Mixture of Diethyl carbonate + 1-Propanol + Water

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Diethyl carbonate

Name
Diethyl carbonate
InChI
InChI=1S/C5H10O3/c1-3-7-5(6)8-4-2/h3-4H2,1-2H3
InChI Key
OIFBSDVPJOWBCH-UHFFFAOYSA-N
Formula
C5H10O3
SMILES
CCOC(=O)OCC
Mol. Weight (g/mol)
118.13
CAS
105-58-8

1-Propanol

Name
1-Propanol
InChI
InChI=1S/C3H8O/c1-2-3-4/h4H,2-3H2,1H3
InChI Key
BDERNNFJNOPAEC-UHFFFAOYSA-N
Formula
C3H8O
SMILES
CCCO
Mol. Weight (g/mol)
60.09
CAS
71-23-8

Water

Name
Water
InChI
InChI=1S/H2O/h1H2
InChI Key
XLYOFNOQVPJJNP-UHFFFAOYSA-N
Formula
H2O
SMILES
O
Mol. Weight (g/mol)
18.02
CAS
7732-18-5
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Datasets

  1. Temperature, K x Mole fraction (6)

Temperature, K x Mole fraction [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 2)

Fixed Measured
Temperature, K - Liquid mixture 1 Mole fraction of Water (3) - Liquid mixture 2 Mole fraction of 1-Propanol (2) - Liquid mixture 2 Mole fraction of 1-Propanol (2) - Liquid mixture 1 Mole fraction of Water (3) - Liquid mixture 1
293.15 0.9974 0.0000 0.0000 0.0539
308.15 0.9622 0.0336 0.2651 0.3490
308.15 0.9888 0.0081 0.0453 0.1109
298.15 0.9779 0.0192 0.1102 0.1222
308.15 0.9812 0.0156 0.0956 0.1334
308.15 0.9754 0.0212 0.1464 0.1746
308.15 0.9710 0.0254 0.1840 0.2364
293.15 0.9786 0.0179 0.0783 0.1028
308.15 0.9681 0.0281 0.2206 0.2742
308.15 0.9974 0.0000 0.0000 0.0857
313.15 0.9661 0.0291 0.2428 0.3159
303.15 0.9762 0.0207 0.1363 0.1657
313.15 0.9628 0.0318 0.2630 0.3559
313.15 0.9972 0.0000 0.0000 0.0928
313.15 0.9893 0.0074 0.0483 0.1169
298.15 0.9699 0.0265 0.1787 0.2004
313.15 0.9834 0.0131 0.0968 0.1322
313.15 0.9771 0.0191 0.1485 0.1796
313.15 0.9730 0.0228 0.1882 0.2338
313.15 0.9693 0.0262 0.2226 0.2805
293.15 0.9717 0.0247 0.1257 0.1409
293.15 0.9664 0.0302 0.1747 0.1882
303.15 0.9895 0.0080 0.0413 0.1019
293.15 0.9618 0.0348 0.2085 0.2298
293.15 0.9577 0.0385 0.2381 0.2802
293.15 0.9543 0.0417 0.2583 0.3194
298.15 0.9892 0.0082 0.0385 0.0785
298.15 0.9637 0.0325 0.2301 0.2659
298.15 0.9606 0.0360 0.2656 0.3231
298.15 0.9573 0.0395 0.2852 0.3842
298.15 0.9975 0.0000 0.0000 0.0601
303.15 0.9603 0.0358 0.2631 0.3418
303.15 0.9821 0.0151 0.0869 0.1238
293.15 0.9876 0.0094 0.0321 0.0760
303.15 0.9708 0.0257 0.1818 0.2150
303.15 0.9670 0.0293 0.2168 0.2583
303.15 0.9975 0.0000 0.0000 0.0778
303.15 0.9634 0.0328 0.2416 0.2990
308.15 0.9651 0.0309 0.2429 0.3100

Mole fraction [ref]

Operational conditions:

Fixed Measured
Mole fraction of 1-Propanol (2) - Liquid mixture 2 Mole fraction of Diethyl carbonate (1) - Liquid mixture 2 Mole fraction of 1-Propanol (2) - Liquid mixture 1 Mole fraction of Diethyl carbonate (1) - Liquid mixture 1
0.0463 0.0041 0.3104 0.2286
0.0418 0.0040 0.2917 0.3078
0.0381 0.0039 0.2677 0.3827
0.0315 0.0037 0.2178 0.5214
0.0235 0.0033 0.1501 0.6682
0.0116 0.0027 0.0752 0.8077
0.0000 0.0025 0.0000 0.9216

Temperature, K x Mole fraction [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid mixture 2)

Fixed Measured
Temperature, K - Liquid mixture 1 Mole fraction of 1-Propanol (2) - Liquid mixture 2 Mole fraction of Diethyl carbonate (1) - Liquid mixture 2 Mole fraction of 1-Propanol (2) - Liquid mixture 1 Mole fraction of Diethyl carbonate (1) - Liquid mixture 1
303.15 0.0566 0.0053 0.1815 0.0437
323.15 0.0319 0.0028 0.2680 0.3583
323.15 0.0267 0.0024 0.2233 0.4729
313.15 0.0310 0.0029 0.2826 0.3145
323.15 0.0226 0.0025 0.1795 0.5902
323.15 0.0170 0.0028 0.1183 0.7086
323.15 0.0071 0.0017 0.0607 0.8079
303.15 0.0093 0.0017 0.0549 0.8398
323.15 0.0000 0.0011 0.0000 0.8982
333.15 0.0441 0.0048 0.1925 0.0602
333.15 0.0390 0.0038 0.2346 0.1081
323.15 0.0606 0.0078 0.1532 0.0337
333.15 0.0362 0.0033 0.2567 0.1569
303.15 0.0387 0.0029 0.2787 0.1846
333.15 0.0342 0.0031 0.2726 0.2209
313.15 0.0319 0.0027 0.2688 0.3652
333.15 0.0304 0.0033 0.2738 0.2830
333.15 0.0313 0.0029 0.2640 0.3422
333.15 0.0238 0.0024 0.2245 0.4637
333.15 0.0188 0.0022 0.1737 0.5890
303.15 0.0000 0.0027 0.0000 0.9155
333.15 0.0140 0.0020 0.1199 0.6951
323.15 0.0436 0.0042 0.2168 0.0734
333.15 0.0061 0.0018 0.0592 0.7943
333.15 0.0000 0.0021 0.0000 0.8776
303.15 0.0361 0.0032 0.2899 0.2575
303.15 0.0320 0.0027 0.2827 0.3280
303.15 0.0457 0.0040 0.2321 0.0805
303.15 0.0336 0.0026 0.2684 0.3815
303.15 0.0315 0.0024 0.2243 0.5084
303.15 0.0253 0.0023 0.1666 0.6403
313.15 0.0530 0.0059 0.1765 0.0414
313.15 0.0440 0.0042 0.2208 0.0735
303.15 0.0211 0.0025 0.1122 0.7431
313.15 0.0394 0.0034 0.2555 0.1253
313.15 0.0372 0.0030 0.2759 0.1769
313.15 0.0355 0.0029 0.2900 0.2514
313.15 0.0299 0.0026 0.2270 0.4837
313.15 0.0226 0.0022 0.1759 0.6081
313.15 0.0178 0.0030 0.1181 0.7181
313.15 0.0076 0.0020 0.0589 0.8218
313.15 0.0000 0.0022 0.0000 0.9153
323.15 0.0394 0.0037 0.2441 0.1155
323.15 0.0358 0.0030 0.2644 0.1657
323.15 0.0339 0.0028 0.2823 0.2371
303.15 0.0411 0.0032 0.2589 0.1289
323.15 0.0310 0.0032 0.2796 0.3022

Temperature, K x Mole fraction [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 2)

Fixed Measured
Temperature, K - Liquid mixture 1 Mole fraction of Water (3) - Liquid mixture 2 Mole fraction of 1-Propanol (2) - Liquid mixture 2 Mole fraction of 1-Propanol (2) - Liquid mixture 1 Mole fraction of Water (3) - Liquid mixture 1
293.15 0.9974 0.0000 0.0000 0.0539
308.15 0.9622 0.0336 0.2651 0.3490
308.15 0.9888 0.0081 0.0453 0.1109
298.15 0.9779 0.0192 0.1102 0.1222
308.15 0.9812 0.0156 0.0956 0.1334
308.15 0.9754 0.0212 0.1464 0.1746
308.15 0.9710 0.0254 0.1840 0.2364
293.15 0.9786 0.0179 0.0783 0.1028
308.15 0.9681 0.0281 0.2206 0.2742
308.15 0.9974 0.0000 0.0000 0.0857
313.15 0.9661 0.0291 0.2428 0.3159
303.15 0.9762 0.0207 0.1363 0.1657
313.15 0.9628 0.0318 0.2630 0.3559
313.15 0.9972 0.0000 0.0000 0.0928
313.15 0.9893 0.0074 0.0483 0.1169
298.15 0.9699 0.0265 0.1787 0.2004
313.15 0.9834 0.0131 0.0968 0.1322
313.15 0.9771 0.0191 0.1485 0.1796
313.15 0.9730 0.0228 0.1882 0.2338
313.15 0.9693 0.0262 0.2226 0.2805
293.15 0.9717 0.0247 0.1257 0.1409
293.15 0.9664 0.0302 0.1747 0.1882
303.15 0.9895 0.0080 0.0413 0.1019
293.15 0.9618 0.0348 0.2085 0.2298
293.15 0.9577 0.0385 0.2381 0.2802
293.15 0.9543 0.0417 0.2583 0.3194
298.15 0.9892 0.0082 0.0385 0.0785
298.15 0.9637 0.0325 0.2301 0.2659
298.15 0.9606 0.0360 0.2656 0.3231
298.15 0.9573 0.0395 0.2852 0.3842
298.15 0.9975 0.0000 0.0000 0.0601
303.15 0.9603 0.0358 0.2631 0.3418
303.15 0.9821 0.0151 0.0869 0.1238
293.15 0.9876 0.0094 0.0321 0.0760
303.15 0.9708 0.0257 0.1818 0.2150
303.15 0.9670 0.0293 0.2168 0.2583
303.15 0.9975 0.0000 0.0000 0.0778
303.15 0.9634 0.0328 0.2416 0.2990
308.15 0.9651 0.0309 0.2429 0.3100

Mole fraction [ref]

Operational conditions:

Fixed Measured
Mole fraction of 1-Propanol (2) - Liquid mixture 2 Mole fraction of Diethyl carbonate (1) - Liquid mixture 2 Mole fraction of 1-Propanol (2) - Liquid mixture 1 Mole fraction of Diethyl carbonate (1) - Liquid mixture 1
0.0463 0.0041 0.3104 0.2286
0.0418 0.0040 0.2917 0.3078
0.0381 0.0039 0.2677 0.3827
0.0315 0.0037 0.2178 0.5214
0.0235 0.0033 0.1501 0.6682
0.0116 0.0027 0.0752 0.8077
0.0000 0.0025 0.0000 0.9216

Temperature, K x Mole fraction [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid mixture 2)

Fixed Measured
Temperature, K - Liquid mixture 1 Mole fraction of 1-Propanol (2) - Liquid mixture 2 Mole fraction of Diethyl carbonate (1) - Liquid mixture 2 Mole fraction of 1-Propanol (2) - Liquid mixture 1 Mole fraction of Diethyl carbonate (1) - Liquid mixture 1
303.15 0.0566 0.0053 0.1815 0.0437
323.15 0.0319 0.0028 0.2680 0.3583
323.15 0.0267 0.0024 0.2233 0.4729
313.15 0.0310 0.0029 0.2826 0.3145
323.15 0.0226 0.0025 0.1795 0.5902
323.15 0.0170 0.0028 0.1183 0.7086
323.15 0.0071 0.0017 0.0607 0.8079
303.15 0.0093 0.0017 0.0549 0.8398
323.15 0.0000 0.0011 0.0000 0.8982
333.15 0.0441 0.0048 0.1925 0.0602
333.15 0.0390 0.0038 0.2346 0.1081
323.15 0.0606 0.0078 0.1532 0.0337
333.15 0.0362 0.0033 0.2567 0.1569
303.15 0.0387 0.0029 0.2787 0.1846
333.15 0.0342 0.0031 0.2726 0.2209
313.15 0.0319 0.0027 0.2688 0.3652
333.15 0.0304 0.0033 0.2738 0.2830
333.15 0.0313 0.0029 0.2640 0.3422
333.15 0.0238 0.0024 0.2245 0.4637
333.15 0.0188 0.0022 0.1737 0.5890
303.15 0.0000 0.0027 0.0000 0.9155
333.15 0.0140 0.0020 0.1199 0.6951
323.15 0.0436 0.0042 0.2168 0.0734
333.15 0.0061 0.0018 0.0592 0.7943
333.15 0.0000 0.0021 0.0000 0.8776
303.15 0.0361 0.0032 0.2899 0.2575
303.15 0.0320 0.0027 0.2827 0.3280
303.15 0.0457 0.0040 0.2321 0.0805
303.15 0.0336 0.0026 0.2684 0.3815
303.15 0.0315 0.0024 0.2243 0.5084
303.15 0.0253 0.0023 0.1666 0.6403
313.15 0.0530 0.0059 0.1765 0.0414
313.15 0.0440 0.0042 0.2208 0.0735
303.15 0.0211 0.0025 0.1122 0.7431
313.15 0.0394 0.0034 0.2555 0.1253
313.15 0.0372 0.0030 0.2759 0.1769
313.15 0.0355 0.0029 0.2900 0.2514
313.15 0.0299 0.0026 0.2270 0.4837
313.15 0.0226 0.0022 0.1759 0.6081
313.15 0.0178 0.0030 0.1181 0.7181
313.15 0.0076 0.0020 0.0589 0.8218
313.15 0.0000 0.0022 0.0000 0.9153
323.15 0.0394 0.0037 0.2441 0.1155
323.15 0.0358 0.0030 0.2644 0.1657
323.15 0.0339 0.0028 0.2823 0.2371
303.15 0.0411 0.0032 0.2589 0.1289
323.15 0.0310 0.0032 0.2796 0.3022

Sources