- InChI
- InChI=1S/C4H6O3/c1-3-2-6-4(5)7-3/h3H,2H2,1H3
- InChI Key
- RUOJZAUFBMNUDX-UHFFFAOYSA-N
- Formula
- C4H6O3
- SMILES
- CC1COC(=O)O1
- Molecular Weight1
- 102.09
- CAS
- 108-32-7
- Other Names
-
- 1,2-PDC
- 1,2-Propanediol carbonate
- 1,2-Propanediol cyclic carbonate
- 1,2-Propanediyl carbonate
- 1,2-Propylene carbonate
- 1,2-Propylene glycol carbonate
- 1,3-Dioxolan-2-one, 4-methyl-
- 1-Methylethylene carbonate
- 4-Methyl-1,3-dioxol-2-one
- 4-Methyl-1,3-dioxolan-2-one
- 4-Methyl-2-oxo-1,3-dioxolane
- 4-Methyldioxalone-2
- Arconate 5000
- Arconate propylene carbonate
- Carbonic acid cyclic methylethylene ester
- Carbonic acid, cyclic propylene ester
- Carbonic acid, propylene ester
- Cyclic 1,2-propylene carbonate
- Cyclic methylethylene carbonate
- Cyclic propylene carbonate
- Dipropylene carbonate
- NSC 11784
- PC-HP
- Propylene glycol cyclic carbonate
- Propylenester kyseliny uhlicite
- Solvenon PC
- Texacar PC
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- η : Dynamic viscosity (Pa×s).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfH°liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔfusH : Enthalpy of fusion at a given temperature (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- S°liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
- csound,fluid : Speed of sound in fluid (m/s).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- Vc : Critical Volume (m3/kmol).
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔcH°liquid | [-1818.00; -1799.70] | kJ/mol |
|
| ΔcH°liquid | -1818.00 ± 1.00 | kJ/mol | NIST |
| ΔcH°liquid | -1799.70 ± 2.10 | kJ/mol | NIST |
| Cp,liquid | 166.98 | J/mol×K | Volumes... |
| ΔfG° | -275.48 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | [-582.50; -563.70] | kJ/mol |
|
| ΔfH°gas | -563.70 | kJ/mol | NIST |
| ΔfH°gas | -582.50 ± 2.50 | kJ/mol | NIST |
| ΔfH°liquid | [-631.80; -613.00] | kJ/mol |
|
| ΔfH°liquid | -613.00 ± 1.00 | kJ/mol | NIST |
| ΔfH°liquid | -631.80 ± 2.10 | kJ/mol | NIST |
| ΔfusH° | 15.52 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [30.70; 71.30] | kJ/mol |
|
| ΔvapH° | 61.50 ± 0.30 | kJ/mol | NIST |
| ΔvapH° | 71.30 | kJ/mol | NIST |
| ΔvapH° | 61.30 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 71.20 ± 0.60 | kJ/mol | NIST |
| ΔvapH° | 30.70 ± 2.10 | kJ/mol | NIST |
| ΔvapH° | 49.30 | kJ/mol | NIST |
| log10WS | -0.43 | Crippen Calculated Property | |
| logPoct/wat | 0.542 | Crippen Calculated Property | |
| McVol | 69.670 | ml/mol | McGowan Calculated Property |
| Pc | 5065.79 | kPa | Joback Calculated Property |
| Inp | [929.00; 932.00] |
|
|
| Inp | 929.00 | NIST | |
| Inp | 932.00 | NIST | |
| S°liquid | [218.60; 219.17] | J/mol×K |
|
| S°liquid | 218.60 | J/mol×K | NIST |
| S°liquid | 219.17 | J/mol×K | NIST |
| Tboil | [513.20; 515.05] | K |
|
| Tboil | 513.20 | K | NIST |
| Tboil | 515.05 ± 0.70 | K | NIST |
| Tc | 650.09 | K | Joback Calculated Property |
| Tfus | [218.62; 222.95] | K |
|
| Tfus | 222.95 ± 1.00 | K | NIST |
| Tfus | 222.95 ± 0.30 | K | NIST |
| Tfus | 218.62 ± 0.06 | K | NIST |
| Ttriple | [218.66; 224.85] | K |
|
| Ttriple | 218.66 ± 0.02 | K | NIST |
| Ttriple | 224.85 ± 0.02 | K | NIST |
| Ttriple | 224.85 ± 0.02 | K | NIST |
| Vc | 0.249 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [142.54; 195.81] | J/mol×K | [427.92; 650.09] |
|
| Cp,gas | 142.54 | J/mol×K | 427.92 | Joback Calculated Property |
| Cp,gas | 152.33 | J/mol×K | 464.95 | Joback Calculated Property |
| Cp,gas | 161.78 | J/mol×K | 501.98 | Joback Calculated Property |
| Cp,gas | 170.87 | J/mol×K | 539.01 | Joback Calculated Property |
| Cp,gas | 179.59 | J/mol×K | 576.04 | Joback Calculated Property |
| Cp,gas | 187.91 | J/mol×K | 613.07 | Joback Calculated Property |
| Cp,gas | 195.81 | J/mol×K | 650.09 | Joback Calculated Property |
| Cp,liquid | [166.28; 205.10] | J/mol×K | [288.15; 423.15] |
|
| Cp,liquid | 166.28 | J/mol×K | 288.15 | Densiti... |
| Cp,liquid | 167.97 | J/mol×K | 293.15 | Densiti... |
| Cp,liquid | 174.10 | J/mol×K | 293.15 | Excess ... |
| Cp,liquid | 175.00 | J/mol×K | 298.00 | NIST |
| Cp,liquid | 174.90 | J/mol×K | 298.15 | Excess ... |
| Cp,liquid | 167.40 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 169.48 | J/mol×K | 298.15 | Densiti... |
| Cp,liquid | 167.60 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 170.49 | J/mol×K | 303.15 | Vapor P... |
| Cp,liquid | 170.79 | J/mol×K | 303.15 | Densiti... |
| Cp,liquid | 175.70 | J/mol×K | 303.15 | Excess ... |
| Cp,liquid | 176.70 | J/mol×K | 308.15 | Excess ... |
| Cp,liquid | 172.22 | J/mol×K | 308.15 | Densiti... |
| Cp,liquid | 174.14 | J/mol×K | 313.15 | Densiti... |
| Cp,liquid | 172.53 | J/mol×K | 313.15 | Vapor P... |
| Cp,liquid | 177.80 | J/mol×K | 313.15 | Excess ... |
| Cp,liquid | 175.87 | J/mol×K | 318.15 | Densiti... |
| Cp,liquid | 179.00 | J/mol×K | 318.15 | Excess ... |
| Cp,liquid | 180.00 | J/mol×K | 323.15 | Excess ... |
| Cp,liquid | 174.57 | J/mol×K | 323.15 | Vapor P... |
| Cp,liquid | 177.45 | J/mol×K | 323.15 | Densiti... |
| Cp,liquid | 184.10 | J/mol×K | 323.15 | NIST |
| Cp,liquid | 181.60 | J/mol×K | 328.15 | Excess ... |
| Cp,liquid | 182.30 | J/mol×K | 333.15 | Excess ... |
| Cp,liquid | 176.61 | J/mol×K | 333.15 | Vapor P... |
| Cp,liquid | 183.30 | J/mol×K | 338.15 | Excess ... |
| Cp,liquid | 178.66 | J/mol×K | 343.15 | Vapor P... |
| Cp,liquid | 184.50 | J/mol×K | 343.15 | Excess ... |
| Cp,liquid | 185.10 | J/mol×K | 348.15 | Excess ... |
| Cp,liquid | 186.20 | J/mol×K | 353.15 | Excess ... |
| Cp,liquid | 180.70 | J/mol×K | 353.15 | Vapor P... |
| Cp,liquid | 187.40 | J/mol×K | 358.15 | Excess ... |
| Cp,liquid | 183.76 | J/mol×K | 363.15 | Vapor P... |
| Cp,liquid | 189.50 | J/mol×K | 363.15 | Excess ... |
| Cp,liquid | 190.80 | J/mol×K | 368.15 | Excess ... |
| Cp,liquid | 192.70 | J/mol×K | 373.15 | Excess ... |
| Cp,liquid | 185.80 | J/mol×K | 373.15 | Vapor P... |
| Cp,liquid | 193.00 | J/mol×K | 378.15 | Excess ... |
| Cp,liquid | 194.30 | J/mol×K | 383.15 | Excess ... |
| Cp,liquid | 188.86 | J/mol×K | 383.15 | Vapor P... |
| Cp,liquid | 195.60 | J/mol×K | 388.15 | Excess ... |
| Cp,liquid | 190.91 | J/mol×K | 393.15 | Vapor P... |
| Cp,liquid | 197.30 | J/mol×K | 393.15 | Excess ... |
| Cp,liquid | 198.20 | J/mol×K | 398.15 | Excess ... |
| Cp,liquid | 199.90 | J/mol×K | 403.15 | Excess ... |
| Cp,liquid | 201.00 | J/mol×K | 408.15 | Excess ... |
| Cp,liquid | 202.30 | J/mol×K | 413.15 | Excess ... |
| Cp,liquid | 203.60 | J/mol×K | 418.15 | Excess ... |
| Cp,liquid | 205.10 | J/mol×K | 423.15 | Excess ... |
| η | [0.0016200; 0.0030860] | Pa×s | [288.15; 323.15] |
|
| η | 0.0030860 | Pa×s | 288.15 | Viscosi... |
| η | 0.0030860 | Pa×s | 288.15 | Densiti... |
| η | 0.0027620 | Pa×s | 293.15 | Densiti... |
| η | 0.0024990 | Pa×s | 298.15 | Densiti... |
| η | 0.0025200 | Pa×s | 298.15 | Volumet... |
| η | 0.0025000 | Pa×s | 298.15 | Viscosi... |
| η | 0.0022700 | Pa×s | 303.15 | Volumet... |
| η | 0.0022710 | Pa×s | 303.15 | Densiti... |
| η | 0.0020730 | Pa×s | 308.15 | Densiti... |
| η | 0.0020800 | Pa×s | 308.15 | Volumet... |
| η | 0.0020730 | Pa×s | 308.15 | Viscosi... |
| η | 0.0019100 | Pa×s | 313.15 | Volumet... |
| η | 0.0017500 | Pa×s | 318.15 | Volumet... |
| η | 0.0016200 | Pa×s | 323.15 | Volumet... |
| ΔfusH | [8.01; 9.62] | kJ/mol | [156.50; 224.85] |
|
| ΔfusH | 8.01 | kJ/mol | 156.50 | NIST |
| ΔfusH | 9.62 | kJ/mol | 218.20 | NIST |
| ΔfusH | 9.62 | kJ/mol | 218.20 | NIST |
| ΔfusH | 8.96 | kJ/mol | 220.30 | NIST |
| ΔfusH | 9.62 | kJ/mol | 224.85 | NIST |
| ΔfusH | 9.62 | kJ/mol | 224.85 | NIST |
| ΔvapH | [33.80; 57.80] | kJ/mol | [323.00; 439.00] |
|
| ΔvapH | 55.20 | kJ/mol | 323.00 | NIST |
| ΔvapH | 33.80 | kJ/mol | 346.50 | NIST |
| ΔvapH | 57.80 | kJ/mol | 415.00 | NIST |
| ΔvapH | 55.20 | kJ/mol | 415.00 | NIST |
| ΔvapH | 53.00 | kJ/mol | 415.00 | NIST |
| ΔvapH | 55.23 | kJ/mol | 423.00 | NIST |
| ΔvapH | 54.40 | kJ/mol | 439.00 | NIST |
| Pvap | [8.50e-03; 50.00] | kPa | [298.40; 485.91] |
|
| Pvap | 8.50e-03 | kPa | 298.40 | Vapour ... |
| Pvap | 0.01 | kPa | 303.30 | Vapour ... |
| Pvap | 0.02 | kPa | 308.20 | Vapour ... |
| Pvap | 0.02 | kPa | 311.30 | Vapour ... |
| Pvap | 0.03 | kPa | 313.20 | Vapour ... |
| Pvap | 0.04 | kPa | 318.20 | Vapour ... |
| Pvap | 0.05 | kPa | 321.20 | Vapour ... |
| Pvap | 0.05 | kPa | 322.70 | Vapour ... |
| Pvap | 0.06 | kPa | 324.20 | Vapour ... |
| Pvap | 0.07 | kPa | 326.60 | Vapour ... |
| Pvap | 0.06 | kPa | 327.12 | Low pre... |
| Pvap | 0.08 | kPa | 329.60 | Vapour ... |
| Pvap | 0.08 | kPa | 331.22 | Low pre... |
| Pvap | 0.10 | kPa | 332.70 | Vapour ... |
| Pvap | 0.13 | kPa | 335.70 | Vapour ... |
| Pvap | 0.14 | kPa | 337.70 | Vapour ... |
| Pvap | 0.12 | kPa | 338.15 | Low pre... |
| Pvap | 0.15 | kPa | 338.80 | Vapour ... |
| Pvap | 0.17 | kPa | 340.80 | Vapour ... |
| Pvap | 0.18 | kPa | 341.80 | Vapour ... |
| Pvap | 0.18 | kPa | 343.15 | Low pre... |
| Pvap | 0.22 | kPa | 344.90 | Vapour ... |
| Pvap | 0.22 | kPa | 348.15 | Low pre... |
| Pvap | 0.25 | kPa | 348.15 | Vapor P... |
| Pvap | 0.29 | kPa | 353.15 | Low pre... |
| Pvap | 0.33 | kPa | 353.15 | Vapor P... |
| Pvap | 0.44 | kPa | 358.15 | Vapor P... |
| Pvap | 0.56 | kPa | 363.15 | Vapor P... |
| Pvap | 0.72 | kPa | 368.15 | Vapor P... |
| Pvap | 0.92 | kPa | 373.15 | Vapor P... |
| Pvap | 1.17 | kPa | 378.15 | Vapor P... |
| Pvap | 1.86 | kPa | 388.15 | Vapor P... |
| Pvap | 2.28 | kPa | 393.15 | Vapor P... |
| Pvap | 2.83 | kPa | 398.15 | Vapor P... |
| Pvap | 3.48 | kPa | 403.15 | Vapor P... |
| Pvap | 4.00 | kPa | 407.97 | Phase E... |
| Pvap | 4.26 | kPa | 408.15 | Vapor P... |
| Pvap | 5.15 | kPa | 413.15 | Vapor P... |
| Pvap | 6.23 | kPa | 418.15 | Vapor P... |
| Pvap | 7.45 | kPa | 423.15 | Vapor P... |
| Pvap | 8.96 | kPa | 428.15 | Vapor P... |
| Pvap | 10.00 | kPa | 432.45 | Phase E... |
| Pvap | 10.78 | kPa | 433.15 | Vapor P... |
| Pvap | 12.00 | kPa | 437.77 | Phase E... |
| Pvap | 12.69 | kPa | 438.15 | Vapor P... |
| Pvap | 14.81 | kPa | 443.15 | Vapor P... |
| Pvap | 17.81 | kPa | 448.15 | Vapor P... |
| Pvap | 20.50 | kPa | 453.15 | Vapor P... |
| Pvap | 20.00 | kPa | 453.60 | Phase E... |
| Pvap | 24.08 | kPa | 458.15 | Vapor P... |
| Pvap | 27.96 | kPa | 463.15 | Vapor P... |
| Pvap | 30.00 | kPa | 467.23 | Phase E... |
| Pvap | 33.01 | kPa | 468.15 | Vapor P... |
| Pvap | 37.77 | kPa | 473.15 | Vapor P... |
| Pvap | 40.00 | kPa | 477.53 | Phase E... |
| Pvap | 50.00 | kPa | 485.91 | Phase E... |
| n0 | [1.41900; 1.42095] | [293.15; 298.15] |
|
|
| n0 | 1.42095 | 293.15 | The vol... | |
| n0 | 1.41900 | 298.15 | Liquid-... | |
| n0 | 1.42030 | 298.15 | Viscosi... | |
| ρl | [1088.38; 1226.25] | kg/m3 | [273.15; 363.15] |
|
| ρl | 1226.25 | kg/m3 | 273.15 | Self-Di... |
| ρl | 1220.90 | kg/m3 | 278.15 | Self-Di... |
| ρl | 1215.55 | kg/m3 | 283.15 | Self-Di... |
| ρl | 1216.30 | kg/m3 | 283.15 | Density... |
| ρl | 1205.20 | kg/m3 | 293.15 | Density... |
| ρl | 1204.89 | kg/m3 | 293.15 | Self-Di... |
| ρl | 1204.81 | kg/m3 | 293.15 | Density... |
| ρl | 1200.25 | kg/m3 | 293.15 | Excess ... |
| ρl | 1199.49 | kg/m3 | 298.15 | Ionic m... |
| ρl | 1204.00 | kg/m3 | 298.15 | Isobari... |
| ρl | 1197.60 | kg/m3 | 298.15 | Isobari... |
| ρl | 1199.58 | kg/m3 | 298.15 | Self-Di... |
| ρl | 1199.02 | kg/m3 | 298.15 | Density... |
| ρl | 1194.50 | kg/m3 | 303.15 | Density... |
| ρl | 1194.27 | kg/m3 | 303.15 | Self-Di... |
| ρl | 1180.56 | kg/m3 | 303.15 | Excess ... |
| ρl | 1180.55 | kg/m3 | 303.15 | Excess ... |
| ρl | 1194.00 | kg/m3 | 303.15 | Density... |
| ρl | 1188.57 | kg/m3 | 308.15 | Density... |
| ρl | 1188.89 | kg/m3 | 308.15 | Excess ... |
| ρl | 1183.67 | kg/m3 | 313.15 | Self-Di... |
| ρl | 1183.11 | kg/m3 | 313.15 | Density... |
| ρl | 1183.90 | kg/m3 | 313.15 | Density... |
| ρl | 1161.28 | kg/m3 | 313.15 | Excess ... |
| ρl | 1177.55 | kg/m3 | 318.15 | Density... |
| ρl | 1171.96 | kg/m3 | 323.15 | Density... |
| ρl | 1142.43 | kg/m3 | 323.15 | Excess ... |
| ρl | 1173.40 | kg/m3 | 323.15 | Density... |
| ρl | 1173.08 | kg/m3 | 323.15 | Self-Di... |
| ρl | 1162.50 | kg/m3 | 333.15 | Self-Di... |
| ρl | 1162.90 | kg/m3 | 333.15 | Density... |
| ρl | 1123.99 | kg/m3 | 333.15 | Excess ... |
| ρl | 1105.98 | kg/m3 | 343.15 | Excess ... |
| ρl | 1151.92 | kg/m3 | 343.15 | Self-Di... |
| ρl | 1152.30 | kg/m3 | 343.15 | Density... |
| ρl | 1088.38 | kg/m3 | 353.15 | Excess ... |
| ρl | 1141.33 | kg/m3 | 353.15 | Self-Di... |
| ρl | 1141.60 | kg/m3 | 353.15 | Density... |
| ρl | 1130.73 | kg/m3 | 363.15 | Self-Di... |
| ΔfusS | 42.80 | J/mol×K | 224.85 | NIST |
| csound,fluid | 1443.40 | m/s | 298.15 | Volumet... |
Datasets
Viscosity, Pa*s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
| 303.15 | 101.30 | 0.0021 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [365.21; 548.53] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.76786e+01 | |||
| Coefficient B | -7.84783e+03 | |||
| Coefficient C | 8.60430e+01 | |||
| Temperature range, min. | 365.21 | |||
| Temperature range, max. | 548.53 | |||
| Pvap | 1.33 | kPa | 365.21 | Calculated Property |
| Pvap | 2.83 | kPa | 385.58 | Calculated Property |
| Pvap | 5.63 | kPa | 405.95 | Calculated Property |
| Pvap | 10.61 | kPa | 426.32 | Calculated Property |
| Pvap | 19.05 | kPa | 446.69 | Calculated Property |
| Pvap | 32.78 | kPa | 467.05 | Calculated Property |
| Pvap | 54.26 | kPa | 487.42 | Calculated Property |
| Pvap | 86.76 | kPa | 507.79 | Calculated Property |
| Pvap | 134.48 | kPa | 528.16 | Calculated Property |
| Pvap | 202.66 | kPa | 548.53 | Calculated Property |
Similar Compounds
Find more compounds similar to Propylene Carbonate.
Mixtures
- Propylene Carbonate + Tetrahydrofuran
- Propylene Carbonate + 1,4-Dioxane
- Propylene Carbonate + Acetylacetone
- Propylene Carbonate + p-Xylene
- Propylene Carbonate + o-Xylene
- Propylene Carbonate + Benzene, 1,3-dimethyl-
- Benzene + Propylene Carbonate
- Propylene Carbonate + Toluene
- Propylene Carbonate + Ethylbenzene
- Propylene Carbonate + Styrene
- Propylene Carbonate + Water
- Propylene Carbonate + Methyl Alcohol
- Propylene Carbonate + sodium iodide + Methyl Alcohol
- Propylene Carbonate + sodium iodide
- Propylene Carbonate + Methane
- Propylene Carbonate + 2-Pyrrolidinone, 1-methyl-
- Diethyl carbonate + Propylene Carbonate
- Propylene Carbonate + Ethanol
- Propylene Carbonate + Ethyl Acetate
- Propylene Carbonate + n-Propyl acetate
Find more mixtures with Propylene Carbonate.
Sources
- Crippen Method
- Crippen Method
- Viscosity Behavior of Some Oxygen Containing Compounds
- Vapour pressure and enthalpy of vaporization of cyclic alkylene carbonates
- Solubilities of six lithium salts in five non-aqueous solvents and in a few of their binary mixtures
- Excess volumes and partial molar volumes of binary mixtures of 1,2-propanediol carbonate with xylene in the temperature range of (293.15 to 353.15) K
- The volumetric properties of (1,2-propanediol carbonate + benzene, or toluene, or styrene) binary mixtures at temperatures from T = 293.15 K to T = 353.15 K
- Volumetric and compressibility properties of liquid water as a solute in glycolic, propylene carbonate, and tetramethylurea solutions at T = 298.15 K
- Cyclic alkylene carbonates. Experiment and first principle calculations for prediction of thermochemical properties
- Low pressure carbon dioxide solubility in pure electrolyte solvents for lithium-ion batteries as a function of temperature. Measurement and prediction
- Density, conductivity, viscosity, and excess properties of (pyrrolidinium nitrate-based Protic Ionic Liquid + propylene carbonate) binary mixture
- Density, electrical conductivity, viscosity and excess properties of 1-butyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide + propylene carbonate binary mixtures
- Ionic molar volumes in methanol mixtures with acetonitrile, N,N-dimethylformamide and propylene carbonate at T = 298.15 K
- Low pressure methane solubility in lithium-ion batteries based solvents and electrolytes as a function of temperature. Measurement and prediction
- Volumetric and viscosimetric properties of N-methyl-2-pyrrolidone with .gamma.-butyrolactone and propylene carbonate
- Liquid-liquid equilibrium study for the system (water + phosphoric acid + propylene carbonate) at different temperatures
- Liquid-liquid equilibria for the aqueous mixture of C5 carboxylic acids and heavier than water solvents at T = 298.2 K
- Solubilities of sulfuryl fluoride in propylene carbonate, tributyl phosphate and N-methylpyrrolidone
- Isobaric Vapor Liquid Equilibria for Binary Systems of Diethyl Carbonate + Propylene Carbonate, Diethyl Carbonate + Propylene Glycol, and Ethanol + Propylene Carbonate at 101.3 kPa
- The Solubility of Hydrogen Sulfide and Carbon Dioxide in Propylene Carbonate
- Self-Diffusion Coefficients and Related Transport Properties for a Number of Fragile Ionic Liquids
- Measurement and Correlation of the Electrical Conductivity of the Ionic Liquid [BMIM][TFSI] in Binary Organic Solvents
- Isobaric Vapor-liquid Equilibrium for Three Binary Systems of Ethyl Acetate + Propyl Acetate, Ethyl Acetate + Propylene Carbonate, and Propyl Acetate + Propylene Carbonate at 101.3 kPa
- Solubilities of Sulfuryl Fluoride in 2-Butoxyethyl Acetate, 3-Methoxybutyl Acetate, 2-Methoxyethyl Acetate, 1-Methoxy-2-propyl Acetate, and 2-(2-Ethoxyethoxy)ethyl Acetate
- Vapor Pressure and Liquid Heat Capacity of Alkylene Carbonates
- Density, Viscosity, and Excess Properties of Binary Liquid Mixtures of Propylene Carbonate with Polar and Nonpolar Solvents
- Densities and Viscosities of Binary Mixtures of Paraldehyde + Propylene Carbonate at (288.15, 293.15, 298.15, 303.15, and 308.15) K
- Excess Properties of Binary Mixtures of Esters of Carbonic Acid + Three Aryl Alcohols at 308.15 K
- Vapor Pressures of Propylene Carbonate and N,N-Dimethylacetamide
- Viscosities, Ultrasonic Velocities at (288.15 and 298.15) K, and Refractive Indices at (298.15) K of Binary Mixtures of 2,4,6-Trimethyl-1,3,5-trioxane with Dimethyl Carbonate, Diethyl Carbonate, and Propylene Carbonate
- Excess Molar Enthalpies, Molar Heat Capacities, Densities, Viscosities, and Refractive Indices of Dimethyl Sulfoxide + Esters of Carbonic Acid at 308.15 K and Atmospheric Pressure
- Densities and Excess Molar Volumes for Binary Mixtures of Ionic Liquid 1-Ethyl-3-methylimidazolium Ethylsulfate with Solvents
- CO2 Capture with Physical Solvent Dimethyl Carbonate at High Pressures
- Volumes, Heat Capacities, and Compressibilities of the Mixtures of Acetonitrile with N,N-Dimethylacetamide and Propylene Carbonate
- Phase Equilibrium and Physical Properties for the Purification of Propylene Carbonate (PC) and y-Butyrolactone (GBL)
- Vapor-Liquid Equilibrium Data of the Carbon Dioxide + Ethyl Butyrate and Carbon Dioxide + Propylene Carbonate Systems at Pressures from (1.00 to 13.00) MPa and Temperatures from (313.0 to 373.0) K
- Electroconductivity of Tetraethylammonium Tetrafluoroborate in Propylene Carbonate at Various Temperatures
- Electrical Conductivity of Solutions of Ionic Liquids with Methanol, Ethanol, Acetonitrile, and Propylene Carbonate
- Comparative Study of the Solubilities of SO2 in Five Low Volatile Organic Solvents (Sulfolane, Ethylene Glycol, Propylene Carbonate, N-Methylimidazole, and N-Methylpyrrolidone)
- Liquid Liquid Equilibria for the Ternary Systems of 4-Methyl-1,3-dioxolan-2-one + 1,4-Dimethylbenzene + Octane, Decane, or Dodecane and the Ternary Systems of Acetonitrile + Morpholine + Octane, Decane, or Dodecane at 313.15 K or 298.15 K
- Determination and Correlation of Solubilities of Lithium Bis(oxalate)borate in Six Different Solvents from (293.15 to 363.15) K
- Modeling of Liquid Liquid Interfacial Properties of Binary and Ternary Mixtures
- Liquid Liquid Equilibria for the Systems: Heptane + Benzene + Solvent (Propylene carbonate, N,N-Dimethylformamide, or Mixtures) at Temperatures from (303.2 to 323.2) K
- Solubility of Methane in Propylene Carbonate
- Phase Equilibria in Binary Mixtures of Water with Cyclic Alkylene Carbonates
- Conductivities of Binary Mixtures of Ionic Liquids with Polar Solvents
- Densities, Viscosities, Refractive Indices, and Heat Capacities of Poly(ethylene glycol-ran-propylene glycol) + Esters of Carbonic Acid at (293.15 and 313.15) K and at Atmospheric Pressure
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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