Operational condition: Pressure, kPa = 101.3 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Ethanol, 2-ethoxy- (1) - Liquid | Viscosity, Pa*s - Liquid |
303.15 | 0.0000 | 0.0008 |
303.15 | 0.0201 | 0.0010 |
303.15 | 0.0442 | 0.0014 |
303.15 | 0.0734 | 0.0017 |
303.15 | 0.1098 | 0.0021 |
303.15 | 0.1561 | 0.0025 |
303.15 | 0.2172 | 0.0027 |
303.15 | 0.3015 | 0.0029 |
303.15 | 0.4252 | 0.0027 |
303.15 | 0.6247 | 0.0023 |
303.15 | 1.0000 | 0.0016 |
308.15 | 0.0000 | 0.0007 |
308.15 | 0.0201 | 0.0009 |
308.15 | 0.0442 | 0.0012 |
308.15 | 0.0734 | 0.0015 |
308.15 | 0.1098 | 0.0018 |
308.15 | 0.1561 | 0.0021 |
308.15 | 0.2172 | 0.0022 |
308.15 | 0.3015 | 0.0023 |
308.15 | 0.4252 | 0.0022 |
308.15 | 0.6247 | 0.0020 |
308.15 | 1.0000 | 0.0014 |
313.15 | 0.0000 | 0.0007 |
313.15 | 0.0201 | 0.0008 |
313.15 | 0.0442 | 0.0010 |
313.15 | 0.0734 | 0.0012 |
313.15 | 0.1098 | 0.0015 |
313.15 | 0.1561 | 0.0017 |
313.15 | 0.2172 | 0.0019 |
313.15 | 0.3015 | 0.0019 |
313.15 | 0.4252 | 0.0019 |
313.15 | 0.6247 | 0.0017 |
313.15 | 1.0000 | 0.0012 |
318.15 | 0.0000 | 0.0006 |
318.15 | 0.0201 | 0.0007 |
318.15 | 0.0442 | 0.0009 |
318.15 | 0.0734 | 0.0011 |
318.15 | 0.1098 | 0.0013 |
318.15 | 0.1561 | 0.0015 |
318.15 | 0.2172 | 0.0017 |
318.15 | 0.3015 | 0.0017 |
318.15 | 0.4252 | 0.0016 |
318.15 | 0.6247 | 0.0015 |
318.15 | 1.0000 | 0.0012 |
323.15 | 0.0000 | 0.0005 |
323.15 | 0.0201 | 0.0007 |
323.15 | 0.0442 | 0.0008 |
323.15 | 0.0734 | 0.0010 |
323.15 | 0.1098 | 0.0012 |
323.15 | 0.1561 | 0.0013 |
323.15 | 0.2172 | 0.0014 |
323.15 | 0.3015 | 0.0015 |
323.15 | 0.4252 | 0.0015 |
323.15 | 0.6247 | 0.0014 |
323.15 | 1.0000 | 0.0010 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Molality, mol/kg of Ethanol, 2-ethoxy- (1) - Liquid | Viscosity, Pa*s - Liquid |
275.15 | 0.0000 | 0.0017 |
275.15 | 0.0102 | 0.0010 |
275.15 | 0.0202 | 0.0010 |
275.15 | 0.0294 | 0.0010 |
275.15 | 0.0459 | 0.0010 |
275.15 | 0.0502 | 0.0010 |
275.15 | 0.0602 | 0.0010 |
275.15 | 0.0710 | 0.0010 |
275.15 | 0.0818 | 0.0010 |
275.15 | 0.0902 | 0.0011 |
275.15 | 0.1008 | 0.0011 |
283.15 | 0.0000 | 0.0013 |
283.15 | 0.0067 | 0.0010 |
283.15 | 0.0191 | 0.0010 |
283.15 | 0.0303 | 0.0010 |
283.15 | 0.0392 | 0.0010 |
283.15 | 0.0492 | 0.0010 |
283.15 | 0.0598 | 0.0010 |
283.15 | 0.0682 | 0.0010 |
283.15 | 0.0799 | 0.0010 |
283.15 | 0.0885 | 0.0010 |
283.15 | 0.0906 | 0.0010 |
283.15 | 0.0996 | 0.0010 |
283.15 | 0.1004 | 0.0010 |
Operational conditions:
Mole fraction of Ethanol, 2-ethoxy- (1) - Liquid | Viscosity, Pa*s - Liquid |
---|---|
0.0109 | 0.0011 |
0.0249 | 0.0013 |
0.0499 | 0.0018 |
0.0750 | 0.0022 |
0.1007 | 0.0026 |
0.1486 | 0.0032 |
0.2030 | 0.0035 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Ethanol, 2-ethoxy- (1) - Liquid | Viscosity, Pa*s - Liquid |
303.15 | 0.0000 | 0.0008 |
303.15 | 0.0201 | 0.0010 |
303.15 | 0.0442 | 0.0014 |
303.15 | 0.0734 | 0.0017 |
303.15 | 0.1098 | 0.0021 |
303.15 | 0.1561 | 0.0025 |
303.15 | 0.2172 | 0.0027 |
303.15 | 0.3015 | 0.0029 |
303.15 | 0.4252 | 0.0027 |
303.15 | 0.6247 | 0.0023 |
303.15 | 1.0000 | 0.0016 |
308.15 | 0.0000 | 0.0007 |
308.15 | 0.0201 | 0.0009 |
308.15 | 0.0442 | 0.0012 |
308.15 | 0.0734 | 0.0015 |
308.15 | 0.1098 | 0.0018 |
308.15 | 0.1561 | 0.0021 |
308.15 | 0.2172 | 0.0022 |
308.15 | 0.3015 | 0.0023 |
308.15 | 0.4252 | 0.0022 |
308.15 | 0.6247 | 0.0020 |
308.15 | 1.0000 | 0.0014 |
313.15 | 0.0000 | 0.0007 |
313.15 | 0.0201 | 0.0008 |
313.15 | 0.0442 | 0.0010 |
313.15 | 0.0734 | 0.0012 |
313.15 | 0.1098 | 0.0015 |
313.15 | 0.1561 | 0.0017 |
313.15 | 0.2172 | 0.0019 |
313.15 | 0.3015 | 0.0019 |
313.15 | 0.4252 | 0.0019 |
313.15 | 0.6247 | 0.0017 |
313.15 | 1.0000 | 0.0012 |
318.15 | 0.0000 | 0.0006 |
318.15 | 0.0201 | 0.0007 |
318.15 | 0.0442 | 0.0009 |
318.15 | 0.0734 | 0.0011 |
318.15 | 0.1098 | 0.0013 |
318.15 | 0.1561 | 0.0015 |
318.15 | 0.2172 | 0.0017 |
318.15 | 0.3015 | 0.0017 |
318.15 | 0.4252 | 0.0016 |
318.15 | 0.6247 | 0.0015 |
318.15 | 1.0000 | 0.0012 |
323.15 | 0.0000 | 0.0005 |
323.15 | 0.0201 | 0.0007 |
323.15 | 0.0442 | 0.0008 |
323.15 | 0.0734 | 0.0010 |
323.15 | 0.1098 | 0.0012 |
323.15 | 0.1561 | 0.0013 |
323.15 | 0.2172 | 0.0014 |
323.15 | 0.3015 | 0.0015 |
323.15 | 0.4252 | 0.0015 |
323.15 | 0.6247 | 0.0014 |
323.15 | 1.0000 | 0.0010 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Molality, mol/kg of Ethanol, 2-ethoxy- (1) - Liquid | Viscosity, Pa*s - Liquid |
275.15 | 0.0000 | 0.0017 |
275.15 | 0.0102 | 0.0010 |
275.15 | 0.0202 | 0.0010 |
275.15 | 0.0294 | 0.0010 |
275.15 | 0.0459 | 0.0010 |
275.15 | 0.0502 | 0.0010 |
275.15 | 0.0602 | 0.0010 |
275.15 | 0.0710 | 0.0010 |
275.15 | 0.0818 | 0.0010 |
275.15 | 0.0902 | 0.0011 |
275.15 | 0.1008 | 0.0011 |
283.15 | 0.0000 | 0.0013 |
283.15 | 0.0067 | 0.0010 |
283.15 | 0.0191 | 0.0010 |
283.15 | 0.0303 | 0.0010 |
283.15 | 0.0392 | 0.0010 |
283.15 | 0.0492 | 0.0010 |
283.15 | 0.0598 | 0.0010 |
283.15 | 0.0682 | 0.0010 |
283.15 | 0.0799 | 0.0010 |
283.15 | 0.0885 | 0.0010 |
283.15 | 0.0906 | 0.0010 |
283.15 | 0.0996 | 0.0010 |
283.15 | 0.1004 | 0.0010 |
Operational conditions:
Mole fraction of Ethanol, 2-ethoxy- (1) - Liquid | Viscosity, Pa*s - Liquid |
---|---|
0.0109 | 0.0011 |
0.0249 | 0.0013 |
0.0499 | 0.0018 |
0.0750 | 0.0022 |
0.1007 | 0.0026 |
0.1486 | 0.0032 |
0.2030 | 0.0035 |
Operational conditions:
Mole fraction of Ethanol, 2-ethoxy- (1) - Liquid | Refractive index (Na D-line) - Liquid |
---|---|
0.0000 | 1.3325 |
0.0092 | 1.3389 |
0.0177 | 1.3415 |
0.0250 | 1.3442 |
0.0502 | 1.3542 |
0.0767 | 1.3628 |
0.1024 | 1.3709 |
0.1830 | 1.3854 |
0.2990 | 1.394 |
0.4058 | 1.3979 |
0.5059 | 1.4012 |
0.5996 | 1.4025 |
0.7060 | 1.4039 |
0.8431 | 1.4046 |
0.8716 | 1.4049 |
1.0000 | 1.4058 |
Operational conditions:
Mole fraction of Ethanol, 2-ethoxy- (1) - Liquid | Refractive index (Na D-line) - Liquid |
---|---|
0.0000 | 1.3325 |
0.0092 | 1.3389 |
0.0177 | 1.3415 |
0.0250 | 1.3442 |
0.0502 | 1.3542 |
0.0767 | 1.3628 |
0.1024 | 1.3709 |
0.1830 | 1.3854 |
0.2990 | 1.394 |
0.4058 | 1.3979 |
0.5059 | 1.4012 |
0.5996 | 1.4025 |
0.7060 | 1.4039 |
0.8431 | 1.4046 |
0.8716 | 1.4049 |
1.0000 | 1.4058 |
Operational conditions:
Mole fraction of Ethanol, 2-ethoxy- (1) - Liquid | Mass density, kg/m3 - Liquid |
---|---|
0.0000 | 999.704 |
0.0092 | 996.93 |
0.0177 | 997.02 |
0.0250 | 997.2 |
0.0502 | 998.06 |
0.0767 | 998.24 |
0.1024 | 996.67 |
0.1830 | 988.37 |
0.2990 | 974.41 |
0.4058 | 963.11 |
0.5059 | 954.22 |
0.5996 | 947.01 |
0.7060 | 940.07 |
0.8431 | 933.47 |
0.8716 | 932.35 |
1.0000 | 925.39 |
Operational conditions:
Molality, mol/kg of Ethanol, 2-ethoxy- (1) - Liquid | Mass density, kg/m3 - Liquid |
---|---|
0.0000 | 999.94 |
0.0102 | 999.95 |
0.0202 | 999.95 |
0.0294 | 999.95 |
0.0459 | 999.96 |
0.0502 | 999.96 |
0.0602 | 999.97 |
0.0710 | 1000.0 |
0.0818 | 1000.0 |
0.0902 | 1000.01 |
0.1008 | 1000.03 |
Operational conditions:
Molality, mol/kg of Ethanol, 2-ethoxy- (1) - Liquid | Mass density, kg/m3 - Liquid |
---|---|
0.0000 | 999.7 |
0.0067 | 999.7 |
0.0191 | 999.71 |
0.0303 | 999.71 |
0.0392 | 999.74 |
0.0492 | 999.72 |
0.0598 | 999.72 |
0.0682 | 999.73 |
0.0799 | 999.73 |
0.0885 | 999.73 |
0.0906 | 999.73 |
0.0996 | 999.76 |
0.1004 | 999.78 |
Operational condition: Pressure, kPa = 100 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Ethanol, 2-ethoxy- (1) - Liquid | Mass density, kg/m3 - Liquid |
283.15 | 0.9426 | 943.675 |
288.15 | 0.9426 | 939.208 |
293.15 | 0.9426 | 934.713 |
298.15 | 0.9426 | 930.19 |
303.15 | 0.9426 | 925.638 |
308.15 | 0.9426 | 921.054 |
313.15 | 0.9426 | 916.435 |
323.15 | 0.9426 | 907.087 |
333.15 | 0.9426 | 897.58 |
343.15 | 0.9426 | 887.911 |
283.15 | 0.9490 | 943.444 |
288.15 | 0.9490 | 938.975 |
293.15 | 0.9490 | 934.479 |
298.15 | 0.9490 | 929.953 |
303.15 | 0.9490 | 925.399 |
308.15 | 0.9490 | 920.815 |
313.15 | 0.9490 | 916.194 |
323.15 | 0.9490 | 906.839 |
333.15 | 0.9490 | 897.329 |
343.15 | 0.9490 | 887.628 |
283.15 | 0.9549 | 943.15 |
288.15 | 0.9549 | 938.68 |
293.15 | 0.9549 | 934.183 |
298.15 | 0.9549 | 929.657 |
303.15 | 0.9549 | 925.102 |
308.15 | 0.9549 | 920.517 |
313.15 | 0.9549 | 915.892 |
323.15 | 0.9549 | 906.54 |
333.15 | 0.9549 | 897.036 |
343.15 | 0.9549 | 887.337 |
283.15 | 0.9567 | 943.112 |
288.15 | 0.9567 | 938.638 |
293.15 | 0.9567 | 934.14 |
298.15 | 0.9567 | 929.614 |
303.15 | 0.9567 | 925.055 |
308.15 | 0.9567 | 920.467 |
313.15 | 0.9567 | 915.843 |
323.15 | 0.9567 | 906.493 |
333.15 | 0.9567 | 896.985 |
343.15 | 0.9567 | 887.297 |
283.15 | 0.9670 | 942.599 |
288.15 | 0.9670 | 938.12 |
293.15 | 0.9670 | 933.622 |
298.15 | 0.9670 | 929.099 |
303.15 | 0.9670 | 924.54 |
308.15 | 0.9670 | 919.951 |
313.15 | 0.9670 | 915.328 |
323.15 | 0.9670 | 905.969 |
333.15 | 0.9670 | 896.461 |
343.15 | 0.9670 | 886.774 |
Operational conditions:
Mole fraction of Ethanol, 2-ethoxy- (1) - Liquid | Mass density, kg/m3 - Liquid |
---|---|
0.0000 | 999.704 |
0.0092 | 996.93 |
0.0177 | 997.02 |
0.0250 | 997.2 |
0.0502 | 998.06 |
0.0767 | 998.24 |
0.1024 | 996.67 |
0.1830 | 988.37 |
0.2990 | 974.41 |
0.4058 | 963.11 |
0.5059 | 954.22 |
0.5996 | 947.01 |
0.7060 | 940.07 |
0.8431 | 933.47 |
0.8716 | 932.35 |
1.0000 | 925.39 |
Operational conditions:
Molality, mol/kg of Ethanol, 2-ethoxy- (1) - Liquid | Mass density, kg/m3 - Liquid |
---|---|
0.0000 | 999.94 |
0.0102 | 999.95 |
0.0202 | 999.95 |
0.0294 | 999.95 |
0.0459 | 999.96 |
0.0502 | 999.96 |
0.0602 | 999.97 |
0.0710 | 1000.0 |
0.0818 | 1000.0 |
0.0902 | 1000.01 |
0.1008 | 1000.03 |
Operational conditions:
Molality, mol/kg of Ethanol, 2-ethoxy- (1) - Liquid | Mass density, kg/m3 - Liquid |
---|---|
0.0000 | 999.7 |
0.0067 | 999.7 |
0.0191 | 999.71 |
0.0303 | 999.71 |
0.0392 | 999.74 |
0.0492 | 999.72 |
0.0598 | 999.72 |
0.0682 | 999.73 |
0.0799 | 999.73 |
0.0885 | 999.73 |
0.0906 | 999.73 |
0.0996 | 999.76 |
0.1004 | 999.78 |
Operational condition: Pressure, kPa = 100 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Ethanol, 2-ethoxy- (1) - Liquid | Mass density, kg/m3 - Liquid |
283.15 | 0.9426 | 943.675 |
288.15 | 0.9426 | 939.208 |
293.15 | 0.9426 | 934.713 |
298.15 | 0.9426 | 930.19 |
303.15 | 0.9426 | 925.638 |
308.15 | 0.9426 | 921.054 |
313.15 | 0.9426 | 916.435 |
323.15 | 0.9426 | 907.087 |
333.15 | 0.9426 | 897.58 |
343.15 | 0.9426 | 887.911 |
283.15 | 0.9490 | 943.444 |
288.15 | 0.9490 | 938.975 |
293.15 | 0.9490 | 934.479 |
298.15 | 0.9490 | 929.953 |
303.15 | 0.9490 | 925.399 |
308.15 | 0.9490 | 920.815 |
313.15 | 0.9490 | 916.194 |
323.15 | 0.9490 | 906.839 |
333.15 | 0.9490 | 897.329 |
343.15 | 0.9490 | 887.628 |
283.15 | 0.9549 | 943.15 |
288.15 | 0.9549 | 938.68 |
293.15 | 0.9549 | 934.183 |
298.15 | 0.9549 | 929.657 |
303.15 | 0.9549 | 925.102 |
308.15 | 0.9549 | 920.517 |
313.15 | 0.9549 | 915.892 |
323.15 | 0.9549 | 906.54 |
333.15 | 0.9549 | 897.036 |
343.15 | 0.9549 | 887.337 |
283.15 | 0.9567 | 943.112 |
288.15 | 0.9567 | 938.638 |
293.15 | 0.9567 | 934.14 |
298.15 | 0.9567 | 929.614 |
303.15 | 0.9567 | 925.055 |
308.15 | 0.9567 | 920.467 |
313.15 | 0.9567 | 915.843 |
323.15 | 0.9567 | 906.493 |
333.15 | 0.9567 | 896.985 |
343.15 | 0.9567 | 887.297 |
283.15 | 0.9670 | 942.599 |
288.15 | 0.9670 | 938.12 |
293.15 | 0.9670 | 933.622 |
298.15 | 0.9670 | 929.099 |
303.15 | 0.9670 | 924.54 |
308.15 | 0.9670 | 919.951 |
313.15 | 0.9670 | 915.328 |
323.15 | 0.9670 | 905.969 |
333.15 | 0.9670 | 896.461 |
343.15 | 0.9670 | 886.774 |
Operational conditions:
Mole fraction of Ethanol, 2-ethoxy- (1) - Liquid | Speed of sound, m/s - Liquid |
---|---|
0.0000 | 1496.6 |
0.0092 | 1541.3 |
0.0177 | 1553.1 |
0.0250 | 1575.6 |
0.0502 | 1626.9 |
0.0767 | 1649.6 |
0.1024 | 1646.5 |
0.1830 | 1567.6 |
0.2990 | 1517.4 |
0.4058 | 1458.1 |
0.5059 | 1415.2 |
0.5996 | 1385.7 |
0.7060 | 1359.6 |
0.8431 | 1330.4 |
0.8716 | 1325.6 |
1.0000 | 1302.5 |
Operational condition: Pressure, kPa = 100 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Ethanol, 2-ethoxy- (1) - Liquid | Speed of sound, m/s - Liquid |
283.15 | 0.9426 | 1364.0 |
288.15 | 0.9426 | 1346.2 |
293.15 | 0.9426 | 1328.3 |
298.15 | 0.9426 | 1310.5 |
303.15 | 0.9426 | 1292.8 |
308.15 | 0.9426 | 1275.0 |
313.15 | 0.9426 | 1257.4 |
323.15 | 0.9426 | 1222.2 |
333.15 | 0.9426 | 1187.1 |
343.15 | 0.9426 | 1152.0 |
283.15 | 0.9490 | 1365.8 |
288.15 | 0.9490 | 1347.5 |
293.15 | 0.9490 | 1329.2 |
298.15 | 0.9490 | 1311.1 |
303.15 | 0.9490 | 1293.0 |
308.15 | 0.9490 | 1275.3 |
313.15 | 0.9490 | 1257.6 |
323.15 | 0.9490 | 1222.2 |
333.15 | 0.9490 | 1186.9 |
343.15 | 0.9490 | 1151.1 |
283.15 | 0.9549 | 1366.2 |
288.15 | 0.9549 | 1347.9 |
293.15 | 0.9549 | 1329.6 |
298.15 | 0.9549 | 1311.3 |
303.15 | 0.9549 | 1293.2 |
308.15 | 0.9549 | 1275.2 |
313.15 | 0.9549 | 1256.6 |
323.15 | 0.9549 | 1220.3 |
333.15 | 0.9549 | 1185.1 |
343.15 | 0.9549 | 1150.1 |
283.15 | 0.9567 | 1366.8 |
288.15 | 0.9567 | 1348.4 |
293.15 | 0.9567 | 1330.2 |
298.15 | 0.9567 | 1311.8 |
303.15 | 0.9567 | 1292.6 |
308.15 | 0.9567 | 1274.3 |
313.15 | 0.9567 | 1256.1 |
323.15 | 0.9567 | 1220.2 |
333.15 | 0.9567 | 1184.9 |
343.15 | 0.9567 | 1149.8 |
283.15 | 0.9670 | 1361.6 |
288.15 | 0.9670 | 1343.5 |
293.15 | 0.9670 | 1325.6 |
298.15 | 0.9670 | 1307.8 |
303.15 | 0.9670 | 1289.8 |
308.15 | 0.9670 | 1272.0 |
313.15 | 0.9670 | 1254.3 |
323.15 | 0.9670 | 1218.9 |
333.15 | 0.9670 | 1183.7 |
343.15 | 0.9670 | 1148.6 |
Operational conditions:
Mole fraction of Ethanol, 2-ethoxy- (1) - Liquid | Speed of sound, m/s - Liquid |
---|---|
0.0000 | 1496.6 |
0.0092 | 1541.3 |
0.0177 | 1553.1 |
0.0250 | 1575.6 |
0.0502 | 1626.9 |
0.0767 | 1649.6 |
0.1024 | 1646.5 |
0.1830 | 1567.6 |
0.2990 | 1517.4 |
0.4058 | 1458.1 |
0.5059 | 1415.2 |
0.5996 | 1385.7 |
0.7060 | 1359.6 |
0.8431 | 1330.4 |
0.8716 | 1325.6 |
1.0000 | 1302.5 |
Operational condition: Pressure, kPa = 100 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Ethanol, 2-ethoxy- (1) - Liquid | Speed of sound, m/s - Liquid |
283.15 | 0.9426 | 1364.0 |
288.15 | 0.9426 | 1346.2 |
293.15 | 0.9426 | 1328.3 |
298.15 | 0.9426 | 1310.5 |
303.15 | 0.9426 | 1292.8 |
308.15 | 0.9426 | 1275.0 |
313.15 | 0.9426 | 1257.4 |
323.15 | 0.9426 | 1222.2 |
333.15 | 0.9426 | 1187.1 |
343.15 | 0.9426 | 1152.0 |
283.15 | 0.9490 | 1365.8 |
288.15 | 0.9490 | 1347.5 |
293.15 | 0.9490 | 1329.2 |
298.15 | 0.9490 | 1311.1 |
303.15 | 0.9490 | 1293.0 |
308.15 | 0.9490 | 1275.3 |
313.15 | 0.9490 | 1257.6 |
323.15 | 0.9490 | 1222.2 |
333.15 | 0.9490 | 1186.9 |
343.15 | 0.9490 | 1151.1 |
283.15 | 0.9549 | 1366.2 |
288.15 | 0.9549 | 1347.9 |
293.15 | 0.9549 | 1329.6 |
298.15 | 0.9549 | 1311.3 |
303.15 | 0.9549 | 1293.2 |
308.15 | 0.9549 | 1275.2 |
313.15 | 0.9549 | 1256.6 |
323.15 | 0.9549 | 1220.3 |
333.15 | 0.9549 | 1185.1 |
343.15 | 0.9549 | 1150.1 |
283.15 | 0.9567 | 1366.8 |
288.15 | 0.9567 | 1348.4 |
293.15 | 0.9567 | 1330.2 |
298.15 | 0.9567 | 1311.8 |
303.15 | 0.9567 | 1292.6 |
308.15 | 0.9567 | 1274.3 |
313.15 | 0.9567 | 1256.1 |
323.15 | 0.9567 | 1220.2 |
333.15 | 0.9567 | 1184.9 |
343.15 | 0.9567 | 1149.8 |
283.15 | 0.9670 | 1361.6 |
288.15 | 0.9670 | 1343.5 |
293.15 | 0.9670 | 1325.6 |
298.15 | 0.9670 | 1307.8 |
303.15 | 0.9670 | 1289.8 |
308.15 | 0.9670 | 1272.0 |
313.15 | 0.9670 | 1254.3 |
323.15 | 0.9670 | 1218.9 |
333.15 | 0.9670 | 1183.7 |
343.15 | 0.9670 | 1148.6 |