- InChI
- InChI=1S/C6H5Br/c7-6-4-2-1-3-5-6/h1-5H
- InChI Key
- QARVLSVVCXYDNA-UHFFFAOYSA-N
- Formula
- C6H5Br
- SMILES
- Brc1ccccc1
- Molecular Weight1
- 157.01
- CAS
- 108-86-1
- Other Names
-
- 1-Bromobenzene
- Bromobenzene
- MONOBROMOBENZENE
- NCI-C55492
- PHENYL BROMIDE
- UN 2514
- ω : Acentric Factor.
- PAff : Proton affinity (kJ/mol).
- Tig : Autoignition Temperature (K).
- BasG : Gas basicity (kJ/mol).
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- μ : Dipole Moment (debye).
- η : Dynamic viscosity (Pa×s).
- Tflash,oc : Flash Point (Open Cup Method) (K).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfH°liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔfusH : Enthalpy of fusion at a given temperature (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- IE : Ionization energy (eV).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- NFPA Fire : NFPA Fire Rating.
- NFPA Health : NFPA Health Rating.
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- S°liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tboil : Boiling point at given pressure (K).
- Tboilr : Boiling point at reduced pressure (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Tfus : Melting point (K).
- Ttriple : Triple Point Temperature (K).
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- Zra : Rackett Parameter.
- 1: Molecular weight from the IUPAC atomic weights tables.
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry.
Do not hesitate to contact us for your projects.
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.2510 | KDB | |
| PAff | 754.10 | kJ/mol | NIST |
| Tig | 838.15 | K | KDB |
| BasG | 725.80 | kJ/mol | NIST |
| ΔcH°liquid | -3111.90 ± 0.67 | kJ/mol | NIST |
| μ | 1.50 | debye | KDB |
| Tflash,oc | 324.26 | K | KDB |
| ΔfG° | 138.60 | kJ/mol | KDB |
| ΔfH°gas | 105.10 | kJ/mol | KDB |
| ΔfH°liquid | [58.60; 60.90] | kJ/mol |
|
| ΔfH°liquid | 58.60 | kJ/mol | NIST |
| ΔfH°liquid | 60.90 ± 4.10 | kJ/mol | NIST |
| ΔfusH° | 10.62 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [37.90; 44.80] | kJ/mol |
|
| ΔvapH° | 44.54 | kJ/mol | NIST |
| ΔvapH° | 44.80 | kJ/mol | NIST |
| ΔvapH° | 44.50 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 44.54 ± 0.04 | kJ/mol | NIST |
| ΔvapH° | 37.90 ± 0.03 | kJ/mol | NIST |
| IE | [8.95; 9.45] | eV |
|
| IE | 9.00 ± 0.03 | eV | NIST |
| IE | 9.00 | eV | NIST |
| IE | 9.00 | eV | NIST |
| IE | 9.02 | eV | NIST |
| IE | 9.05 ± 0.02 | eV | NIST |
| IE | 8.98 ± 0.02 | eV | NIST |
| IE | 8.98 | eV | NIST |
| IE | Outlier 9.45 | eV | NIST |
| IE | 8.97 ± 0.02 | eV | NIST |
| IE | 8.99 | eV | NIST |
| IE | 9.03 ± 0.01 | eV | NIST |
| IE | 8.98 ± 0.03 | eV | NIST |
| IE | 8.95 | eV | NIST |
| IE | 8.98 ± 0.02 | eV | NIST |
| IE | 8.99 | eV | NIST |
| IE | 9.04 | eV | NIST |
| IE | 9.05 | eV | NIST |
| IE | 8.99 ± 0.03 | eV | NIST |
| IE | 9.00 | eV | NIST |
| log10WS | [-2.55; -2.55] |
|
|
| log10WS | -2.55 | Aq. Solubility Prediction | |
| log10WS | -2.55 | Estimated Solubility | |
| logPoct/wat | 2.449 | Crippen Calculated Property | |
| McVol | 89.140 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 2 | KDB | |
| NFPA Health | 2 | KDB | |
| Pc | 4520.00 | kPa | KDB |
| Inp | [150.00; 983.00] |
|
|
| Inp | 960.00 | NIST | |
| Inp | 952.20 | NIST | |
| Inp | 931.71 | NIST | |
| Inp | 941.36 | NIST | |
| Inp | 924.00 | NIST | |
| Inp | 932.00 | NIST | |
| Inp | 914.70 | NIST | |
| Inp | 923.70 | NIST | |
| Inp | 934.80 | NIST | |
| Inp | 959.60 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 974.00 | NIST | |
| Inp | 974.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 945.00 | NIST | |
| Inp | 925.80 | NIST | |
| Inp | 965.00 | NIST | |
| Inp | 982.00 | NIST | |
| Inp | 979.60 | NIST | |
| Inp | 941.00 | NIST | |
| Inp | 903.90 | NIST | |
| Inp | 926.00 | NIST | |
| Inp | 909.50 | NIST | |
| Inp | 919.67 | NIST | |
| Inp | 921.35 | NIST | |
| Inp | 926.64 | NIST | |
| Inp | 927.00 | NIST | |
| Inp | 927.00 | NIST | |
| Inp | 918.00 | NIST | |
| Inp | 915.00 | NIST | |
| Inp | 930.00 | NIST | |
| Inp | 921.00 | NIST | |
| Inp | 935.00 | NIST | |
| Inp | 982.00 | NIST | |
| Inp | 936.00 | NIST | |
| Inp | 895.00 | NIST | |
| Inp | 983.00 | NIST | |
| Inp | 910.00 | NIST | |
| Inp | 936.00 | NIST | |
| Inp | 945.00 | NIST | |
| Inp | 930.00 | NIST | |
| Inp | 945.00 | NIST | |
| Inp | Outlier 150.00 | NIST | |
| I | [1330.00; 1391.00] |
|
|
| I | 1351.00 | NIST | |
| I | 1338.00 | NIST | |
| I | 1330.00 | NIST | |
| I | 1381.03 | NIST | |
| I | 1373.68 | NIST | |
| I | 1358.59 | NIST | |
| I | 1348.92 | NIST | |
| I | 1391.00 | NIST | |
| I | 1338.00 | NIST | |
| I | 1365.00 | NIST | |
| S°liquid | [207.90; 21922.00] | J/mol×K |
|
| S°liquid | 21922.00 | J/mol×K | NIST |
| S°liquid | 207.90 | J/mol×K | NIST |
| Tboil | 429.21 | K | KDB |
| Tc | 670.00 | K | KDB |
| Tfus | [242.25; 242.50] | K |
|
| Tfus | 242.50 | K | KDB |
| Tfus | 242.25 | K | Aq. Solubility Prediction |
| Ttriple | [242.40; 242.42] | K |
|
| Ttriple | 242.40 | K | KDB |
| Ttriple | 242.42 ± 0.02 | K | NIST |
| Ttriple | 242.40 ± 0.01 | K | NIST |
| Ttriple | 242.40 ± 0.20 | K | NIST |
| Vc | 0.324 | m3/kmol | KDB |
| Zc | 0.2628890 | KDB | |
| Zra | 0.26 | KDB |
Temperature Dependent Properties
Pressure Dependent Properties
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 248.15 | 99.70 | 1554.489 |
| 248.15 | 1231.41 | 1555.368 |
| 248.15 | 2075.45 | 1556.036 |
| 248.15 | 4196.22 | 1557.697 |
| 248.15 | 5950.98 | 1559.054 |
| 248.15 | 8068.32 | 1560.666 |
| 248.15 | 10015.40 | 1562.113 |
| 248.15 | 11951.60 | 1563.577 |
| 248.15 | 13994.80 | 1565.093 |
| 248.15 | 15940.30 | 1566.527 |
| 248.15 | 18145.00 | 1568.122 |
| 248.15 | 19946.50 | 1569.417 |
| 248.15 | 21965.00 | 1570.861 |
| 248.15 | 24135.90 | 1572.41 |
| 248.15 | 25864.70 | 1573.623 |
| 248.15 | 27917.30 | 1575.05 |
| 248.15 | 29850.30 | 1576.387 |
| 273.15 | 100.51 | 1520.557 |
| 273.15 | 1116.26 | 1521.447 |
| 273.15 | 2128.10 | 1522.34 |
| 273.15 | 4045.82 | 1524.026 |
| 273.15 | 5967.30 | 1525.66 |
| 273.15 | 8142.83 | 1527.515 |
| 273.15 | 10020.30 | 1529.109 |
| 273.15 | 11896.10 | 1530.677 |
| 273.15 | 13922.00 | 1532.353 |
| 273.15 | 16083.00 | 1534.134 |
| 273.15 | 18195.20 | 1535.834 |
| 273.15 | 20035.10 | 1537.31 |
| 273.15 | 21829.30 | 1538.747 |
| 273.15 | 23856.50 | 1540.342 |
| 273.15 | 25976.20 | 1542.017 |
| 273.15 | 28097.70 | 1543.651 |
| 273.15 | 29947.00 | 1545.093 |
| 293.15 | 101.93 | 1493.557 |
| 293.15 | 1239.69 | 1494.684 |
| 293.15 | 2010.73 | 1495.408 |
| 293.15 | 4059.70 | 1497.371 |
| 293.15 | 6007.85 | 1499.218 |
| 293.15 | 8079.77 | 1501.16 |
| 293.15 | 10000.80 | 1502.944 |
| 293.15 | 11960.00 | 1504.732 |
| 293.15 | 14168.60 | 1506.732 |
| 293.15 | 15878.80 | 1508.265 |
| 293.15 | 17960.30 | 1510.109 |
| 293.15 | 19999.40 | 1511.901 |
| 293.15 | 21880.00 | 1513.531 |
| 293.15 | 24122.20 | 1515.458 |
| 293.15 | 26141.00 | 1517.174 |
| 293.15 | 28060.50 | 1518.79 |
| 293.15 | 29992.70 | 1520.418 |
| 313.15 | 102.54 | 1466.553 |
| 313.15 | 2000.76 | 1468.587 |
| 313.15 | 4010.97 | 1470.712 |
| 313.15 | 6189.56 | 1473.0 |
| 313.15 | 7991.64 | 1474.858 |
| 313.15 | 10089.40 | 1477.007 |
| 313.15 | 12142.80 | 1479.063 |
| 313.15 | 14014.60 | 1480.929 |
| 313.15 | 16087.30 | 1482.944 |
| 313.15 | 18046.60 | 1484.852 |
| 313.15 | 20004.20 | 1486.73 |
| 313.15 | 22154.30 | 1488.763 |
| 313.15 | 23944.20 | 1490.446 |
| 313.15 | 26099.80 | 1492.424 |
| 313.15 | 28042.50 | 1494.215 |
| 313.15 | 29905.50 | 1495.902 |
| 333.15 | 100.42 | 1439.385 |
| 333.15 | 1115.03 | 1440.596 |
| 333.15 | 1943.37 | 1441.571 |
| 333.15 | 4094.54 | 1444.097 |
| 333.15 | 6114.22 | 1446.439 |
| 333.15 | 7927.80 | 1448.512 |
| 333.15 | 10021.70 | 1450.842 |
| 333.15 | 11958.50 | 1453.001 |
| 333.15 | 13999.00 | 1455.239 |
| 333.15 | 16048.70 | 1457.443 |
| 333.15 | 18155.70 | 1459.682 |
| 333.15 | 20007.80 | 1461.631 |
| 333.15 | 22157.50 | 1463.842 |
| 333.15 | 24129.60 | 1465.857 |
| 333.15 | 26094.50 | 1467.846 |
| 333.15 | 28018.50 | 1469.764 |
| 333.15 | 29890.30 | 1471.607 |
| 353.15 | 99.80 | 1411.936 |
| 353.15 | 1173.75 | 1413.368 |
| 353.15 | 1944.34 | 1414.39 |
| 353.15 | 3949.81 | 1417.013 |
| 353.15 | 5968.93 | 1419.612 |
| 353.15 | 7990.46 | 1422.164 |
| 353.15 | 9916.05 | 1424.555 |
| 353.15 | 11986.60 | 1427.088 |
| 353.15 | 14134.60 | 1429.674 |
| 353.15 | 15921.30 | 1431.797 |
| 353.15 | 18146.30 | 1434.386 |
| 353.15 | 19873.50 | 1436.374 |
| 353.15 | 22180.00 | 1438.986 |
| 353.15 | 23963.50 | 1440.977 |
| 353.15 | 26085.20 | 1443.316 |
| 353.15 | 28122.10 | 1445.529 |
| 353.15 | 29956.10 | 1447.501 |
| 373.15 | 98.54 | 1384.068 |
| 373.15 | 1150.11 | 1385.641 |
| 373.15 | 2174.39 | 1387.16 |
| 373.15 | 3917.65 | 1389.708 |
| 373.15 | 6182.40 | 1392.956 |
| 373.15 | 8042.69 | 1395.57 |
| 373.15 | 10003.40 | 1398.276 |
| 373.15 | 12007.70 | 1400.991 |
| 373.15 | 14086.40 | 1403.757 |
| 373.15 | 15912.60 | 1406.155 |
| 373.15 | 18065.60 | 1408.912 |
| 373.15 | 19882.10 | 1411.213 |
| 373.15 | 22174.10 | 1414.047 |
| 373.15 | 24052.60 | 1416.329 |
| 373.15 | 25897.20 | 1418.541 |
| 373.15 | 27711.00 | 1420.705 |
| 373.15 | 29530.80 | 1422.851 |
| 393.15 | 97.33 | 1355.66 |
| 393.15 | 1226.04 | 1357.559 |
| 393.15 | 2181.20 | 1359.152 |
| 393.15 | 3965.26 | 1362.078 |
| 393.15 | 6075.43 | 1365.466 |
| 393.15 | 8146.91 | 1368.751 |
| 393.15 | 9937.30 | 1371.465 |
| 393.15 | 11969.70 | 1374.529 |
| 393.15 | 14177.00 | 1377.777 |
| 393.15 | 15955.80 | 1380.344 |
| 393.15 | 18163.70 | 1383.473 |
| 393.15 | 20146.90 | 1386.231 |
| 393.15 | 22175.70 | 1388.998 |
| 393.15 | 23981.50 | 1391.424 |
| 393.15 | 26169.90 | 1394.302 |
| 393.15 | 28005.40 | 1396.697 |
| 393.15 | 29541.50 | 1398.685 |
| 413.15 | 99.45 | 1326.547 |
| 413.15 | 1202.85 | 1328.655 |
| 413.15 | 2177.13 | 1330.512 |
| 413.15 | 3915.54 | 1333.735 |
| 413.15 | 6185.52 | 1337.833 |
| 413.15 | 8176.14 | 1341.325 |
| 413.15 | 10032.40 | 1344.48 |
| 413.15 | 12103.60 | 1348.01 |
| 413.15 | 13991.80 | 1351.03 |
| 413.15 | 15890.50 | 1354.115 |
| 413.15 | 18162.20 | 1357.681 |
| 413.15 | 19933.00 | 1360.414 |
| 413.15 | 22150.20 | 1363.736 |
| 413.15 | 24133.10 | 1366.656 |
| 413.15 | 26038.90 | 1369.413 |
| 413.15 | 27898.50 | 1372.058 |
| 413.15 | 29858.00 | 1374.805 |
| 433.15 | 1243.75 | 1299.092 |
| 433.15 | 1973.28 | 1300.66 |
| 433.15 | 4075.91 | 1305.09 |
| 433.15 | 6197.75 | 1309.427 |
| 433.15 | 7981.47 | 1312.955 |
| 433.15 | 10019.80 | 1316.907 |
| 433.15 | 12072.60 | 1320.75 |
| 433.15 | 14033.50 | 1324.335 |
| 433.15 | 15960.20 | 1327.765 |
| 433.15 | 17921.10 | 1331.186 |
| 433.15 | 19992.20 | 1334.752 |
| 433.15 | 21950.20 | 1337.95 |
| 433.15 | 24017.90 | 1341.307 |
| 433.15 | 26143.40 | 1344.678 |
| 433.15 | 28052.40 | 1347.64 |
| 433.15 | 29864.50 | 1350.426 |
| 453.15 | 1135.36 | 1268.141 |
| 453.15 | 1982.45 | 1270.245 |
| 453.15 | 4017.67 | 1275.165 |
| 453.15 | 6189.02 | 1280.221 |
| 453.15 | 7994.19 | 1284.28 |
| 453.15 | 10138.80 | 1288.978 |
| 453.15 | 12157.20 | 1293.201 |
| 453.15 | 13981.80 | 1296.937 |
| 453.15 | 16133.80 | 1301.214 |
| 453.15 | 18121.60 | 1305.054 |
| 453.15 | 19974.20 | 1308.564 |
| 453.15 | 22140.80 | 1312.522 |
| 453.15 | 24115.40 | 1316.051 |
| 453.15 | 26121.30 | 1319.557 |
| 453.15 | 28034.20 | 1322.825 |
| 453.15 | 29912.10 | 1325.979 |
| 473.15 | 1191.19 | 1236.278 |
| 473.15 | 2175.44 | 1239.118 |
| 473.15 | 4131.48 | 1244.576 |
| 473.15 | 5988.10 | 1249.543 |
| 473.15 | 8161.41 | 1255.135 |
| 473.15 | 10165.40 | 1260.077 |
| 473.15 | 12165.90 | 1264.845 |
| 473.15 | 14162.70 | 1269.434 |
| 473.15 | 16124.70 | 1273.802 |
| 473.15 | 18166.70 | 1278.202 |
| 473.15 | 20146.20 | 1282.345 |
| 473.15 | 22123.10 | 1286.362 |
| 473.15 | 24157.00 | 1290.388 |
| 473.15 | 26074.70 | 1294.08 |
| 473.15 | 28019.90 | 1297.733 |
| 473.15 | 29860.30 | 1301.116 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [312.67; 458.01] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.44191e+01 | |||
| Coefficient B | -3.72354e+03 | |||
| Coefficient C | -4.91780e+01 | |||
| Temperature range, min. | 312.67 | |||
| Temperature range, max. | 458.01 | |||
| Pvap | 1.33 | kPa | 312.67 | Calculated Property |
| Pvap | 3.02 | kPa | 328.82 | Calculated Property |
| Pvap | 6.24 | kPa | 344.97 | Calculated Property |
| Pvap | 11.97 | kPa | 361.12 | Calculated Property |
| Pvap | 21.54 | kPa | 377.27 | Calculated Property |
| Pvap | 36.68 | kPa | 393.41 | Calculated Property |
| Pvap | 59.56 | kPa | 409.56 | Calculated Property |
| Pvap | 92.77 | kPa | 425.71 | Calculated Property |
| Pvap | 139.33 | kPa | 441.86 | Calculated Property |
| Pvap | 202.63 | kPa | 458.01 | Calculated Property |
| Pvap | [7.67e-03; 4446.48] | kPa | [242.43; 670.15] |
KDB Vapor Pressure Data
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 7.92440e+01 | |||
| Coefficient B | -7.92948e+03 | |||
| Coefficient C | -9.41640e+00 | |||
| Coefficient D | 5.04459e-06 | |||
| Temperature range, min. | 242.43 | |||
| Temperature range, max. | 670.15 | |||
| Pvap | 7.67e-03 | kPa | 242.43 | Calculated Property |
| Pvap | 0.34 | kPa | 289.95 | Calculated Property |
| Pvap | 4.50 | kPa | 337.48 | Calculated Property |
| Pvap | 28.15 | kPa | 385.00 | Calculated Property |
| Pvap | 110.01 | kPa | 432.53 | Calculated Property |
| Pvap | 315.03 | kPa | 480.05 | Calculated Property |
| Pvap | 730.18 | kPa | 527.58 | Calculated Property |
| Pvap | 1461.92 | kPa | 575.10 | Calculated Property |
| Pvap | 2642.33 | kPa | 622.63 | Calculated Property |
| Pvap | 4446.48 | kPa | 670.15 | Calculated Property |
Similar Compounds
Find more compounds similar to Benzene, bromo-.
Mixtures
- Benzene, bromo- + Triethylene glycol
- Benzene, bromo- + Methyl Alcohol
- Benzene, bromo- + 1-Hexanol, 2-ethyl-
- Benzene, bromo- + Heptane
- Benzene, nitro- + Benzene, bromo-
- Benzene, bromo- + Dimethyl Sulfoxide
- Benzene, bromo- + Formamide, N,N-dimethyl-
- Benzene, bromo- + N-Formylmorpholine
- Acetonitrile + Benzene, bromo-
- Benzene, bromo- + Ethane, 1,2-dichloro-
- Benzene, bromo- + m-Chloroaniline
- Acetic acid, pentyl ester + Benzene, bromo-
- Acetic acid, chloro-, ethyl ester + Benzene, bromo-
- Ethane, 1,2-dibromo- + Benzene, bromo-
- Benzene, bromo- + Methyl formate
- Ethyl formate + Benzene, bromo-
- Formic acid, propyl ester + Benzene, bromo-
- Acetic acid, phenylmethyl ester + Benzene, bromo-
- Benzene, bromo- + Ethanol, 2-methoxy-
- Benzene, bromo- + Benzene, chloro-
Find more mixtures with Benzene, bromo-.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Cheméo Relay (1.0)
- Crippen Method
- Thermophysical Properties For Diethylene Glycol + Nitrobenzene and Triethylene Glycol + (Chloro-, Bromo-, Nitro-) Benzene Systems at Different Temperatures
- Thermophysical Properties of Binary Mixtures of Methanol with Chlorobenzene and Bromobenzene from 293K to 313K
- Densities, Viscosities, Speeds of Sound, and Refractive Indices of Binary Mixtures of 2-Ethyl-1-hexanol with Benzene and Halobenzenes
- Isobaric vapour liquid equilibria for binary mixtures of n-heptane with bromobenzene, chlorobenzene and fluorobenzene at atmospheric pressure
- Excess Gibbs energies of binary mixtures formed by nitrobenzene with selected compounds at 94.95 kPa
- Vapor-liquid equilibrium for the binary mixtures of dimethylsulfoxide with substituted benzenes
- Excess enthalpies of dimethylsulfoxide with substituted benzenes at 298.15K
- Activity coefficients and excess Gibbs energy of binary mixtures of N,N-dimethyl formamide with selected compounds at 95.5 kPa
- Refractive properties, speed of sound and FT-IR study of binary mixtures of N-formylmorpholine with some halobenzenes at 303.15, 308.15 and 313.15 K
- (Vapor + liquid) equilibrium of the binary mixtures formed by acetonitrile with selected compounds at 95.5 kPa
- Measurement and correlation of the (p, ?, T) relation of liquid n-heptane, n-nonane, 2,4-dichlorotoluene, and bromobenzene in the temperature range from (233.15 to 473.15) K at pressures up to 30 MPa for use as density reference liquids
- Activity coefficients at infinite dilution of organic solutes in 1-hexyl-3- methylimidazolium trifluoroacetate and influence of interfacial adsorption using gas liquid chromatography
- Thermodynamics of solvation in propylene glycol and methyl cellosolve
- Phase behavior of ionic liquids 1-alkyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imides with halogenated benzenes
- Theoretical and experimental study on volumetric and electromagnetic properties of binary systems consisting of 1,2-dichloroethane with benzene and its derivatives at T = (293.15 to 333.15) K
- Studies on the importance of nature of substituent on the thermodynamic and transport properties of liquid mixtures at various temperatures
- Abraham model correlations for describing the thermodynamic properties of solute transfer into pentyl acetate based on headspace chromatographic and solubility measurements
- Volumetric and electromagnetic properties of binary mixtures consist of benzene derivatives at different temperature and ternary mixtures with 1,2-dichloroethane at T = 293.15 K with application of the Prigogine-Flory-Patterson theory and PC-SAFT
- Density, Viscosity, Refractive Index, and Speed of Sound in the Binary Mixtures of Ethyl Chloroacetate + Cyclohexanone, + Chlorobenzene, + Bromobenzene, or + Benzyl Alcohol at (298.15, 303.15, and 308.15) K
- Solubilities of p-Tolylboronic Acid, Bromobenzene and 4-Phenyltoluene in Carbon Dioxide at Elevated Pressures
- Isobaric Vapor-Liquid Equilibria for Binary Mixtures of 1,2-Dibromoethane with Benzene, Toluene, Fluorobenzene, and Bromobenzene at Atmospheric Pressure
- Thermophysical properties of the binary mixtures of 1,2-Dichloroethane with Chlorobenzene and Bromobenzene from 298.15 to 313.15 K
- Measuring the Aqueous Henry's Law Constant at Elevated Temperatures Using an Extended EPICS Technique
- Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
- Solubility of Hydrofluorocarbons in Halobenzene Solvents
- Thermochemistry of Halogen-Substituted Methylbenzenes
- Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
- Excess Volumes of Binary Solutions of Methyl Formate, Ethyl Formate, Propyl Formate, and Benzyl Acetate with Bromo-, Chloro-, and Nitrobenzenes at (303.15, 308.15, and 313.15) K
- Fusion Curves and Enthalpy and Internal Energy Changes of Benzene, Nitrobenzene, Bromobenzene, and Chlorobenzene at Pressures up to 3500 MPa
- Liquid-Liquid Equilibria in Binary Mixtures Containing Chlorobenzene, Bromobenzene, and Iodobenzene with Ionic Liquid 1-Ethyl-3-methylimidazolim Bis(trifluoromethylsulfonyl)imide
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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.
Outlier This icon means
that the value is more than 2 standard deviations away from the
property mean.