.1 |
298.15 | 7600.00 | 1139.4 |
298.15 | 8100.00 | 1139.8 |
298.15 | 8600.00 | 1140.2 |
298.15 | 9200.00 | 1140.6 |
298.15 | 9600.00 | 1141.0 |
298.15 | 10100.00 | 1141.4 |
298.15 | 10700.00 | 1141.8 |
298.15 | 11100.00 | 1142.1 |
298.15 | 11600.00 | 1142.4 |
298.15 | 12100.00 | 1142.8 |
298.15 | 12600.00 | 1143.2 |
298.15 | 13100.00 | 1143.6 |
298.15 | 13600.00 | 1143.9 |
298.15 | 14100.00 | 1144.2 |
298.15 | 14700.00 | 1144.6 |
298.15 | 15200.00 | 1145.0 |
298.15 | 15700.00 | 1145.4 |
298.15 | 16200.00 | 1145.8 |
298.15 | 16700.00 | 1146.1 |
298.15 | 17200.00 | 1146.5 |
298.15 | 17800.00 | 1146.9 |
298.15 | 18300.00 | 1147.2 |
298.15 | 18800.00 | 1147.6 |
298.15 | 19200.00 | 1147.9 |
298.15 | 19700.00 | 1148.2 |
298.15 | 20200.00 | 1148.7 |
308.15 | 100.00 | 1122.3 |
308.15 | 500.00 | 1122.7 |
308.15 | 1000.00 | 1123.1 |
308.15 | 1500.00 | 1123.5 |
308.15 | 2000.00 | 1123.9 |
308.15 | 2500.00 | 1124.3 |
308.15 | 3100.00 | 1124.8 |
308.15 | 3600.00 | 1125.2 |
308.15 | 4100.00 | 1125.6 |
308.15 | 4600.00 | 1126.0 |
308.15 | 5100.00 | 1126.4 |
308.15 | 5600.00 | 1126.9 |
308.15 | 6100.00 | 1127.2 |
308.15 | 6600.00 | 1127.5 |
308.15 | 7100.00 | 1128.0 |
308.15 | 7600.00 | 1128.4 |
308.15 | 8100.00 | 1128.8 |
308.15 | 8600.00 | 1129.2 |
308.15 | 9200.00 | 1129.6 |
308.15 | 9600.00 | 1130.0 |
308.15 | 10100.00 | 1130.4 |
308.15 | 10600.00 | 1130.9 |
308.15 | 11100.00 | 1131.2 |
308.15 | 11600.00 | 1131.5 |
308.15 | 12100.00 | 1131.9 |
308.15 | 12600.00 | 1132.4 |
308.15 | 13100.00 | 1132.6 |
308.15 | 13600.00 | 1133.1 |
308.15 | 14100.00 | 1133.5 |
308.15 | 14700.00 | 1133.9 |
308.15 | 15100.00 | 1134.2 |
308.15 | 15700.00 | 1134.6 |
308.15 | 16200.00 | 1135.0 |
308.15 | 16700.00 | 1135.3 |
308.15 | 17200.00 | 1135.7 |
308.15 | 17800.00 | 1136.1 |
308.15 | 18300.00 | 1136.5 |
308.15 | 18800.00 | 1136.8 |
308.15 | 19200.00 | 1137.2 |
308.15 | 19700.00 | 1137.6 |
308.15 | 20200.00 | 1138.0 |
318.15 | 100.00 | 1112.0 |
318.15 | 500.00 | 1112.4 |
318.15 | 1000.00 | 1112.8 |
318.15 | 1500.00 | 1113.2 |
318.15 | 2000.00 | 1113.7 |
318.15 | 2500.00 | 1114.1 |
318.15 | 3100.00 | 1114.7 |
318.15 | 3500.00 | 1115.0 |
318.15 | 4100.00 | 1115.5 |
318.15 | 4600.00 | 1115.9 |
318.15 | 5100.00 | 1116.3 |
318.15 | 5600.00 | 1116.8 |
318.15 | 6100.00 | 1117.3 |
318.15 | 6600.00 | 1117.7 |
318.15 | 7100.00 | 1118.1 |
318.15 | 7600.00 | 1118.4 |
318.15 | 8100.00 | 1118.9 |
318.15 | 8600.00 | 1119.3 |
318.15 | 9200.00 | 1119.8 |
318.15 | 9600.00 | 1120.2 |
318.15 | 10100.00 | 1120.6 |
318.15 | 10600.00 | 1121.0 |
318.15 | 11100.00 | 1121.4 |
318.15 | 11600.00 | 1121.8 |
318.15 | 12100.00 | 1122.1 |
318.15 | 12600.00 | 1122.6 |
318.15 | 13000.00 | 1123.0 |
318.15 | 13600.00 | 1123.3 |
318.15 | 14200.00 | 1123.9 |
318.15 | 14700.00 | 1124.4 |
318.15 | 15200.00 | 1124.7 |
318.15 | 15700.00 | 1125.1 |
318.15 | 16300.00 | 1125.4 |
318.15 | 16800.00 | 1126.0 |
318.15 | 17300.00 | 1126.3 |
318.15 | 17800.00 | 1126.5 |
318.15 | 18300.00 | 1127.0 |
318.15 | 18800.00 | 1127.4 |
318.15 | 19200.00 | 1127.7 |
318.15 | 19700.00 | 1128.0 |
318.15 | 20200.00 | 1128.4 |
Reference |
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
298.15 | 100.00 | 1133.7 |
Reference |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.65] | kPa | [312.79; 432.68] |
The Yaw...
![]() |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.62874e+01 | |||
Coefficient B | -4.19096e+03 | |||
Coefficient C | -5.08480e+01 | |||
Temperature range, min. | 312.79 | |||
Temperature range, max. | 432.68 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 | ||||
Pvap | 1.33 | kPa | 312.79 | Calculated Property |
Pvap | 2.89 | kPa | 326.11 | Calculated Property |
Pvap | 5.84 | kPa | 339.43 | Calculated Property |
Pvap | 11.09 | kPa | 352.75 | Calculated Property |
Pvap | 19.93 | kPa | 366.07 | Calculated Property |
Pvap | 34.17 | kPa | 379.40 | Calculated Property |
Pvap | 56.17 | kPa | 392.72 | Calculated Property |
Pvap | 88.96 | kPa | 406.04 | Calculated Property |
Pvap | 136.28 | kPa | 419.36 | Calculated Property |
Pvap | 202.65 | kPa | 432.68 | Calculated Property |
Pvap | [3.53e-03; 3577.43] | kPa | [235.85; 641.00] |
KDB Vap...
![]() |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 7.77758e+01 | |||
Coefficient B | -7.95407e+03 | |||
Coefficient C | -9.14431e+00 | |||
Coefficient D | 4.66169e-06 | |||
Temperature range, min. | 235.85 | |||
Temperature range, max. | 641.00 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 300 400 500 600 | ||||
Pvap | 3.53e-03 | kPa | 235.85 | Calculated Property |
Pvap | 0.18 | kPa | 280.87 | Calculated Property |
Pvap | 2.58 | kPa | 325.88 | Calculated Property |
Pvap | 17.72 | kPa | 370.90 | Calculated Property |
Pvap | 74.69 | kPa | 415.92 | Calculated Property |
Pvap | 227.10 | kPa | 460.93 | Calculated Property |
Pvap | 550.91 | kPa | 505.95 | Calculated Property |
Pvap | 1139.60 | kPa | 550.97 | Calculated Property |
Pvap | 2103.57 | kPa | 595.98 | Calculated Property |
Pvap | 3577.43 | kPa | 641.00 | Calculated Property |
Find more compounds similar to Butane, 1,4-dichloro-.
Find more mixtures with Butane, 1,4-dichloro-.
Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more. Take the time to validate and double check the source of the data.