Mixture of Carbon dioxide + Butanedioic acid, diethyl ester

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Carbon dioxide

Name
Carbon dioxide
InChI
InChI=1S/CO2/c2-1-3
InChI Key
CURLTUGMZLYLDI-UHFFFAOYSA-N
Formula
CO2
SMILES
O=C=O
Mol. Weight (g/mol)
44.01
CAS
124-38-9

Butanedioic acid, diethyl ester

Name
Butanedioic acid, diethyl ester
InChI
InChI=1S/C8H14O4/c1-3-11-7(9)5-6-8(10)12-4-2/h3-6H2,1-2H3
InChI Key
DKMROQRQHGEIOW-UHFFFAOYSA-N
Formula
C8H14O4
SMILES
CCOC(=O)CCC(=O)OCC
Mol. Weight (g/mol)
174.19
CAS
123-25-1
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Datasets

  1. Mole fraction (2)
  2. Pvap - Vapor or sublimation pressure, kPa (2)
  3. Vapor or sublimation pressure, kPa (2)

Mole fraction of Carbon dioxide (1) [ref]

Fixed Measured
Temperature, K - Liquid Pressure, kPa of Carbon dioxide (1) - Gas Mole fraction of Carbon dioxide (1) - Liquid
285.19 63.60 0.0143
285.19 133.60 0.0300
285.19 199.20 0.0389
285.19 273.20 0.0616
285.19 525.50 0.1067
285.19 828.70 0.1868
285.19 966.20 0.2178
285.19 1260.90 0.2707
285.19 1435.20 0.3236
285.19 1724.60 0.3888
285.19 1893.50 0.4269
285.19 2157.90 0.4865
285.19 2414.60 0.5444
285.19 2596.20 0.5853
285.19 2772.30 0.6250
285.19 2979.80 0.6718
285.19 3378.40 0.7391
285.19 3565.30 0.7812
291.43 139.70 0.0273
291.43 176.20 0.0345
291.43 228.10 0.0407
291.43 272.20 0.0532
291.43 463.10 0.0906
291.43 807.80 0.1522
291.43 1002.70 0.1962
291.43 1337.60 0.2539
291.43 1605.20 0.2945
291.43 1843.10 0.3607
291.43 2023.50 0.3959
291.43 2341.40 0.4581
291.43 2561.90 0.5013
291.43 2886.50 0.5648
291.43 3314.20 0.6485
291.43 3595.00 0.7035
291.43 3883.10 0.7499
291.43 4212.40 0.8047
299.56 178.40 0.0292
299.56 258.40 0.0424
299.56 322.70 0.0529
299.56 485.10 0.0796
299.56 522.90 0.0858
299.56 636.70 0.1045
299.56 723.30 0.1187
299.56 954.70 0.1567
299.56 1408.50 0.2180
299.56 1712.10 0.2810
299.56 2119.70 0.3397
299.56 2315.10 0.3799
299.56 2733.40 0.4486
299.56 2990.40 0.4908
299.56 3279.70 0.5383
299.56 3582.20 0.5879
299.56 3961.90 0.6338
299.56 4298.60 0.6792
304.37 123.10 0.0187
304.37 255.70 0.0388
304.37 324.40 0.0492
304.37 471.10 0.0714
304.37 641.50 0.0972
304.37 828.90 0.1256
304.37 1093.30 0.1657
304.37 1396.40 0.2117
304.37 1718.20 0.2604
304.37 2059.00 0.3121
304.37 2471.30 0.3746
304.37 2651.90 0.4019
304.37 2957.70 0.4483
304.37 3331.80 0.5051
304.37 3579.20 0.5425
304.37 3794.40 0.5751
304.37 4156.80 0.6164
304.37 4673.20 0.6932
313.26 154.70 0.0201
313.26 254.40 0.0329
313.26 453.90 0.0587
313.26 507.40 0.0656
313.26 767.20 0.0863
313.26 885.10 0.1144
313.26 1244.80 0.1609
313.26 1583.10 0.2047
313.26 1787.80 0.2311
313.26 2043.30 0.2642
313.26 2365.10 0.3058
313.26 2745.70 0.3421
313.26 3229.50 0.4175
313.26 3732.60 0.4826
313.26 4240.10 0.5353
313.26 4761.10 0.6156
313.26 5450.50 0.6918
313.26 5805.80 0.7377

Mole fraction of Carbon dioxide (1) [ref]

Fixed Measured
Temperature, K - Liquid Pressure, kPa of Carbon dioxide (1) - Gas Mole fraction of Carbon dioxide (1) - Liquid
285.19 63.60 0.0143
285.19 133.60 0.0300
285.19 199.20 0.0389
285.19 273.20 0.0616
285.19 525.50 0.1067
285.19 828.70 0.1868
285.19 966.20 0.2178
285.19 1260.90 0.2707
285.19 1435.20 0.3236
285.19 1724.60 0.3888
285.19 1893.50 0.4269
285.19 2157.90 0.4865
285.19 2414.60 0.5444
285.19 2596.20 0.5853
285.19 2772.30 0.6250
285.19 2979.80 0.6718
285.19 3378.40 0.7391
285.19 3565.30 0.7812
291.43 139.70 0.0273
291.43 176.20 0.0345
291.43 228.10 0.0407
291.43 272.20 0.0532
291.43 463.10 0.0906
291.43 807.80 0.1522
291.43 1002.70 0.1962
291.43 1337.60 0.2539
291.43 1605.20 0.2945
291.43 1843.10 0.3607
291.43 2023.50 0.3959
291.43 2341.40 0.4581
291.43 2561.90 0.5013
291.43 2886.50 0.5648
291.43 3314.20 0.6485
291.43 3595.00 0.7035
291.43 3883.10 0.7499
291.43 4212.40 0.8047
299.56 178.40 0.0292
299.56 258.40 0.0424
299.56 322.70 0.0529
299.56 485.10 0.0796
299.56 522.90 0.0858
299.56 636.70 0.1045
299.56 723.30 0.1187
299.56 954.70 0.1567
299.56 1408.50 0.2180
299.56 1712.10 0.2810
299.56 2119.70 0.3397
299.56 2315.10 0.3799
299.56 2733.40 0.4486
299.56 2990.40 0.4908
299.56 3279.70 0.5383
299.56 3582.20 0.5879
299.56 3961.90 0.6338
299.56 4298.60 0.6792
304.37 123.10 0.0187
304.37 255.70 0.0388
304.37 324.40 0.0492
304.37 471.10 0.0714
304.37 641.50 0.0972
304.37 828.90 0.1256
304.37 1093.30 0.1657
304.37 1396.40 0.2117
304.37 1718.20 0.2604
304.37 2059.00 0.3121
304.37 2471.30 0.3746
304.37 2651.90 0.4019
304.37 2957.70 0.4483
304.37 3331.80 0.5051
304.37 3579.20 0.5425
304.37 3794.40 0.5751
304.37 4156.80 0.6164
304.37 4673.20 0.6932
313.26 154.70 0.0201
313.26 254.40 0.0329
313.26 453.90 0.0587
313.26 507.40 0.0656
313.26 767.20 0.0863
313.26 885.10 0.1144
313.26 1244.80 0.1609
313.26 1583.10 0.2047
313.26 1787.80 0.2311
313.26 2043.30 0.2642
313.26 2365.10 0.3058
313.26 2745.70 0.3421
313.26 3229.50 0.4175
313.26 3732.60 0.4826
313.26 4240.10 0.5353
313.26 4761.10 0.6156
313.26 5450.50 0.6918
313.26 5805.80 0.7377

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of Carbon dioxide (1) - Liquid Vapor or sublimation pressure, kPa - Liquid
308.21 0.4246 2460.00
308.21 0.5484 3440.00
308.21 0.7024 4950.00
308.21 0.8052 6060.00
308.21 0.9008 6900.00
308.21 0.9483 7380.00
308.21 0.9925 7690.00
318.24 0.4246 2880.00
318.24 0.5484 4480.00
318.24 0.7024 6070.00
318.24 0.8052 7360.00
318.24 0.9008 8240.00
318.24 0.9483 8910.00
328.23 0.4246 3400.00
328.23 0.5484 5030.00
328.23 0.7024 7230.00
328.23 0.8052 8530.00
328.23 0.9008 9930.00
328.23 0.9483 10720.00
337.91 0.4246 3810.00
337.91 0.5484 5340.00
337.91 0.7024 8220.00
337.91 0.8052 10150.00
337.91 0.9008 11620.00
337.91 0.9483 12570.00
348.13 0.4246 4530.00
348.13 0.5484 6250.00
348.13 0.7024 9520.00
348.13 0.8052 11610.00
348.13 0.9008 13570.00
348.13 0.9483 14450.00
358.09 0.4246 5140.00
358.09 0.5484 7060.00
358.09 0.7024 10750.00
358.09 0.8052 13200.00
358.09 0.9008 15210.00
358.09 0.9483 16020.00

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of Carbon dioxide (1) - Liquid Vapor or sublimation pressure, kPa - Liquid
308.21 0.4246 2460.00
308.21 0.5484 3440.00
308.21 0.7024 4950.00
308.21 0.8052 6060.00
308.21 0.9008 6900.00
308.21 0.9483 7380.00
308.21 0.9925 7690.00
318.24 0.4246 2880.00
318.24 0.5484 4480.00
318.24 0.7024 6070.00
318.24 0.8052 7360.00
318.24 0.9008 8240.00
318.24 0.9483 8910.00
328.23 0.4246 3400.00
328.23 0.5484 5030.00
328.23 0.7024 7230.00
328.23 0.8052 8530.00
328.23 0.9008 9930.00
328.23 0.9483 10720.00
337.91 0.4246 3810.00
337.91 0.5484 5340.00
337.91 0.7024 8220.00
337.91 0.8052 10150.00
337.91 0.9008 11620.00
337.91 0.9483 12570.00
348.13 0.4246 4530.00
348.13 0.5484 6250.00
348.13 0.7024 9520.00
348.13 0.8052 11610.00
348.13 0.9008 13570.00
348.13 0.9483 14450.00
358.09 0.4246 5140.00
358.09 0.5484 7060.00
358.09 0.7024 10750.00
358.09 0.8052 13200.00
358.09 0.9008 15210.00
358.09 0.9483 16020.00

Vapor or sublimation pressure, kPa [ref]

Operational condition: Mole fraction = 0.9925 (Gas)

Temperature, K - Gas Vapor or sublimation pressure, kPa - Gas
318.24 8990.00
328.23 10390.00
337.91 11670.00
348.13 12820.00
358.09 13740.00

Vapor or sublimation pressure, kPa [ref]

Operational condition: Mole fraction = 0.9925 (Gas)

Temperature, K - Gas Vapor or sublimation pressure, kPa - Gas
318.24 8990.00
328.23 10390.00
337.91 11670.00
348.13 12820.00
358.09 13740.00

Sources