- Name
- Tributyl phosphate
- InChI
- InChI=1S/C12H27O4P/c1-4-7-10-14-17(13,15-11-8-5-2)16-12-9-6-3/h4-12H2,1-3H3
- InChI Key
- STCOOQWBFONSKY-UHFFFAOYSA-N
- Formula
- C12H27O4P
- SMILES
- CCCCOP(=O)(OCCCC)OCCCC
- Mol. Weight (g/mol)
- 266.31
- CAS
- 126-73-8
- Name
- 1-Octanol
- InChI
- InChI=1S/C8H18O/c1-2-3-4-5-6-7-8-9/h9H,2-8H2,1H3
- InChI Key
- KBPLFHHGFOOTCA-UHFFFAOYSA-N
- Formula
- C8H18O
- SMILES
- CCCCCCCCO
- Mol. Weight (g/mol)
- 130.23
- CAS
- 111-87-5
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Datasets
- n0 - Refractive index (Na D-line) (2)
- ρl - Mass density, kg/m3 (4)
- csound,fluid - Speed of Sound, m/s (2)
- Tfus - Solid-liquid equilibrium temperature, K (4)
Refractive index (Na D-line) [ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 298.15 (Liquid)
| Mole fraction of Tributyl phosphate (1) - Liquid | Refractive index (Na D-line) - Liquid |
|---|---|
| 0.0496 | 1.427 |
| 0.0998 | 1.4259 |
| 0.1996 | 1.4243 |
| 0.2995 | 1.4225 |
| 0.4001 | 1.4216 |
| 0.5002 | 1.4213 |
| 0.5988 | 1.4213 |
| 0.7011 | 1.4216 |
| 0.8011 | 1.4219 |
| 0.9008 | 1.4221 |
| 0.9513 | 1.4224 |
Refractive index (Na D-line) [ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 298.15 (Liquid)
| Mole fraction of Tributyl phosphate (1) - Liquid | Refractive index (Na D-line) - Liquid |
|---|---|
| 0.0496 | 1.427 |
| 0.0998 | 1.4259 |
| 0.1996 | 1.4243 |
| 0.2995 | 1.4225 |
| 0.4001 | 1.4216 |
| 0.5002 | 1.4213 |
| 0.5988 | 1.4213 |
| 0.7011 | 1.4216 |
| 0.8011 | 1.4219 |
| 0.9008 | 1.4221 |
| 0.9513 | 1.4224 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Tributyl phosphate (1) - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 0.0160 | 825.66 |
| 298.15 | 0.0320 | 829.43 |
| 298.15 | 0.0490 | 833.45 |
| 298.15 | 0.1000 | 844.7 |
| 298.15 | 0.2000 | 864.91 |
| 298.15 | 0.3010 | 883.29 |
| 298.15 | 0.3980 | 899.38 |
| 298.15 | 0.5020 | 914.86 |
| 298.15 | 0.6020 | 928.59 |
| 298.15 | 0.7040 | 941.3 |
| 298.15 | 0.8030 | 952.67 |
| 298.15 | 0.9000 | 962.97 |
| 298.15 | 0.9190 | 964.88 |
| 298.15 | 0.9460 | 967.61 |
| 298.15 | 0.9710 | 970.09 |
| 303.15 | 0.0160 | 822.16 |
| 303.15 | 0.0320 | 825.92 |
| 303.15 | 0.0490 | 829.91 |
| 303.15 | 0.1000 | 841.09 |
| 303.15 | 0.2000 | 861.18 |
| 303.15 | 0.3010 | 879.45 |
| 303.15 | 0.3980 | 895.45 |
| 303.15 | 0.5020 | 910.85 |
| 303.15 | 0.6020 | 924.51 |
| 303.15 | 0.7040 | 937.15 |
| 303.15 | 0.8030 | 948.47 |
| 303.15 | 0.9000 | 958.71 |
| 303.15 | 0.9190 | 960.61 |
| 303.15 | 0.9460 | 963.32 |
| 303.15 | 0.9710 | 965.79 |
| 308.15 | 0.0160 | 818.64 |
| 308.15 | 0.0320 | 822.38 |
| 308.15 | 0.0490 | 826.35 |
| 308.15 | 0.1000 | 837.47 |
| 308.15 | 0.2000 | 857.44 |
| 308.15 | 0.3010 | 875.61 |
| 308.15 | 0.3980 | 891.51 |
| 308.15 | 0.5020 | 906.83 |
| 308.15 | 0.6020 | 920.42 |
| 308.15 | 0.7040 | 932.99 |
| 308.15 | 0.8030 | 944.26 |
| 308.15 | 0.9000 | 954.45 |
| 308.15 | 0.9190 | 956.34 |
| 308.15 | 0.9460 | 959.03 |
| 308.15 | 0.9710 | 961.49 |
| 313.15 | 0.0160 | 815.1 |
| 313.15 | 0.0320 | 818.82 |
| 313.15 | 0.0490 | 822.77 |
| 313.15 | 0.1000 | 833.83 |
| 313.15 | 0.2000 | 853.68 |
| 313.15 | 0.3010 | 871.75 |
| 313.15 | 0.3980 | 887.57 |
| 313.15 | 0.5020 | 902.81 |
| 313.15 | 0.6020 | 916.33 |
| 313.15 | 0.7040 | 928.84 |
| 313.15 | 0.8030 | 940.04 |
| 313.15 | 0.9000 | 950.19 |
| 313.15 | 0.9190 | 952.06 |
| 313.15 | 0.9460 | 954.75 |
| 313.15 | 0.9710 | 957.19 |
| 318.15 | 0.0160 | 811.54 |
| 318.15 | 0.0320 | 815.24 |
| 318.15 | 0.0490 | 819.16 |
| 318.15 | 0.1000 | 830.17 |
| 318.15 | 0.2000 | 849.91 |
| 318.15 | 0.3010 | 867.88 |
| 318.15 | 0.3980 | 883.61 |
| 318.15 | 0.5020 | 898.78 |
| 318.15 | 0.6020 | 912.23 |
| 318.15 | 0.7040 | 924.68 |
| 318.15 | 0.8030 | 935.82 |
| 318.15 | 0.9000 | 945.92 |
| 318.15 | 0.9190 | 947.78 |
| 318.15 | 0.9460 | 950.45 |
| 318.15 | 0.9710 | 952.88 |
| 323.15 | 0.0160 | 807.94 |
| 323.15 | 0.0320 | 811.63 |
| 323.15 | 0.0490 | 815.54 |
| 323.15 | 0.1000 | 826.49 |
| 323.15 | 0.2000 | 846.12 |
| 323.15 | 0.3010 | 864.0 |
| 323.15 | 0.3980 | 879.65 |
| 323.15 | 0.5020 | 894.74 |
| 323.15 | 0.6020 | 908.12 |
| 323.15 | 0.7040 | 920.51 |
| 323.15 | 0.8030 | 931.6 |
| 323.15 | 0.9000 | 941.65 |
| 323.15 | 0.9190 | 943.5 |
| 323.15 | 0.9460 | 946.15 |
| 323.15 | 0.9710 | 948.58 |
| 298.15 | 1.0000 | 972.77 |
| 303.15 | 1.0000 | 968.46 |
| 308.15 | 1.0000 | 964.15 |
| 313.15 | 1.0000 | 959.84 |
| 318.15 | 1.0000 | 955.52 |
| 323.15 | 1.0000 | 951.2 |
| 298.15 | 0.0000 | 821.74 |
| 303.15 | 0.0000 | 818.26 |
| 308.15 | 0.0000 | 814.76 |
| 313.15 | 0.0000 | 811.24 |
| 318.15 | 0.0000 | 807.69 |
| 323.15 | 0.0000 | 804.12 |
Mass density, kg/m3 [ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 298.15 (Liquid)
| Mole fraction of Tributyl phosphate (1) - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 0.0496 | 833.7 |
| 0.0998 | 844.7 |
| 0.1996 | 865.0 |
| 0.2995 | 883.2 |
| 0.4001 | 899.7 |
| 0.5002 | 914.6 |
| 0.5988 | 928.1 |
| 0.7011 | 940.9 |
| 0.8011 | 952.5 |
| 0.9008 | 963.0 |
| 0.9513 | 968.0 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Tributyl phosphate (1) - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 0.0160 | 825.66 |
| 298.15 | 0.0320 | 829.43 |
| 298.15 | 0.0490 | 833.45 |
| 298.15 | 0.1000 | 844.7 |
| 298.15 | 0.2000 | 864.91 |
| 298.15 | 0.3010 | 883.29 |
| 298.15 | 0.3980 | 899.38 |
| 298.15 | 0.5020 | 914.86 |
| 298.15 | 0.6020 | 928.59 |
| 298.15 | 0.7040 | 941.3 |
| 298.15 | 0.8030 | 952.67 |
| 298.15 | 0.9000 | 962.97 |
| 298.15 | 0.9190 | 964.88 |
| 298.15 | 0.9460 | 967.61 |
| 298.15 | 0.9710 | 970.09 |
| 303.15 | 0.0160 | 822.16 |
| 303.15 | 0.0320 | 825.92 |
| 303.15 | 0.0490 | 829.91 |
| 303.15 | 0.1000 | 841.09 |
| 303.15 | 0.2000 | 861.18 |
| 303.15 | 0.3010 | 879.45 |
| 303.15 | 0.3980 | 895.45 |
| 303.15 | 0.5020 | 910.85 |
| 303.15 | 0.6020 | 924.51 |
| 303.15 | 0.7040 | 937.15 |
| 303.15 | 0.8030 | 948.47 |
| 303.15 | 0.9000 | 958.71 |
| 303.15 | 0.9190 | 960.61 |
| 303.15 | 0.9460 | 963.32 |
| 303.15 | 0.9710 | 965.79 |
| 308.15 | 0.0160 | 818.64 |
| 308.15 | 0.0320 | 822.38 |
| 308.15 | 0.0490 | 826.35 |
| 308.15 | 0.1000 | 837.47 |
| 308.15 | 0.2000 | 857.44 |
| 308.15 | 0.3010 | 875.61 |
| 308.15 | 0.3980 | 891.51 |
| 308.15 | 0.5020 | 906.83 |
| 308.15 | 0.6020 | 920.42 |
| 308.15 | 0.7040 | 932.99 |
| 308.15 | 0.8030 | 944.26 |
| 308.15 | 0.9000 | 954.45 |
| 308.15 | 0.9190 | 956.34 |
| 308.15 | 0.9460 | 959.03 |
| 308.15 | 0.9710 | 961.49 |
| 313.15 | 0.0160 | 815.1 |
| 313.15 | 0.0320 | 818.82 |
| 313.15 | 0.0490 | 822.77 |
| 313.15 | 0.1000 | 833.83 |
| 313.15 | 0.2000 | 853.68 |
| 313.15 | 0.3010 | 871.75 |
| 313.15 | 0.3980 | 887.57 |
| 313.15 | 0.5020 | 902.81 |
| 313.15 | 0.6020 | 916.33 |
| 313.15 | 0.7040 | 928.84 |
| 313.15 | 0.8030 | 940.04 |
| 313.15 | 0.9000 | 950.19 |
| 313.15 | 0.9190 | 952.06 |
| 313.15 | 0.9460 | 954.75 |
| 313.15 | 0.9710 | 957.19 |
| 318.15 | 0.0160 | 811.54 |
| 318.15 | 0.0320 | 815.24 |
| 318.15 | 0.0490 | 819.16 |
| 318.15 | 0.1000 | 830.17 |
| 318.15 | 0.2000 | 849.91 |
| 318.15 | 0.3010 | 867.88 |
| 318.15 | 0.3980 | 883.61 |
| 318.15 | 0.5020 | 898.78 |
| 318.15 | 0.6020 | 912.23 |
| 318.15 | 0.7040 | 924.68 |
| 318.15 | 0.8030 | 935.82 |
| 318.15 | 0.9000 | 945.92 |
| 318.15 | 0.9190 | 947.78 |
| 318.15 | 0.9460 | 950.45 |
| 318.15 | 0.9710 | 952.88 |
| 323.15 | 0.0160 | 807.94 |
| 323.15 | 0.0320 | 811.63 |
| 323.15 | 0.0490 | 815.54 |
| 323.15 | 0.1000 | 826.49 |
| 323.15 | 0.2000 | 846.12 |
| 323.15 | 0.3010 | 864.0 |
| 323.15 | 0.3980 | 879.65 |
| 323.15 | 0.5020 | 894.74 |
| 323.15 | 0.6020 | 908.12 |
| 323.15 | 0.7040 | 920.51 |
| 323.15 | 0.8030 | 931.6 |
| 323.15 | 0.9000 | 941.65 |
| 323.15 | 0.9190 | 943.5 |
| 323.15 | 0.9460 | 946.15 |
| 323.15 | 0.9710 | 948.58 |
| 298.15 | 1.0000 | 972.77 |
| 303.15 | 1.0000 | 968.46 |
| 308.15 | 1.0000 | 964.15 |
| 313.15 | 1.0000 | 959.84 |
| 318.15 | 1.0000 | 955.52 |
| 323.15 | 1.0000 | 951.2 |
| 298.15 | 0.0000 | 821.74 |
| 303.15 | 0.0000 | 818.26 |
| 308.15 | 0.0000 | 814.76 |
| 313.15 | 0.0000 | 811.24 |
| 318.15 | 0.0000 | 807.69 |
| 323.15 | 0.0000 | 804.12 |
Mass density, kg/m3 [ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 298.15 (Liquid)
| Mole fraction of Tributyl phosphate (1) - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 0.0496 | 833.7 |
| 0.0998 | 844.7 |
| 0.1996 | 865.0 |
| 0.2995 | 883.2 |
| 0.4001 | 899.7 |
| 0.5002 | 914.6 |
| 0.5988 | 928.1 |
| 0.7011 | 940.9 |
| 0.8011 | 952.5 |
| 0.9008 | 963.0 |
| 0.9513 | 968.0 |
Speed of sound, m/s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Tributyl phosphate (1) - Liquid | Speed of sound, m/s - Liquid |
| 298.15 | 0.0000 | 1349.0 |
| 298.15 | 0.0160 | 1344.0 |
| 298.15 | 0.0320 | 1341.0 |
| 298.15 | 0.0490 | 1337.0 |
| 298.15 | 0.1000 | 1328.0 |
| 298.15 | 0.2000 | 1312.0 |
| 298.15 | 0.3010 | 1300.0 |
| 298.15 | 0.3980 | 1291.0 |
| 298.15 | 0.5020 | 1283.0 |
| 298.15 | 0.6020 | 1277.0 |
| 298.15 | 0.7040 | 1273.0 |
| 298.15 | 0.8030 | 1269.0 |
| 298.15 | 0.9000 | 1267.0 |
| 298.15 | 0.9190 | 1267.0 |
| 298.15 | 0.9460 | 1266.0 |
| 298.15 | 0.9710 | 1266.0 |
| 298.15 | 1.0000 | 1265.0 |
| 303.15 | 0.0000 | 1332.0 |
| 303.15 | 0.0160 | 1327.0 |
| 303.15 | 0.0320 | 1324.0 |
| 303.15 | 0.0490 | 1320.0 |
| 303.15 | 0.1000 | 1311.0 |
| 303.15 | 0.2000 | 1295.0 |
| 303.15 | 0.3010 | 1283.0 |
| 303.15 | 0.3980 | 1274.0 |
| 303.15 | 0.5020 | 1266.0 |
| 303.15 | 0.6020 | 1260.0 |
| 303.15 | 0.7040 | 1256.0 |
| 303.15 | 0.8030 | 1252.0 |
| 303.15 | 0.9000 | 1250.0 |
| 303.15 | 0.9190 | 1250.0 |
| 303.15 | 0.9460 | 1249.0 |
| 303.15 | 0.9710 | 1249.0 |
| 303.15 | 1.0000 | 1248.0 |
| 308.15 | 0.0000 | 1315.0 |
| 308.15 | 0.0160 | 1310.0 |
| 308.15 | 0.0320 | 1307.0 |
| 308.15 | 0.0490 | 1303.0 |
| 308.15 | 0.1000 | 1294.0 |
| 308.15 | 0.2000 | 1278.0 |
| 308.15 | 0.3010 | 1266.0 |
| 308.15 | 0.3980 | 1257.0 |
| 308.15 | 0.5020 | 1249.0 |
| 308.15 | 0.6020 | 1243.0 |
| 308.15 | 0.7040 | 1239.0 |
| 308.15 | 0.8030 | 1236.0 |
| 308.15 | 0.9000 | 1233.0 |
| 308.15 | 0.9190 | 1233.0 |
| 308.15 | 0.9460 | 1232.0 |
| 308.15 | 0.9710 | 1232.0 |
| 308.15 | 1.0000 | 1231.0 |
| 313.15 | 0.0000 | 1299.0 |
| 313.15 | 0.0160 | 1293.0 |
| 313.15 | 0.0320 | 1290.0 |
| 313.15 | 0.0490 | 1286.0 |
| 313.15 | 0.1000 | 1277.0 |
| 313.15 | 0.2000 | 1262.0 |
| 313.15 | 0.3010 | 1249.0 |
| 313.15 | 0.3980 | 1240.0 |
| 313.15 | 0.5020 | 1232.0 |
| 313.15 | 0.6020 | 1226.0 |
| 313.15 | 0.7040 | 1222.0 |
| 313.15 | 0.8030 | 1219.0 |
| 313.15 | 0.9000 | 1216.0 |
| 313.15 | 0.9190 | 1216.0 |
| 313.15 | 0.9460 | 1215.0 |
| 313.15 | 0.9710 | 1215.0 |
| 313.15 | 1.0000 | 1214.0 |
| 318.15 | 0.0000 | 1282.0 |
| 318.15 | 0.0160 | 1277.0 |
| 318.15 | 0.0320 | 1273.0 |
| 318.15 | 0.0490 | 1270.0 |
| 318.15 | 0.1000 | 1260.0 |
| 318.15 | 0.2000 | 1245.0 |
| 318.15 | 0.3010 | 1233.0 |
| 318.15 | 0.3980 | 1223.0 |
| 318.15 | 0.5020 | 1216.0 |
| 318.15 | 0.6020 | 1210.0 |
| 318.15 | 0.7040 | 1206.0 |
| 318.15 | 0.8030 | 1202.0 |
| 318.15 | 0.9000 | 1200.0 |
| 318.15 | 0.9190 | 1199.0 |
| 318.15 | 0.9460 | 1199.0 |
| 318.15 | 0.9710 | 1198.0 |
| 318.15 | 1.0000 | 1198.0 |
| 323.15 | 0.0000 | 1265.0 |
| 323.15 | 0.0160 | 1260.0 |
| 323.15 | 0.0320 | 1257.0 |
| 323.15 | 0.0490 | 1253.0 |
| 323.15 | 0.1000 | 1244.0 |
| 323.15 | 0.2000 | 1229.0 |
| 323.15 | 0.3010 | 1216.0 |
| 323.15 | 0.3980 | 1207.0 |
| 323.15 | 0.5020 | 1199.0 |
| 323.15 | 0.6020 | 1194.0 |
| 323.15 | 0.7040 | 1188.0 |
| 323.15 | 0.8030 | 1186.0 |
| 323.15 | 0.9000 | 1183.0 |
| 323.15 | 0.9190 | 1183.0 |
| 323.15 | 0.9460 | 1182.0 |
| 323.15 | 0.9710 | 1182.0 |
| 323.15 | 1.0000 | 1181.0 |
Speed of sound, m/s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Tributyl phosphate (1) - Liquid | Speed of sound, m/s - Liquid |
| 298.15 | 0.0000 | 1349.0 |
| 298.15 | 0.0160 | 1344.0 |
| 298.15 | 0.0320 | 1341.0 |
| 298.15 | 0.0490 | 1337.0 |
| 298.15 | 0.1000 | 1328.0 |
| 298.15 | 0.2000 | 1312.0 |
| 298.15 | 0.3010 | 1300.0 |
| 298.15 | 0.3980 | 1291.0 |
| 298.15 | 0.5020 | 1283.0 |
| 298.15 | 0.6020 | 1277.0 |
| 298.15 | 0.7040 | 1273.0 |
| 298.15 | 0.8030 | 1269.0 |
| 298.15 | 0.9000 | 1267.0 |
| 298.15 | 0.9190 | 1267.0 |
| 298.15 | 0.9460 | 1266.0 |
| 298.15 | 0.9710 | 1266.0 |
| 298.15 | 1.0000 | 1265.0 |
| 303.15 | 0.0000 | 1332.0 |
| 303.15 | 0.0160 | 1327.0 |
| 303.15 | 0.0320 | 1324.0 |
| 303.15 | 0.0490 | 1320.0 |
| 303.15 | 0.1000 | 1311.0 |
| 303.15 | 0.2000 | 1295.0 |
| 303.15 | 0.3010 | 1283.0 |
| 303.15 | 0.3980 | 1274.0 |
| 303.15 | 0.5020 | 1266.0 |
| 303.15 | 0.6020 | 1260.0 |
| 303.15 | 0.7040 | 1256.0 |
| 303.15 | 0.8030 | 1252.0 |
| 303.15 | 0.9000 | 1250.0 |
| 303.15 | 0.9190 | 1250.0 |
| 303.15 | 0.9460 | 1249.0 |
| 303.15 | 0.9710 | 1249.0 |
| 303.15 | 1.0000 | 1248.0 |
| 308.15 | 0.0000 | 1315.0 |
| 308.15 | 0.0160 | 1310.0 |
| 308.15 | 0.0320 | 1307.0 |
| 308.15 | 0.0490 | 1303.0 |
| 308.15 | 0.1000 | 1294.0 |
| 308.15 | 0.2000 | 1278.0 |
| 308.15 | 0.3010 | 1266.0 |
| 308.15 | 0.3980 | 1257.0 |
| 308.15 | 0.5020 | 1249.0 |
| 308.15 | 0.6020 | 1243.0 |
| 308.15 | 0.7040 | 1239.0 |
| 308.15 | 0.8030 | 1236.0 |
| 308.15 | 0.9000 | 1233.0 |
| 308.15 | 0.9190 | 1233.0 |
| 308.15 | 0.9460 | 1232.0 |
| 308.15 | 0.9710 | 1232.0 |
| 308.15 | 1.0000 | 1231.0 |
| 313.15 | 0.0000 | 1299.0 |
| 313.15 | 0.0160 | 1293.0 |
| 313.15 | 0.0320 | 1290.0 |
| 313.15 | 0.0490 | 1286.0 |
| 313.15 | 0.1000 | 1277.0 |
| 313.15 | 0.2000 | 1262.0 |
| 313.15 | 0.3010 | 1249.0 |
| 313.15 | 0.3980 | 1240.0 |
| 313.15 | 0.5020 | 1232.0 |
| 313.15 | 0.6020 | 1226.0 |
| 313.15 | 0.7040 | 1222.0 |
| 313.15 | 0.8030 | 1219.0 |
| 313.15 | 0.9000 | 1216.0 |
| 313.15 | 0.9190 | 1216.0 |
| 313.15 | 0.9460 | 1215.0 |
| 313.15 | 0.9710 | 1215.0 |
| 313.15 | 1.0000 | 1214.0 |
| 318.15 | 0.0000 | 1282.0 |
| 318.15 | 0.0160 | 1277.0 |
| 318.15 | 0.0320 | 1273.0 |
| 318.15 | 0.0490 | 1270.0 |
| 318.15 | 0.1000 | 1260.0 |
| 318.15 | 0.2000 | 1245.0 |
| 318.15 | 0.3010 | 1233.0 |
| 318.15 | 0.3980 | 1223.0 |
| 318.15 | 0.5020 | 1216.0 |
| 318.15 | 0.6020 | 1210.0 |
| 318.15 | 0.7040 | 1206.0 |
| 318.15 | 0.8030 | 1202.0 |
| 318.15 | 0.9000 | 1200.0 |
| 318.15 | 0.9190 | 1199.0 |
| 318.15 | 0.9460 | 1199.0 |
| 318.15 | 0.9710 | 1198.0 |
| 318.15 | 1.0000 | 1198.0 |
| 323.15 | 0.0000 | 1265.0 |
| 323.15 | 0.0160 | 1260.0 |
| 323.15 | 0.0320 | 1257.0 |
| 323.15 | 0.0490 | 1253.0 |
| 323.15 | 0.1000 | 1244.0 |
| 323.15 | 0.2000 | 1229.0 |
| 323.15 | 0.3010 | 1216.0 |
| 323.15 | 0.3980 | 1207.0 |
| 323.15 | 0.5020 | 1199.0 |
| 323.15 | 0.6020 | 1194.0 |
| 323.15 | 0.7040 | 1188.0 |
| 323.15 | 0.8030 | 1186.0 |
| 323.15 | 0.9000 | 1183.0 |
| 323.15 | 0.9190 | 1183.0 |
| 323.15 | 0.9460 | 1182.0 |
| 323.15 | 0.9710 | 1182.0 |
| 323.15 | 1.0000 | 1181.0 |
Solid-liquid equilibrium temperature, K [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Mole fraction of Tributyl phosphate (1) - Liquid | Solid-liquid equilibrium temperature, K - Liquid |
|---|---|
| 0.0000 | 257.70 |
| 0.0522 | 256.33 |
| 0.0997 | 255.02 |
| 0.2000 | 252.18 |
| 0.3020 | 248.54 |
| 0.3988 | 244.08 |
| 0.5114 | 238.61 |
| 0.5999 | 232.71 |
| 0.6997 | 224.05 |
| 0.7999 | 212.92 |
| 0.8998 | 194.59 |
Solid-liquid equilibrium temperature, K [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Mole fraction of Tributyl phosphate (1) - Liquid | Solid-liquid equilibrium temperature, K - Liquid |
|---|---|
| 0.9100 | 191.76 |
| 0.9500 | 192.97 |
| 1.0000 | 194.20 |
Solid-liquid equilibrium temperature, K [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Mole fraction of Tributyl phosphate (1) - Liquid | Solid-liquid equilibrium temperature, K - Liquid |
|---|---|
| 0.0000 | 257.70 |
| 0.0522 | 256.33 |
| 0.0997 | 255.02 |
| 0.2000 | 252.18 |
| 0.3020 | 248.54 |
| 0.3988 | 244.08 |
| 0.5114 | 238.61 |
| 0.5999 | 232.71 |
| 0.6997 | 224.05 |
| 0.7999 | 212.92 |
| 0.8998 | 194.59 |
Solid-liquid equilibrium temperature, K [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Mole fraction of Tributyl phosphate (1) - Liquid | Solid-liquid equilibrium temperature, K - Liquid |
|---|---|
| 0.9100 | 191.76 |
| 0.9500 | 192.97 |
| 1.0000 | 194.20 |
Sources
- SLE and LLE for tri-butylphosphate or tri-octylamine contained systems; extractive solvents of Molybdenum
- Volumetric and compressibility studies on tri-n-butyl phosphate (TBP)-phase modifier (1-octanol, 1-decanol and isodecanol) interactions from T = (298.15 to 323.15) K
- Solid-Liquid Equilibria, Excess Molar Volumes, and Molar Refractivity Deviations for Extractive Solvents of Molybdenum