- 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-Decanol
- InChI
- InChI=1S/C10H22O/c1-2-3-4-5-6-7-8-9-10-11/h11H,2-10H2,1H3
- InChI Key
- MWKFXSUHUHTGQN-UHFFFAOYSA-N
- Formula
- C10H22O
- SMILES
- CCCCCCCCCCO
- Mol. Weight (g/mol)
- 158.28
- CAS
- 112-30-1
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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 | 1.4341 |
| 0.0999 | 1.4329 |
| 0.2008 | 1.4307 |
| 0.3001 | 1.429 |
| 0.4004 | 1.4275 |
| 0.4996 | 1.4262 |
| 0.6007 | 1.4252 |
| 0.6981 | 1.4244 |
| 0.7985 | 1.4236 |
| 0.9003 | 1.423 |
| 0.9505 | 1.4227 |
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 | 1.4341 |
| 0.0999 | 1.4329 |
| 0.2008 | 1.4307 |
| 0.3001 | 1.429 |
| 0.4004 | 1.4275 |
| 0.4996 | 1.4262 |
| 0.6007 | 1.4252 |
| 0.6981 | 1.4244 |
| 0.7985 | 1.4236 |
| 0.9003 | 1.423 |
| 0.9505 | 1.4227 |
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 | 0.0190 | 829.97 |
| 298.15 | 0.0400 | 833.94 |
| 298.15 | 0.0630 | 838.11 |
| 298.15 | 0.0990 | 844.9 |
| 298.15 | 0.2000 | 862.8 |
| 298.15 | 0.2920 | 877.97 |
| 298.15 | 0.3980 | 894.53 |
| 298.15 | 0.5010 | 909.53 |
| 298.15 | 0.5990 | 923.45 |
| 298.15 | 0.7030 | 937.13 |
| 298.15 | 0.8030 | 949.69 |
| 298.15 | 0.9040 | 961.91 |
| 298.15 | 0.9200 | 963.71 |
| 298.15 | 0.9460 | 966.71 |
| 298.15 | 0.9730 | 969.8 |
| 303.15 | 0.0190 | 826.54 |
| 303.15 | 0.0400 | 830.48 |
| 303.15 | 0.0630 | 834.63 |
| 303.15 | 0.0990 | 841.37 |
| 303.15 | 0.2000 | 859.15 |
| 303.15 | 0.2920 | 874.23 |
| 303.15 | 0.3980 | 890.68 |
| 303.15 | 0.5010 | 905.61 |
| 303.15 | 0.5990 | 919.44 |
| 303.15 | 0.7030 | 933.04 |
| 303.15 | 0.8030 | 945.53 |
| 303.15 | 0.9040 | 957.67 |
| 303.15 | 0.9200 | 959.45 |
| 303.15 | 0.9460 | 962.44 |
| 303.15 | 0.9730 | 965.51 |
| 308.15 | 0.0190 | 823.09 |
| 308.15 | 0.0400 | 827.02 |
| 308.15 | 0.0630 | 831.14 |
| 308.15 | 0.0990 | 837.84 |
| 308.15 | 0.2000 | 855.5 |
| 308.15 | 0.2920 | 870.47 |
| 308.15 | 0.3980 | 886.82 |
| 308.15 | 0.5010 | 901.68 |
| 308.15 | 0.5990 | 915.41 |
| 308.15 | 0.7030 | 928.94 |
| 308.15 | 0.8030 | 941.36 |
| 308.15 | 0.9040 | 953.42 |
| 308.15 | 0.9200 | 955.2 |
| 308.15 | 0.9460 | 958.17 |
| 308.15 | 0.9730 | 961.22 |
| 313.15 | 0.0190 | 819.63 |
| 313.15 | 0.0400 | 823.54 |
| 313.15 | 0.0630 | 827.64 |
| 313.15 | 0.0990 | 834.29 |
| 313.15 | 0.2000 | 851.83 |
| 313.15 | 0.2920 | 866.71 |
| 313.15 | 0.3980 | 882.96 |
| 313.15 | 0.5010 | 897.74 |
| 313.15 | 0.5990 | 911.39 |
| 313.15 | 0.7030 | 924.84 |
| 313.15 | 0.8030 | 937.19 |
| 313.15 | 0.9040 | 949.17 |
| 313.15 | 0.9200 | 950.94 |
| 313.15 | 0.9460 | 953.89 |
| 313.15 | 0.9730 | 956.92 |
| 318.15 | 0.0190 | 816.14 |
| 318.15 | 0.0400 | 820.04 |
| 318.15 | 0.0630 | 824.12 |
| 318.15 | 0.0990 | 830.73 |
| 318.15 | 0.2000 | 848.15 |
| 318.15 | 0.2920 | 862.93 |
| 318.15 | 0.3980 | 879.09 |
| 318.15 | 0.5010 | 893.8 |
| 318.15 | 0.5990 | 907.35 |
| 318.15 | 0.7030 | 920.73 |
| 318.15 | 0.8030 | 933.01 |
| 318.15 | 0.9040 | 944.91 |
| 318.15 | 0.9200 | 946.68 |
| 318.15 | 0.9460 | 949.62 |
| 318.15 | 0.9730 | 952.63 |
| 323.15 | 0.0190 | 812.64 |
| 323.15 | 0.0400 | 816.52 |
| 323.15 | 0.0630 | 820.57 |
| 323.15 | 0.0990 | 827.14 |
| 323.15 | 0.2000 | 844.46 |
| 323.15 | 0.2920 | 859.14 |
| 323.15 | 0.3980 | 875.2 |
| 323.15 | 0.5010 | 889.85 |
| 323.15 | 0.5990 | 903.31 |
| 323.15 | 0.7030 | 916.62 |
| 323.15 | 0.8030 | 928.83 |
| 323.15 | 0.9040 | 940.66 |
| 323.15 | 0.9200 | 942.42 |
| 323.15 | 0.9460 | 945.33 |
| 323.15 | 0.9730 | 948.33 |
| 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 | 826.36 |
| 303.15 | 0.0000 | 822.88 |
| 308.15 | 0.0000 | 819.43 |
| 313.15 | 0.0000 | 815.97 |
| 318.15 | 0.0000 | 812.49 |
| 323.15 | 0.0000 | 809.03 |
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 | 835.9 |
| 0.0999 | 845.2 |
| 0.2008 | 862.8 |
| 0.3001 | 879.1 |
| 0.4004 | 894.7 |
| 0.4996 | 909.3 |
| 0.6007 | 923.4 |
| 0.6981 | 936.3 |
| 0.7985 | 949.0 |
| 0.9003 | 961.2 |
| 0.9505 | 967.0 |
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 | 0.0190 | 829.97 |
| 298.15 | 0.0400 | 833.94 |
| 298.15 | 0.0630 | 838.11 |
| 298.15 | 0.0990 | 844.9 |
| 298.15 | 0.2000 | 862.8 |
| 298.15 | 0.2920 | 877.97 |
| 298.15 | 0.3980 | 894.53 |
| 298.15 | 0.5010 | 909.53 |
| 298.15 | 0.5990 | 923.45 |
| 298.15 | 0.7030 | 937.13 |
| 298.15 | 0.8030 | 949.69 |
| 298.15 | 0.9040 | 961.91 |
| 298.15 | 0.9200 | 963.71 |
| 298.15 | 0.9460 | 966.71 |
| 298.15 | 0.9730 | 969.8 |
| 303.15 | 0.0190 | 826.54 |
| 303.15 | 0.0400 | 830.48 |
| 303.15 | 0.0630 | 834.63 |
| 303.15 | 0.0990 | 841.37 |
| 303.15 | 0.2000 | 859.15 |
| 303.15 | 0.2920 | 874.23 |
| 303.15 | 0.3980 | 890.68 |
| 303.15 | 0.5010 | 905.61 |
| 303.15 | 0.5990 | 919.44 |
| 303.15 | 0.7030 | 933.04 |
| 303.15 | 0.8030 | 945.53 |
| 303.15 | 0.9040 | 957.67 |
| 303.15 | 0.9200 | 959.45 |
| 303.15 | 0.9460 | 962.44 |
| 303.15 | 0.9730 | 965.51 |
| 308.15 | 0.0190 | 823.09 |
| 308.15 | 0.0400 | 827.02 |
| 308.15 | 0.0630 | 831.14 |
| 308.15 | 0.0990 | 837.84 |
| 308.15 | 0.2000 | 855.5 |
| 308.15 | 0.2920 | 870.47 |
| 308.15 | 0.3980 | 886.82 |
| 308.15 | 0.5010 | 901.68 |
| 308.15 | 0.5990 | 915.41 |
| 308.15 | 0.7030 | 928.94 |
| 308.15 | 0.8030 | 941.36 |
| 308.15 | 0.9040 | 953.42 |
| 308.15 | 0.9200 | 955.2 |
| 308.15 | 0.9460 | 958.17 |
| 308.15 | 0.9730 | 961.22 |
| 313.15 | 0.0190 | 819.63 |
| 313.15 | 0.0400 | 823.54 |
| 313.15 | 0.0630 | 827.64 |
| 313.15 | 0.0990 | 834.29 |
| 313.15 | 0.2000 | 851.83 |
| 313.15 | 0.2920 | 866.71 |
| 313.15 | 0.3980 | 882.96 |
| 313.15 | 0.5010 | 897.74 |
| 313.15 | 0.5990 | 911.39 |
| 313.15 | 0.7030 | 924.84 |
| 313.15 | 0.8030 | 937.19 |
| 313.15 | 0.9040 | 949.17 |
| 313.15 | 0.9200 | 950.94 |
| 313.15 | 0.9460 | 953.89 |
| 313.15 | 0.9730 | 956.92 |
| 318.15 | 0.0190 | 816.14 |
| 318.15 | 0.0400 | 820.04 |
| 318.15 | 0.0630 | 824.12 |
| 318.15 | 0.0990 | 830.73 |
| 318.15 | 0.2000 | 848.15 |
| 318.15 | 0.2920 | 862.93 |
| 318.15 | 0.3980 | 879.09 |
| 318.15 | 0.5010 | 893.8 |
| 318.15 | 0.5990 | 907.35 |
| 318.15 | 0.7030 | 920.73 |
| 318.15 | 0.8030 | 933.01 |
| 318.15 | 0.9040 | 944.91 |
| 318.15 | 0.9200 | 946.68 |
| 318.15 | 0.9460 | 949.62 |
| 318.15 | 0.9730 | 952.63 |
| 323.15 | 0.0190 | 812.64 |
| 323.15 | 0.0400 | 816.52 |
| 323.15 | 0.0630 | 820.57 |
| 323.15 | 0.0990 | 827.14 |
| 323.15 | 0.2000 | 844.46 |
| 323.15 | 0.2920 | 859.14 |
| 323.15 | 0.3980 | 875.2 |
| 323.15 | 0.5010 | 889.85 |
| 323.15 | 0.5990 | 903.31 |
| 323.15 | 0.7030 | 916.62 |
| 323.15 | 0.8030 | 928.83 |
| 323.15 | 0.9040 | 940.66 |
| 323.15 | 0.9200 | 942.42 |
| 323.15 | 0.9460 | 945.33 |
| 323.15 | 0.9730 | 948.33 |
| 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 | 826.36 |
| 303.15 | 0.0000 | 822.88 |
| 308.15 | 0.0000 | 819.43 |
| 313.15 | 0.0000 | 815.97 |
| 318.15 | 0.0000 | 812.49 |
| 323.15 | 0.0000 | 809.03 |
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 | 835.9 |
| 0.0999 | 845.2 |
| 0.2008 | 862.8 |
| 0.3001 | 879.1 |
| 0.4004 | 894.7 |
| 0.4996 | 909.3 |
| 0.6007 | 923.4 |
| 0.6981 | 936.3 |
| 0.7985 | 949.0 |
| 0.9003 | 961.2 |
| 0.9505 | 967.0 |
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 | 1380.0 |
| 298.15 | 0.0190 | 1375.0 |
| 298.15 | 0.0400 | 1370.0 |
| 298.15 | 0.0630 | 1365.0 |
| 298.15 | 0.0990 | 1358.0 |
| 298.15 | 0.2000 | 1340.0 |
| 298.15 | 0.2920 | 1325.0 |
| 298.15 | 0.3980 | 1311.0 |
| 298.15 | 0.5010 | 1298.0 |
| 298.15 | 0.5990 | 1289.0 |
| 298.15 | 0.7030 | 1281.0 |
| 298.15 | 0.8030 | 1274.0 |
| 298.15 | 0.9040 | 1269.0 |
| 298.15 | 0.9200 | 1268.0 |
| 298.15 | 0.9460 | 1267.0 |
| 298.15 | 0.9730 | 1266.0 |
| 298.15 | 1.0000 | 1265.0 |
| 303.15 | 0.0000 | 1363.0 |
| 303.15 | 0.0190 | 1358.0 |
| 303.15 | 0.0400 | 1353.0 |
| 303.15 | 0.0630 | 1348.0 |
| 303.15 | 0.0990 | 1341.0 |
| 303.15 | 0.2000 | 1323.0 |
| 303.15 | 0.2920 | 1308.0 |
| 303.15 | 0.3980 | 1294.0 |
| 303.15 | 0.5010 | 1281.0 |
| 303.15 | 0.5990 | 1273.0 |
| 303.15 | 0.7030 | 1264.0 |
| 303.15 | 0.8030 | 1257.0 |
| 303.15 | 0.9040 | 1252.0 |
| 303.15 | 0.9200 | 1251.0 |
| 303.15 | 0.9460 | 1250.0 |
| 303.15 | 0.9730 | 1249.0 |
| 303.15 | 1.0000 | 1248.0 |
| 308.15 | 0.0000 | 1346.0 |
| 308.15 | 0.0190 | 1341.0 |
| 308.15 | 0.0400 | 1336.0 |
| 308.15 | 0.0630 | 1331.0 |
| 308.15 | 0.0990 | 1324.0 |
| 308.15 | 0.2000 | 1306.0 |
| 308.15 | 0.2920 | 1292.0 |
| 308.15 | 0.3980 | 1277.0 |
| 308.15 | 0.5010 | 1264.0 |
| 308.15 | 0.5990 | 1256.0 |
| 308.15 | 0.7030 | 1247.0 |
| 308.15 | 0.8030 | 1241.0 |
| 308.15 | 0.9040 | 1236.0 |
| 308.15 | 0.9200 | 1234.0 |
| 308.15 | 0.9460 | 1233.0 |
| 308.15 | 0.9730 | 1232.0 |
| 308.15 | 1.0000 | 1231.0 |
| 313.15 | 0.0000 | 1329.0 |
| 313.15 | 0.0190 | 1324.0 |
| 313.15 | 0.0400 | 1319.0 |
| 313.15 | 0.0630 | 1314.0 |
| 313.15 | 0.0990 | 1307.0 |
| 313.15 | 0.2000 | 1289.0 |
| 313.15 | 0.2920 | 1275.0 |
| 313.15 | 0.3980 | 1260.0 |
| 313.15 | 0.5010 | 1248.0 |
| 313.15 | 0.5990 | 1239.0 |
| 313.15 | 0.7030 | 1231.0 |
| 313.15 | 0.8030 | 1224.0 |
| 313.15 | 0.9040 | 1219.0 |
| 313.15 | 0.9200 | 1218.0 |
| 313.15 | 0.9460 | 1216.0 |
| 313.15 | 0.9730 | 1215.0 |
| 313.15 | 1.0000 | 1214.0 |
| 318.15 | 0.0000 | 1312.0 |
| 318.15 | 0.0190 | 1307.0 |
| 318.15 | 0.0400 | 1303.0 |
| 318.15 | 0.0630 | 1298.0 |
| 318.15 | 0.0990 | 1291.0 |
| 318.15 | 0.2000 | 1273.0 |
| 318.15 | 0.2920 | 1258.0 |
| 318.15 | 0.3980 | 1244.0 |
| 318.15 | 0.5010 | 1231.0 |
| 318.15 | 0.5990 | 1223.0 |
| 318.15 | 0.7030 | 1214.0 |
| 318.15 | 0.8030 | 1207.0 |
| 318.15 | 0.9040 | 1202.0 |
| 318.15 | 0.9200 | 1201.0 |
| 318.15 | 0.9460 | 1200.0 |
| 318.15 | 0.9730 | 1199.0 |
| 318.15 | 1.0000 | 1198.0 |
| 323.15 | 0.0000 | 1296.0 |
| 323.15 | 0.0190 | 1291.0 |
| 323.15 | 0.0400 | 1286.0 |
| 323.15 | 0.0630 | 1281.0 |
| 323.15 | 0.0990 | 1274.0 |
| 323.15 | 0.2000 | 1256.0 |
| 323.15 | 0.2920 | 1242.0 |
| 323.15 | 0.3980 | 1227.0 |
| 323.15 | 0.5010 | 1215.0 |
| 323.15 | 0.5990 | 1206.0 |
| 323.15 | 0.7030 | 1198.0 |
| 323.15 | 0.8030 | 1191.0 |
| 323.15 | 0.9040 | 1186.0 |
| 323.15 | 0.9200 | 1185.0 |
| 323.15 | 0.9460 | 1183.0 |
| 323.15 | 0.9730 | 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 | 1380.0 |
| 298.15 | 0.0190 | 1375.0 |
| 298.15 | 0.0400 | 1370.0 |
| 298.15 | 0.0630 | 1365.0 |
| 298.15 | 0.0990 | 1358.0 |
| 298.15 | 0.2000 | 1340.0 |
| 298.15 | 0.2920 | 1325.0 |
| 298.15 | 0.3980 | 1311.0 |
| 298.15 | 0.5010 | 1298.0 |
| 298.15 | 0.5990 | 1289.0 |
| 298.15 | 0.7030 | 1281.0 |
| 298.15 | 0.8030 | 1274.0 |
| 298.15 | 0.9040 | 1269.0 |
| 298.15 | 0.9200 | 1268.0 |
| 298.15 | 0.9460 | 1267.0 |
| 298.15 | 0.9730 | 1266.0 |
| 298.15 | 1.0000 | 1265.0 |
| 303.15 | 0.0000 | 1363.0 |
| 303.15 | 0.0190 | 1358.0 |
| 303.15 | 0.0400 | 1353.0 |
| 303.15 | 0.0630 | 1348.0 |
| 303.15 | 0.0990 | 1341.0 |
| 303.15 | 0.2000 | 1323.0 |
| 303.15 | 0.2920 | 1308.0 |
| 303.15 | 0.3980 | 1294.0 |
| 303.15 | 0.5010 | 1281.0 |
| 303.15 | 0.5990 | 1273.0 |
| 303.15 | 0.7030 | 1264.0 |
| 303.15 | 0.8030 | 1257.0 |
| 303.15 | 0.9040 | 1252.0 |
| 303.15 | 0.9200 | 1251.0 |
| 303.15 | 0.9460 | 1250.0 |
| 303.15 | 0.9730 | 1249.0 |
| 303.15 | 1.0000 | 1248.0 |
| 308.15 | 0.0000 | 1346.0 |
| 308.15 | 0.0190 | 1341.0 |
| 308.15 | 0.0400 | 1336.0 |
| 308.15 | 0.0630 | 1331.0 |
| 308.15 | 0.0990 | 1324.0 |
| 308.15 | 0.2000 | 1306.0 |
| 308.15 | 0.2920 | 1292.0 |
| 308.15 | 0.3980 | 1277.0 |
| 308.15 | 0.5010 | 1264.0 |
| 308.15 | 0.5990 | 1256.0 |
| 308.15 | 0.7030 | 1247.0 |
| 308.15 | 0.8030 | 1241.0 |
| 308.15 | 0.9040 | 1236.0 |
| 308.15 | 0.9200 | 1234.0 |
| 308.15 | 0.9460 | 1233.0 |
| 308.15 | 0.9730 | 1232.0 |
| 308.15 | 1.0000 | 1231.0 |
| 313.15 | 0.0000 | 1329.0 |
| 313.15 | 0.0190 | 1324.0 |
| 313.15 | 0.0400 | 1319.0 |
| 313.15 | 0.0630 | 1314.0 |
| 313.15 | 0.0990 | 1307.0 |
| 313.15 | 0.2000 | 1289.0 |
| 313.15 | 0.2920 | 1275.0 |
| 313.15 | 0.3980 | 1260.0 |
| 313.15 | 0.5010 | 1248.0 |
| 313.15 | 0.5990 | 1239.0 |
| 313.15 | 0.7030 | 1231.0 |
| 313.15 | 0.8030 | 1224.0 |
| 313.15 | 0.9040 | 1219.0 |
| 313.15 | 0.9200 | 1218.0 |
| 313.15 | 0.9460 | 1216.0 |
| 313.15 | 0.9730 | 1215.0 |
| 313.15 | 1.0000 | 1214.0 |
| 318.15 | 0.0000 | 1312.0 |
| 318.15 | 0.0190 | 1307.0 |
| 318.15 | 0.0400 | 1303.0 |
| 318.15 | 0.0630 | 1298.0 |
| 318.15 | 0.0990 | 1291.0 |
| 318.15 | 0.2000 | 1273.0 |
| 318.15 | 0.2920 | 1258.0 |
| 318.15 | 0.3980 | 1244.0 |
| 318.15 | 0.5010 | 1231.0 |
| 318.15 | 0.5990 | 1223.0 |
| 318.15 | 0.7030 | 1214.0 |
| 318.15 | 0.8030 | 1207.0 |
| 318.15 | 0.9040 | 1202.0 |
| 318.15 | 0.9200 | 1201.0 |
| 318.15 | 0.9460 | 1200.0 |
| 318.15 | 0.9730 | 1199.0 |
| 318.15 | 1.0000 | 1198.0 |
| 323.15 | 0.0000 | 1296.0 |
| 323.15 | 0.0190 | 1291.0 |
| 323.15 | 0.0400 | 1286.0 |
| 323.15 | 0.0630 | 1281.0 |
| 323.15 | 0.0990 | 1274.0 |
| 323.15 | 0.2000 | 1256.0 |
| 323.15 | 0.2920 | 1242.0 |
| 323.15 | 0.3980 | 1227.0 |
| 323.15 | 0.5010 | 1215.0 |
| 323.15 | 0.5990 | 1206.0 |
| 323.15 | 0.7030 | 1198.0 |
| 323.15 | 0.8030 | 1191.0 |
| 323.15 | 0.9040 | 1186.0 |
| 323.15 | 0.9200 | 1185.0 |
| 323.15 | 0.9460 | 1183.0 |
| 323.15 | 0.9730 | 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 | 280.19 |
| 0.0501 | 278.91 |
| 0.1000 | 278.30 |
| 0.2000 | 275.67 |
| 0.3000 | 272.78 |
| 0.4000 | 269.98 |
| 0.5000 | 263.71 |
| 0.6000 | 256.46 |
| 0.7001 | 247.24 |
| 0.8000 | 231.90 |
| 0.9000 | 206.31 |
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 |
|---|---|
| 0.9501 | 192.07 |
| 1.0000 | 194.31 |
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 | 280.19 |
| 0.0501 | 278.91 |
| 0.1000 | 278.30 |
| 0.2000 | 275.67 |
| 0.3000 | 272.78 |
| 0.4000 | 269.98 |
| 0.5000 | 263.71 |
| 0.6000 | 256.46 |
| 0.7001 | 247.24 |
| 0.8000 | 231.90 |
| 0.9000 | 206.31 |
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 |
|---|---|
| 0.9501 | 192.07 |
| 1.0000 | 194.31 |
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