Mixture of Butane, decafluoro- + Dimethyl ether

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Butane, decafluoro-

Name
Butane, decafluoro-
InChI
InChI=1S/C4F10/c5-1(6,3(9,10)11)2(7,8)4(12,13)14
InChI Key
KAVGMUDTWQVPDF-UHFFFAOYSA-N
Formula
C4F10
SMILES
FC(F)(F)C(F)(F)C(F)(F)C(F)(F)F
Mol. Weight (g/mol)
238.03
CAS
355-25-9

Dimethyl ether

Name
Dimethyl ether
InChI
InChI=1S/C2H6O/c1-3-2/h1-2H3
InChI Key
LCGLNKUTAGEVQW-UHFFFAOYSA-N
Formula
C2H6O
SMILES
COC
Mol. Weight (g/mol)
46.07
CAS
115-10-6
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Datasets

  1. Azeotropic composition: mole fraction (6)
  2. Pvap - Vapor or sublimation pressure, kPa (2)

Azeotropic composition: mole fraction of Dimethyl ether (2) [ref]

Pressure, kPa - Liquid Azeotropic composition: mole fraction of Dimethyl ether (2) - Liquid
1060.00 0.7670
1530.00 0.7630
2110.00 0.7700
2820.00 0.7520
3310.00 0.7570

Azeotropic composition: mole fraction of Dimethyl ether (2) [ref]

Temperature, K - Liquid Azeotropic composition: mole fraction of Dimethyl ether (2) - Liquid
313.28 0.7670
328.16 0.7630
343.10 0.7700
357.12 0.7520
365.30 0.7570

Mole fraction of Dimethyl ether (2) [ref]

Fixed Measured
Mole fraction of Dimethyl ether (2) - Liquid Temperature, K - Liquid Mole fraction of Dimethyl ether (2) - Gas
0.0218 379.05 0.0360
0.0293 328.16 0.1187
0.0315 313.28 0.1509
0.0468 373.36 0.0822
0.0510 343.10 0.1510
0.0512 379.05 0.0784
0.0576 357.12 0.1352
0.0581 328.16 0.2090
0.0669 313.28 0.2716
0.0794 379.05 0.1131
0.0916 328.16 0.2869
0.0960 373.36 0.1553
0.1109 379.05 0.1465
0.1133 313.28 0.3681
0.1158 343.10 0.2850
0.1192 328.16 0.3411
0.1195 357.12 0.2417
0.1216 379.05 0.1578
0.1355 379.05 0.1695
0.1458 373.36 0.2176
0.1530 379.05 0.1806
0.1576 328.16 0.4029
0.1884 313.28 0.4788
0.1901 343.10 0.3884
0.1939 328.16 0.4475
0.1950 357.12 0.3407
0.1979 373.36 0.2712
0.2367 328.16 0.4934
0.2520 313.28 0.5538
0.2540 365.30 0.3674
0.2567 373.36 0.3180
0.2735 357.12 0.4241
0.2882 343.10 0.4860
0.2907 328.16 0.5371
0.3126 373.36 0.3510
0.3514 328.16 0.5814
0.3558 373.36 0.3619
0.3579 313.28 0.6235
0.3700 357.12 0.5083
0.3943 365.30 0.4856
0.4154 343.10 0.5791
0.4458 328.16 0.6331
0.4721 313.28 0.6750
0.4935 365.30 0.5586
0.5032 357.12 0.6001
0.5414 328.16 0.6782
0.6405 313.28 0.7293
0.6451 343.10 0.7066
0.6778 365.30 0.6988
0.7233 357.12 0.7385
0.7406 328.16 0.7570
0.7577 343.10 0.7623
0.7600 365.30 0.7666
0.8066 343.10 0.7886
0.8202 373.36 0.8080
0.8244 365.30 0.8069
0.8349 328.16 0.7984
0.8353 357.12 0.8105
0.8397 379.05 0.8363
0.8528 313.28 0.8026
0.8668 373.36 0.8459
0.8812 379.05 0.8635
0.8903 365.30 0.8594
0.9001 343.10 0.8513
0.9005 385.84 0.8991
0.9076 328.16 0.8447
0.9167 373.36 0.8910
0.9173 379.05 0.8959
0.9222 357.12 0.8822
0.9248 385.84 0.9123
0.9347 343.10 0.8857
0.9403 365.30 0.9084
0.9462 379.05 0.9258
0.9487 328.16 0.8887
0.9489 385.84 0.9347
0.9495 373.36 0.9294
0.9518 313.28 0.8825
0.9603 392.83 0.9575
0.9637 357.12 0.9330
0.9649 379.05 0.9482
0.9661 328.16 0.9166
0.9705 385.84 0.9591
0.9708 343.10 0.9352
0.9720 365.30 0.9502
0.9746 392.83 0.9683
0.9764 373.36 0.9606
0.9821 379.05 0.9700
0.9856 392.83 0.9812
0.9875 385.84 0.9814
0.9897 313.28 0.9655
0.9928 385.84 0.9890
0.9955 392.83 0.9937

Azeotropic composition: mole fraction of Dimethyl ether (2) [ref]

Pressure, kPa - Liquid Azeotropic composition: mole fraction of Dimethyl ether (2) - Liquid
1060.00 0.7670
1530.00 0.7630
2110.00 0.7700
2820.00 0.7520
3310.00 0.7570

Azeotropic composition: mole fraction of Dimethyl ether (2) [ref]

Temperature, K - Liquid Azeotropic composition: mole fraction of Dimethyl ether (2) - Liquid
313.28 0.7670
328.16 0.7630
343.10 0.7700
357.12 0.7520
365.30 0.7570

Mole fraction of Dimethyl ether (2) [ref]

Fixed Measured
Mole fraction of Dimethyl ether (2) - Liquid Temperature, K - Liquid Mole fraction of Dimethyl ether (2) - Gas
0.0218 379.05 0.0360
0.0293 328.16 0.1187
0.0315 313.28 0.1509
0.0468 373.36 0.0822
0.0510 343.10 0.1510
0.0512 379.05 0.0784
0.0576 357.12 0.1352
0.0581 328.16 0.2090
0.0669 313.28 0.2716
0.0794 379.05 0.1131
0.0916 328.16 0.2869
0.0960 373.36 0.1553
0.1109 379.05 0.1465
0.1133 313.28 0.3681
0.1158 343.10 0.2850
0.1192 328.16 0.3411
0.1195 357.12 0.2417
0.1216 379.05 0.1578
0.1355 379.05 0.1695
0.1458 373.36 0.2176
0.1530 379.05 0.1806
0.1576 328.16 0.4029
0.1884 313.28 0.4788
0.1901 343.10 0.3884
0.1939 328.16 0.4475
0.1950 357.12 0.3407
0.1979 373.36 0.2712
0.2367 328.16 0.4934
0.2520 313.28 0.5538
0.2540 365.30 0.3674
0.2567 373.36 0.3180
0.2735 357.12 0.4241
0.2882 343.10 0.4860
0.2907 328.16 0.5371
0.3126 373.36 0.3510
0.3514 328.16 0.5814
0.3558 373.36 0.3619
0.3579 313.28 0.6235
0.3700 357.12 0.5083
0.3943 365.30 0.4856
0.4154 343.10 0.5791
0.4458 328.16 0.6331
0.4721 313.28 0.6750
0.4935 365.30 0.5586
0.5032 357.12 0.6001
0.5414 328.16 0.6782
0.6405 313.28 0.7293
0.6451 343.10 0.7066
0.6778 365.30 0.6988
0.7233 357.12 0.7385
0.7406 328.16 0.7570
0.7577 343.10 0.7623
0.7600 365.30 0.7666
0.8066 343.10 0.7886
0.8202 373.36 0.8080
0.8244 365.30 0.8069
0.8349 328.16 0.7984
0.8353 357.12 0.8105
0.8397 379.05 0.8363
0.8528 313.28 0.8026
0.8668 373.36 0.8459
0.8812 379.05 0.8635
0.8903 365.30 0.8594
0.9001 343.10 0.8513
0.9005 385.84 0.8991
0.9076 328.16 0.8447
0.9167 373.36 0.8910
0.9173 379.05 0.8959
0.9222 357.12 0.8822
0.9248 385.84 0.9123
0.9347 343.10 0.8857
0.9403 365.30 0.9084
0.9462 379.05 0.9258
0.9487 328.16 0.8887
0.9489 385.84 0.9347
0.9495 373.36 0.9294
0.9518 313.28 0.8825
0.9603 392.83 0.9575
0.9637 357.12 0.9330
0.9649 379.05 0.9482
0.9661 328.16 0.9166
0.9705 385.84 0.9591
0.9708 343.10 0.9352
0.9720 365.30 0.9502
0.9746 392.83 0.9683
0.9764 373.36 0.9606
0.9821 379.05 0.9700
0.9856 392.83 0.9812
0.9875 385.84 0.9814
0.9897 313.28 0.9655
0.9928 385.84 0.9890
0.9955 392.83 0.9937

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Mole fraction of Dimethyl ether (2) - Liquid Temperature, K - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0218 379.05 2105.70
0.0293 328.16 719.90
0.0315 313.28 494.90
0.0468 373.36 1989.70
0.0510 343.10 1086.50
0.0512 379.05 2237.20
0.0576 357.12 1482.60
0.0581 328.16 797.80
0.0669 313.28 571.90
0.0794 379.05 2354.80
0.0916 328.16 881.00
0.0960 373.36 2197.90
0.1109 379.05 2480.00
0.1133 313.28 659.10
0.1158 343.10 1278.40
0.1192 328.16 943.40
0.1195 357.12 1699.80
0.1216 379.05 2525.50
0.1355 379.05 2579.90
0.1458 373.36 2398.30
0.1530 379.05 2641.50
0.1576 328.16 1019.10
0.1884 313.28 767.30
0.1901 343.10 1459.50
0.1939 328.16 1085.20
0.1950 357.12 1935.40
0.1979 373.36 2589.40
0.2367 328.16 1155.40
0.2520 313.28 847.30
0.2540 365.30 2422.30
0.2567 373.36 2774.90
0.2735 357.12 2147.10
0.2882 343.10 1660.20
0.2907 328.16 1231.50
0.3126 373.36 2924.00
0.3514 328.16 1302.90
0.3558 373.36 2996.20
0.3579 313.28 937.70
0.3700 357.12 2368.60
0.3943 365.30 2794.30
0.4154 343.10 1862.40
0.4458 328.16 1388.40
0.4721 313.28 1000.60
0.4935 365.30 2995.80
0.5032 357.12 2599.90
0.5414 328.16 1452.10
0.6405 313.28 1049.90
0.6451 343.10 2072.50
0.6778 365.30 3248.50
0.7233 357.12 2794.40
0.7406 328.16 1516.40
0.7577 343.10 2106.00
0.7600 365.30 3281.80
0.8066 343.10 2104.20
0.8202 373.36 3796.30
0.8244 365.30 3266.10
0.8349 328.16 1512.80
0.8353 357.12 2785.10
0.8397 379.05 4193.80
0.8528 313.28 1054.50
0.8668 373.36 3751.40
0.8812 379.05 4135.10
0.8903 365.30 3200.70
0.9001 343.10 2057.50
0.9005 385.84 4583.00
0.9076 328.16 1480.70
0.9167 373.36 3657.80
0.9173 379.05 4052.50
0.9222 357.12 2690.40
0.9248 385.84 4537.10
0.9347 343.10 2012.80
0.9403 365.30 3100.40
0.9462 379.05 3964.50
0.9487 328.16 1436.10
0.9489 385.84 4449.70
0.9495 373.36 3564.80
0.9518 313.28 1003.20
0.9603 392.83 4949.80
0.9637 357.12 2589.30
0.9649 379.05 3888.60
0.9661 328.16 1404.20
0.9705 385.84 4348.10
0.9708 343.10 1933.60
0.9720 365.30 2995.30
0.9746 392.83 4880.50
0.9764 373.36 3454.00
0.9821 379.05 3802.10
0.9856 392.83 4810.50
0.9875 385.84 4251.60
0.9897 313.28 931.60
0.9928 385.84 4215.90
0.9955 392.83 4738.50

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Mole fraction of Dimethyl ether (2) - Liquid Temperature, K - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0218 379.05 2105.70
0.0293 328.16 719.90
0.0315 313.28 494.90
0.0468 373.36 1989.70
0.0510 343.10 1086.50
0.0512 379.05 2237.20
0.0576 357.12 1482.60
0.0581 328.16 797.80
0.0669 313.28 571.90
0.0794 379.05 2354.80
0.0916 328.16 881.00
0.0960 373.36 2197.90
0.1109 379.05 2480.00
0.1133 313.28 659.10
0.1158 343.10 1278.40
0.1192 328.16 943.40
0.1195 357.12 1699.80
0.1216 379.05 2525.50
0.1355 379.05 2579.90
0.1458 373.36 2398.30
0.1530 379.05 2641.50
0.1576 328.16 1019.10
0.1884 313.28 767.30
0.1901 343.10 1459.50
0.1939 328.16 1085.20
0.1950 357.12 1935.40
0.1979 373.36 2589.40
0.2367 328.16 1155.40
0.2520 313.28 847.30
0.2540 365.30 2422.30
0.2567 373.36 2774.90
0.2735 357.12 2147.10
0.2882 343.10 1660.20
0.2907 328.16 1231.50
0.3126 373.36 2924.00
0.3514 328.16 1302.90
0.3558 373.36 2996.20
0.3579 313.28 937.70
0.3700 357.12 2368.60
0.3943 365.30 2794.30
0.4154 343.10 1862.40
0.4458 328.16 1388.40
0.4721 313.28 1000.60
0.4935 365.30 2995.80
0.5032 357.12 2599.90
0.5414 328.16 1452.10
0.6405 313.28 1049.90
0.6451 343.10 2072.50
0.6778 365.30 3248.50
0.7233 357.12 2794.40
0.7406 328.16 1516.40
0.7577 343.10 2106.00
0.7600 365.30 3281.80
0.8066 343.10 2104.20
0.8202 373.36 3796.30
0.8244 365.30 3266.10
0.8349 328.16 1512.80
0.8353 357.12 2785.10
0.8397 379.05 4193.80
0.8528 313.28 1054.50
0.8668 373.36 3751.40
0.8812 379.05 4135.10
0.8903 365.30 3200.70
0.9001 343.10 2057.50
0.9005 385.84 4583.00
0.9076 328.16 1480.70
0.9167 373.36 3657.80
0.9173 379.05 4052.50
0.9222 357.12 2690.40
0.9248 385.84 4537.10
0.9347 343.10 2012.80
0.9403 365.30 3100.40
0.9462 379.05 3964.50
0.9487 328.16 1436.10
0.9489 385.84 4449.70
0.9495 373.36 3564.80
0.9518 313.28 1003.20
0.9603 392.83 4949.80
0.9637 357.12 2589.30
0.9649 379.05 3888.60
0.9661 328.16 1404.20
0.9705 385.84 4348.10
0.9708 343.10 1933.60
0.9720 365.30 2995.30
0.9746 392.83 4880.50
0.9764 373.36 3454.00
0.9821 379.05 3802.10
0.9856 392.83 4810.50
0.9875 385.84 4251.60
0.9897 313.28 931.60
0.9928 385.84 4215.90
0.9955 392.83 4738.50

Sources