- 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
- Name
- Ethanol
- InChI
- InChI=1S/C2H6O/c1-2-3/h3H,2H2,1H3
- InChI Key
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N
- Formula
- C2H6O
- SMILES
- CCO
- Mol. Weight (g/mol)
- 46.07
- CAS
- 64-17-5
- Name
- 1,4-Dioxane-2,5-dione, 3,6-dimethyl-, (3S-cis)-
- InChI
- InChI=1S/C6H8O4/c1-3-5(7)10-4(2)6(8)9-3/h3-4H,1-2H3/t3-,4-/m0/s1
- InChI Key
- JJTUDXZGHPGLLC-IMJSIDKUSA-N
- Formula
- C6H8O4
- SMILES
- CC1OC(=O)C(C)OC1=O
- Mol. Weight (g/mol)
- 144.13
- CAS
- 4511-42-6
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Datasets
Vapor or sublimation pressure, kPa [ref]
| Fixed | Measured | ||
|---|---|---|---|
| Temperature, K - Liquid | Mole fraction of Carbon dioxide (1) - Liquid | Mole fraction of 1,4-Dioxane-2,5-dione, 3,6-dimethyl-, (3S-cis)- (3) - Liquid | Vapor or sublimation pressure, kPa - Liquid |
| 323.00 | 0.6663 | 0.2227 | 12610.00 |
| 333.00 | 0.6663 | 0.2227 | 15410.00 |
| 343.00 | 0.6663 | 0.2227 | 18130.00 |
| 323.00 | 0.7260 | 0.1824 | 16600.00 |
| 333.00 | 0.7260 | 0.1824 | 19400.00 |
| 343.00 | 0.7260 | 0.1824 | 21830.00 |
| 323.00 | 0.7587 | 0.1607 | 18520.00 |
| 333.00 | 0.7587 | 0.1607 | 21080.00 |
| 343.00 | 0.7587 | 0.1607 | 23630.00 |
| 323.00 | 0.7900 | 0.1398 | 19590.00 |
| 333.00 | 0.7900 | 0.1398 | 22090.00 |
| 343.00 | 0.7900 | 0.1398 | 25130.00 |
| 323.00 | 0.8235 | 0.1177 | 20750.00 |
| 333.00 | 0.8235 | 0.1177 | 23470.00 |
| 323.00 | 0.8366 | 0.1087 | 22300.00 |
| 323.00 | 0.8570 | 0.0953 | 23320.00 |
| 323.00 | 0.8914 | 0.0724 | 23720.00 |
| 323.00 | 0.5990 | 0.2006 | 9840.00 |
| 333.00 | 0.5990 | 0.2006 | 11920.00 |
| 343.00 | 0.5990 | 0.2006 | 13760.00 |
| 323.00 | 0.6661 | 0.1672 | 11710.00 |
| 333.00 | 0.6661 | 0.1672 | 14290.00 |
| 343.00 | 0.6661 | 0.1672 | 16630.00 |
| 323.00 | 0.6844 | 0.1578 | 12250.00 |
| 333.00 | 0.6844 | 0.1578 | 14720.00 |
| 343.00 | 0.6844 | 0.1578 | 17310.00 |
| 323.00 | 0.7015 | 0.1495 | 13450.00 |
| 333.00 | 0.7015 | 0.1495 | 15850.00 |
| 343.00 | 0.7015 | 0.1495 | 18070.00 |
| 323.00 | 0.7389 | 0.1305 | 14860.00 |
| 333.00 | 0.7389 | 0.1305 | 17150.00 |
| 343.00 | 0.7389 | 0.1305 | 19400.00 |
| 323.00 | 0.7774 | 0.1115 | 16050.00 |
| 333.00 | 0.7774 | 0.1115 | 18250.00 |
| 343.00 | 0.7774 | 0.1115 | 20570.00 |
| 323.00 | 0.8182 | 0.0909 | 17650.00 |
| 333.00 | 0.8182 | 0.0909 | 19950.00 |
| 343.00 | 0.8182 | 0.0909 | 21800.00 |
| 323.00 | 0.8606 | 0.0697 | 18350.00 |
| 333.00 | 0.8606 | 0.0697 | 20500.00 |
| 343.00 | 0.8606 | 0.0697 | 22650.00 |
| 323.00 | 0.9053 | 0.0474 | 18830.00 |
| 333.00 | 0.9053 | 0.0474 | 21630.00 |
| 343.00 | 0.9053 | 0.0474 | 23700.00 |
| 323.00 | 0.5455 | 0.1818 | 9210.00 |
| 333.00 | 0.5455 | 0.1818 | 11030.00 |
| 343.00 | 0.5455 | 0.1818 | 13240.00 |
| 353.00 | 0.5455 | 0.1818 | 15250.00 |
| 323.00 | 0.6153 | 0.1539 | 10130.00 |
| 333.00 | 0.6153 | 0.1539 | 12500.00 |
| 343.00 | 0.6153 | 0.1539 | 15010.00 |
| 353.00 | 0.6153 | 0.1539 | 16760.00 |
| 323.00 | 0.6935 | 0.1225 | 11550.00 |
| 333.00 | 0.6935 | 0.1225 | 14270.00 |
| 343.00 | 0.6935 | 0.1225 | 16760.00 |
| 353.00 | 0.6935 | 0.1225 | 18960.00 |
| 323.00 | 0.7151 | 0.1140 | 12180.00 |
| 333.00 | 0.7151 | 0.1140 | 14830.00 |
| 343.00 | 0.7151 | 0.1140 | 17390.00 |
| 353.00 | 0.7151 | 0.1140 | 19600.00 |
| 323.00 | 0.7371 | 0.1052 | 13290.00 |
| 333.00 | 0.7371 | 0.1052 | 15850.00 |
| 343.00 | 0.7371 | 0.1052 | 18380.00 |
| 353.00 | 0.7371 | 0.1052 | 20780.00 |
| 323.00 | 0.7829 | 0.0869 | 14500.00 |
| 333.00 | 0.7829 | 0.0869 | 17000.00 |
| 343.00 | 0.7829 | 0.0869 | 19300.00 |
| 353.00 | 0.7829 | 0.0869 | 21500.00 |
| 323.00 | 0.8207 | 0.0717 | 15500.00 |
| 333.00 | 0.8207 | 0.0717 | 18520.00 |
| 343.00 | 0.8207 | 0.0717 | 21000.00 |
| 353.00 | 0.8207 | 0.0717 | 23000.00 |
| 323.00 | 0.8522 | 0.0591 | 17140.00 |
| 333.00 | 0.8522 | 0.0591 | 19840.00 |
| 343.00 | 0.8522 | 0.0591 | 22470.00 |
| 323.00 | 0.8836 | 0.0465 | 17460.00 |
| 333.00 | 0.8836 | 0.0465 | 20010.00 |
| 343.00 | 0.8836 | 0.0465 | 22070.00 |
Vapor or sublimation pressure, kPa [ref]
| Fixed | Measured | ||
|---|---|---|---|
| Temperature, K - Liquid | Mole fraction of Carbon dioxide (1) - Liquid | Mole fraction of 1,4-Dioxane-2,5-dione, 3,6-dimethyl-, (3S-cis)- (3) - Liquid | Vapor or sublimation pressure, kPa - Liquid |
| 323.00 | 0.6663 | 0.2227 | 12610.00 |
| 333.00 | 0.6663 | 0.2227 | 15410.00 |
| 343.00 | 0.6663 | 0.2227 | 18130.00 |
| 323.00 | 0.7260 | 0.1824 | 16600.00 |
| 333.00 | 0.7260 | 0.1824 | 19400.00 |
| 343.00 | 0.7260 | 0.1824 | 21830.00 |
| 323.00 | 0.7587 | 0.1607 | 18520.00 |
| 333.00 | 0.7587 | 0.1607 | 21080.00 |
| 343.00 | 0.7587 | 0.1607 | 23630.00 |
| 323.00 | 0.7900 | 0.1398 | 19590.00 |
| 333.00 | 0.7900 | 0.1398 | 22090.00 |
| 343.00 | 0.7900 | 0.1398 | 25130.00 |
| 323.00 | 0.8235 | 0.1177 | 20750.00 |
| 333.00 | 0.8235 | 0.1177 | 23470.00 |
| 323.00 | 0.8366 | 0.1087 | 22300.00 |
| 323.00 | 0.8570 | 0.0953 | 23320.00 |
| 323.00 | 0.8914 | 0.0724 | 23720.00 |
| 323.00 | 0.5990 | 0.2006 | 9840.00 |
| 333.00 | 0.5990 | 0.2006 | 11920.00 |
| 343.00 | 0.5990 | 0.2006 | 13760.00 |
| 323.00 | 0.6661 | 0.1672 | 11710.00 |
| 333.00 | 0.6661 | 0.1672 | 14290.00 |
| 343.00 | 0.6661 | 0.1672 | 16630.00 |
| 323.00 | 0.6844 | 0.1578 | 12250.00 |
| 333.00 | 0.6844 | 0.1578 | 14720.00 |
| 343.00 | 0.6844 | 0.1578 | 17310.00 |
| 323.00 | 0.7015 | 0.1495 | 13450.00 |
| 333.00 | 0.7015 | 0.1495 | 15850.00 |
| 343.00 | 0.7015 | 0.1495 | 18070.00 |
| 323.00 | 0.7389 | 0.1305 | 14860.00 |
| 333.00 | 0.7389 | 0.1305 | 17150.00 |
| 343.00 | 0.7389 | 0.1305 | 19400.00 |
| 323.00 | 0.7774 | 0.1115 | 16050.00 |
| 333.00 | 0.7774 | 0.1115 | 18250.00 |
| 343.00 | 0.7774 | 0.1115 | 20570.00 |
| 323.00 | 0.8182 | 0.0909 | 17650.00 |
| 333.00 | 0.8182 | 0.0909 | 19950.00 |
| 343.00 | 0.8182 | 0.0909 | 21800.00 |
| 323.00 | 0.8606 | 0.0697 | 18350.00 |
| 333.00 | 0.8606 | 0.0697 | 20500.00 |
| 343.00 | 0.8606 | 0.0697 | 22650.00 |
| 323.00 | 0.9053 | 0.0474 | 18830.00 |
| 333.00 | 0.9053 | 0.0474 | 21630.00 |
| 343.00 | 0.9053 | 0.0474 | 23700.00 |
| 323.00 | 0.5455 | 0.1818 | 9210.00 |
| 333.00 | 0.5455 | 0.1818 | 11030.00 |
| 343.00 | 0.5455 | 0.1818 | 13240.00 |
| 353.00 | 0.5455 | 0.1818 | 15250.00 |
| 323.00 | 0.6153 | 0.1539 | 10130.00 |
| 333.00 | 0.6153 | 0.1539 | 12500.00 |
| 343.00 | 0.6153 | 0.1539 | 15010.00 |
| 353.00 | 0.6153 | 0.1539 | 16760.00 |
| 323.00 | 0.6935 | 0.1225 | 11550.00 |
| 333.00 | 0.6935 | 0.1225 | 14270.00 |
| 343.00 | 0.6935 | 0.1225 | 16760.00 |
| 353.00 | 0.6935 | 0.1225 | 18960.00 |
| 323.00 | 0.7151 | 0.1140 | 12180.00 |
| 333.00 | 0.7151 | 0.1140 | 14830.00 |
| 343.00 | 0.7151 | 0.1140 | 17390.00 |
| 353.00 | 0.7151 | 0.1140 | 19600.00 |
| 323.00 | 0.7371 | 0.1052 | 13290.00 |
| 333.00 | 0.7371 | 0.1052 | 15850.00 |
| 343.00 | 0.7371 | 0.1052 | 18380.00 |
| 353.00 | 0.7371 | 0.1052 | 20780.00 |
| 323.00 | 0.7829 | 0.0869 | 14500.00 |
| 333.00 | 0.7829 | 0.0869 | 17000.00 |
| 343.00 | 0.7829 | 0.0869 | 19300.00 |
| 353.00 | 0.7829 | 0.0869 | 21500.00 |
| 323.00 | 0.8207 | 0.0717 | 15500.00 |
| 333.00 | 0.8207 | 0.0717 | 18520.00 |
| 343.00 | 0.8207 | 0.0717 | 21000.00 |
| 353.00 | 0.8207 | 0.0717 | 23000.00 |
| 323.00 | 0.8522 | 0.0591 | 17140.00 |
| 333.00 | 0.8522 | 0.0591 | 19840.00 |
| 343.00 | 0.8522 | 0.0591 | 22470.00 |
| 323.00 | 0.8836 | 0.0465 | 17460.00 |
| 333.00 | 0.8836 | 0.0465 | 20010.00 |
| 343.00 | 0.8836 | 0.0465 | 22070.00 |
Vapor or sublimation pressure, kPa [ref]
| Fixed | Measured | ||
|---|---|---|---|
| Temperature, K - Gas | Mole fraction of Carbon dioxide (1) - Gas | Mole fraction of 1,4-Dioxane-2,5-dione, 3,6-dimethyl-, (3S-cis)- (3) - Gas | Vapor or sublimation pressure, kPa - Gas |
| 323.00 | 0.9263 | 0.0489 | 23300.00 |
| 323.00 | 0.9481 | 0.0344 | 22250.00 |
| 323.00 | 0.9706 | 0.0198 | 19800.00 |
| 333.00 | 0.9706 | 0.0198 | 21810.00 |
| 343.00 | 0.9706 | 0.0198 | 23800.00 |
| 323.00 | 0.9849 | 0.0100 | 15360.00 |
| 333.00 | 0.9849 | 0.0100 | 17570.00 |
| 343.00 | 0.9849 | 0.0100 | 19800.00 |
| 323.00 | 0.9602 | 0.0202 | 17280.00 |
| 333.00 | 0.9602 | 0.0202 | 19570.00 |
| 343.00 | 0.9602 | 0.0202 | 21480.00 |
| 323.00 | 0.9801 | 0.0100 | 15250.00 |
| 333.00 | 0.9801 | 0.0100 | 17250.00 |
| 343.00 | 0.9801 | 0.0100 | 19450.00 |
| 323.00 | 0.9167 | 0.0333 | 16790.00 |
| 333.00 | 0.9167 | 0.0333 | 19480.00 |
| 343.00 | 0.9167 | 0.0333 | 21800.00 |
| 353.00 | 0.9167 | 0.0333 | 23940.00 |
| 323.00 | 0.9515 | 0.0194 | 15720.00 |
| 333.00 | 0.9515 | 0.0194 | 18540.00 |
| 343.00 | 0.9515 | 0.0194 | 20430.00 |
| 353.00 | 0.9515 | 0.0194 | 22500.00 |
| 323.00 | 0.9755 | 0.0098 | 13380.00 |
| 333.00 | 0.9755 | 0.0098 | 15690.00 |
| 343.00 | 0.9755 | 0.0098 | 18060.00 |
| 353.00 | 0.9755 | 0.0098 | 19620.00 |
Vapor or sublimation pressure, kPa [ref]
| Fixed | Measured | ||
|---|---|---|---|
| Temperature, K - Gas | Mole fraction of Carbon dioxide (1) - Gas | Mole fraction of 1,4-Dioxane-2,5-dione, 3,6-dimethyl-, (3S-cis)- (3) - Gas | Vapor or sublimation pressure, kPa - Gas |
| 323.00 | 0.9263 | 0.0489 | 23300.00 |
| 323.00 | 0.9481 | 0.0344 | 22250.00 |
| 323.00 | 0.9706 | 0.0198 | 19800.00 |
| 333.00 | 0.9706 | 0.0198 | 21810.00 |
| 343.00 | 0.9706 | 0.0198 | 23800.00 |
| 323.00 | 0.9849 | 0.0100 | 15360.00 |
| 333.00 | 0.9849 | 0.0100 | 17570.00 |
| 343.00 | 0.9849 | 0.0100 | 19800.00 |
| 323.00 | 0.9602 | 0.0202 | 17280.00 |
| 333.00 | 0.9602 | 0.0202 | 19570.00 |
| 343.00 | 0.9602 | 0.0202 | 21480.00 |
| 323.00 | 0.9801 | 0.0100 | 15250.00 |
| 333.00 | 0.9801 | 0.0100 | 17250.00 |
| 343.00 | 0.9801 | 0.0100 | 19450.00 |
| 323.00 | 0.9167 | 0.0333 | 16790.00 |
| 333.00 | 0.9167 | 0.0333 | 19480.00 |
| 343.00 | 0.9167 | 0.0333 | 21800.00 |
| 353.00 | 0.9167 | 0.0333 | 23940.00 |
| 323.00 | 0.9515 | 0.0194 | 15720.00 |
| 333.00 | 0.9515 | 0.0194 | 18540.00 |
| 343.00 | 0.9515 | 0.0194 | 20430.00 |
| 353.00 | 0.9515 | 0.0194 | 22500.00 |
| 323.00 | 0.9755 | 0.0098 | 13380.00 |
| 333.00 | 0.9755 | 0.0098 | 15690.00 |
| 343.00 | 0.9755 | 0.0098 | 18060.00 |
| 353.00 | 0.9755 | 0.0098 | 19620.00 |