- 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-Propylene glycol carbonate
- 1,2-propanediyl carbonate
- 1,2-propylene carbonate
- 1-methylethylene carbonate
- 4-Methyl-1,3-dioxol-2-one
- 4-Methyldioxalone-2
- 4-methyl-1,3-dioxolan-2-one
- 4-methyl-2-oxo-1,3-dioxolane
- Arconate 5000
- Arconate propylene carbonate
- Carbonic acid cyclic methylethylene ester
- Carbonic acid, cyclic propylene ester
- Carbonic acid, propylene ester
- Dipropylene carbonate
- NSC 11784
- PC-HP
- Propylene glycol cyclic carbonate
- Propylenester kyseliny uhlicite
- Solvenon PC
- Texacar PC
- cyclic 1,2-propylene carbonate
- cyclic methylethylene carbonate
- cyclic propylene carbonate
- propylene carbonate
- ω : Acentric Factor.
- 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).
- μ : Dipole Moment (debye).
- η : Dynamic viscosity (Pa×s).
- εr : Dielectric Constant (Relative permittivity).
- Tflash,cc : Flash Point (Closed Cup Method) (K).
- 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).
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- Pc : Critical Pressure (kPa).
- Ptriple : Triple Point 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).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- λgas : Gas thermal conductivity (W/m×K).
- λliquid : Liquid thermal conductivity (W/m×K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- UQi : UNIQUAC Qi Parameter.
- URi : UNIQUAC Ri Parameter.
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- Zra : Rackett Parameter.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | [0.4107; 0.4498] |
|
|
| ω | 0.4107 | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value | |
| ω | 0.4498 | ChemSep v8.3 pure component data Compiled value | |
| 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, Heat Capacities, and Compressibilities of the Mixtures of Acetonitrile with N,N-Dimethylacetamide and Propylene Carbonate |
| μ | 4.95 | debye | ChemSep v8.3 pure component data Compiled value |
| εr | 64.92 | NCMS SOLV-DB | |
| Tflash,cc | 405.15 | K | NCMS SOLV-DB |
| ΔfG° | -455.50 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | [-601.16; -563.70] | kJ/mol |
|
| ΔfH°gas | -601.16 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| 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° | 16.60 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [30.70; 71.30] | kJ/mol |
|
| ΔvapH° | 49.79 | kJ/mol | NCMS SOLV-DB |
| 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 |
| logPoct/wat | 0.017 | NCMS SOLV-DB | |
| McVol | 69.670 | ml/mol | McGowan Calculated Property |
| Pc | [4140.00; 5410.00] | kPa |
|
| Pc | 4140.00 | kPa | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Pc | 5410.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| Ptriple | 1.17e-06 | kPa | ChemSep v8.3 pure component data Compiled value |
| 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 | 514.90 | K | ChemSep v8.3 pure component data Compiled value |
| Tboil | 514.85 | K | NCMS SOLV-DB |
| Tboil | 513.20 | K | NIST |
| Tboil | 515.05 ± 0.70 | K | NIST |
| Tc | [762.70; 778.00] | K |
|
| Tc | 762.70 | K | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Tc | 778.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | [218.62; 224.15] | K |
|
| Tfus | 224.15 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 218.62 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 218.62 | K | NCMS SOLV-DB |
| 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 | 224.85 | K | ChemSep v8.3 pure component data Compiled value |
| Ttriple | 218.66 ± 0.02 | K | NIST |
| Ttriple | 224.85 ± 0.02 | K | NIST |
| Ttriple | 224.85 ± 0.02 | K | NIST |
| Ttriple | 224.85 ± 0.02 | K | NIST |
| UQi | 3.01 | ChemSep v8.3 pure component data Compiled value | |
| URi | 3.60 | ChemSep v8.3 pure component data Compiled value | |
| Vc | [0.246; 0.250] | m3/kmol |
|
| Vc | 0.250 | m3/kmol | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Vc | 0.246 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Zc | 0.2060000 | ChemSep v8.3 pure component data Compiled value | |
| Zra | 0.24 | ChemSep v8.3 pure component data Compiled value |
Cheméo can also estimate Ionization energy, Log10 of Water solubility in mol/l for this compound, but they fall outside the models' validated range, so they are not shown here. Open the prediction tool to compute them on demand.
Temperature Dependent Properties
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 |
|---|---|---|---|---|
| Cp,gas | [100.43; 257.81] | J/mol×K | [273.00; 1500.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 5.16960e+01 | |||
| Coefficient B | -5.02590e+02 | |||
| Coefficient C | 5.74724e+00 | |||
| Coefficient D | -7.64940e-05 | |||
| Coefficient E | 1.37810e-08 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 100.43 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 140.85 | J/mol×K | 409.33 | Calculated Property |
| Cp,gas | 171.82 | J/mol×K | 545.67 | Calculated Property |
| Cp,gas | 194.94 | J/mol×K | 682.00 | Calculated Property |
| Cp,gas | 212.42 | J/mol×K | 818.33 | Calculated Property |
| Cp,gas | 225.92 | J/mol×K | 954.67 | Calculated Property |
| Cp,gas | 236.54 | J/mol×K | 1091.00 | Calculated Property |
| Cp,gas | 245.07 | J/mol×K | 1227.33 | Calculated Property |
| Cp,gas | 252.03 | J/mol×K | 1363.67 | Calculated Property |
| Cp,gas | 257.81 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [162.92; 205.38] | J/mol×K | [298.15; 425.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K | |||
| Coefficient A | 1.21750e+02 | |||
| Coefficient B | 1.05890e+02 | |||
| Coefficient C | -3.99455e-01 | |||
| Coefficient D | 1.69640e-02 | |||
| Coefficient E | -1.45770e-05 | |||
| Temperature range, min. | 298.15 | |||
| Temperature range, max. | 425.00 | |||
| Cp,liquid | 162.92 | J/mol×K | 298.15 | Calculated Property |
| Cp,liquid | 167.14 | J/mol×K | 312.24 | Calculated Property |
| Cp,liquid | 171.58 | J/mol×K | 326.34 | Calculated Property |
| Cp,liquid | 176.20 | J/mol×K | 340.43 | Calculated Property |
| Cp,liquid | 180.97 | J/mol×K | 354.53 | Calculated Property |
| Cp,liquid | 185.84 | J/mol×K | 368.62 | Calculated Property |
| Cp,liquid | 190.78 | J/mol×K | 382.72 | Calculated Property |
| Cp,liquid | 195.72 | J/mol×K | 396.81 | Calculated Property |
| Cp,liquid | 200.61 | J/mol×K | 410.91 | Calculated Property |
| Cp,liquid | 205.38 | J/mol×K | 425.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0724231; 9.3355675e-13] | Pa×s | [219.00; 622.40] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -8.18330e+02 | |||
| Coefficient B | 2.80570e+04 | |||
| Coefficient C | 1.29620e+02 | |||
| Coefficient D | -2.28120e-04 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 219.00 | |||
| Temperature range, max. | 622.40 | |||
| η | 0.0724231 | Pa×s | 219.00 | Calculated Property |
| η | 0.0055592 | Pa×s | 263.82 | Calculated Property |
| η | 0.0021322 | Pa×s | 308.64 | Calculated Property |
| η | 0.0010369 | Pa×s | 353.47 | Calculated Property |
| η | 0.0003302 | Pa×s | 398.29 | Calculated Property |
| η | 0.0000491 | Pa×s | 443.11 | Calculated Property |
| η | 0.0000029 | Pa×s | 487.93 | Calculated Property |
| η | 5.8716875e-08 | Pa×s | 532.76 | Calculated Property |
| η | 4.0802686e-10 | Pa×s | 577.58 | Calculated Property |
| η | 9.3355675e-13 | Pa×s | 622.40 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [67.92; 0.00] | kJ/mol | [224.85; 778.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K | |||
| Coefficient A | 3.14590e+02 | |||
| Coefficient B | 9.99821e+00 | |||
| Coefficient C | -2.62884e+01 | |||
| Coefficient D | 2.83829e+01 | |||
| Coefficient E | -1.14905e+01 | |||
| Critical temperature, Tc (K) | 7.78000e+02 | |||
| Temperature range, min. | 224.85 | |||
| Temperature range, max. | 778.00 | |||
| ΔvapH | 67.92 | kJ/mol | 224.85 | Calculated Property |
| ΔvapH | 60.43 | kJ/mol | 286.31 | Calculated Property |
| ΔvapH | 56.71 | kJ/mol | 347.77 | Calculated Property |
| ΔvapH | 54.38 | kJ/mol | 409.23 | Calculated Property |
| ΔvapH | 51.99 | kJ/mol | 470.69 | Calculated Property |
| ΔvapH | 48.73 | kJ/mol | 532.16 | Calculated Property |
| ΔvapH | 44.42 | kJ/mol | 593.62 | Calculated Property |
| ΔvapH | 39.35 | kJ/mol | 655.08 | Calculated Property |
| ΔvapH | 33.24 | kJ/mol | 716.54 | Calculated Property |
| ΔvapH | 0.00 | kJ/mol | 778.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [365.21; 548.53] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| 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 |
| Pvap | [1.56e-06; 5440.54] | kPa | [224.85; 778.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K | |||
| Coefficient A | 9.54122e+01 | |||
| Coefficient B | -1.05300e+04 | |||
| Coefficient C | -1.14890e+01 | |||
| Coefficient D | 5.29210e-06 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 224.85 | |||
| Temperature range, max. | 778.00 | |||
| Pvap | 1.56e-06 | kPa | 224.85 | Calculated Property |
| Pvap | 2.67e-03 | kPa | 286.31 | Calculated Property |
| Pvap | 0.23 | kPa | 347.77 | Calculated Property |
| Pvap | 4.35 | kPa | 409.23 | Calculated Property |
| Pvap | 33.38 | kPa | 470.69 | Calculated Property |
| Pvap | 149.57 | kPa | 532.16 | Calculated Property |
| Pvap | 476.72 | kPa | 593.62 | Calculated Property |
| Pvap | 1218.60 | kPa | 655.08 | Calculated Property |
| Pvap | 2697.44 | kPa | 716.54 | Calculated Property |
| Pvap | 5440.54 | kPa | 778.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [1274.39; 415.03] | kg/m3 | [224.85; 778.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K | |||
| Coefficient A | 1.14543e+02 | |||
| Coefficient B | 2.75990e-01 | |||
| Coefficient C | 7.78000e+02 | |||
| Coefficient D | 4.03440e-01 | |||
| Temperature range, min. | 224.85 | |||
| Temperature range, max. | 778.00 | |||
| ρl | 1274.39 | kg/m3 | 224.85 | Calculated Property |
| ρl | 1209.74 | kg/m3 | 286.31 | Calculated Property |
| ρl | 1143.73 | kg/m3 | 347.77 | Calculated Property |
| ρl | 1075.92 | kg/m3 | 409.23 | Calculated Property |
| ρl | 1005.64 | kg/m3 | 470.69 | Calculated Property |
| ρl | 931.86 | kg/m3 | 532.16 | Calculated Property |
| ρl | 852.82 | kg/m3 | 593.62 | Calculated Property |
| ρl | 764.99 | kg/m3 | 655.08 | Calculated Property |
| ρl | 658.98 | kg/m3 | 716.54 | Calculated Property |
| ρl | 415.03 | kg/m3 | 778.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.01; 0.07] | W/m×K | [274.00; 1000.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·T^B / (1 + C/T + D/T²) Y is λgas in W/m×K, T in K | |||
| Coefficient A | 1.74160e-04 | |||
| Coefficient B | 9.48570e-01 | |||
| Coefficient C | 6.59280e+02 | |||
| Coefficient D | 1.63640e+04 | |||
| Temperature range, min. | 274.00 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.01 | W/m×K | 274.00 | Calculated Property |
| λgas | 0.02 | W/m×K | 354.67 | Calculated Property |
| λgas | 0.02 | W/m×K | 435.33 | Calculated Property |
| λgas | 0.03 | W/m×K | 516.00 | Calculated Property |
| λgas | 0.03 | W/m×K | 596.67 | Calculated Property |
| λgas | 0.04 | W/m×K | 677.33 | Calculated Property |
| λgas | 0.05 | W/m×K | 758.00 | Calculated Property |
| λgas | 0.06 | W/m×K | 838.67 | Calculated Property |
| λgas | 0.06 | W/m×K | 919.33 | Calculated Property |
| λgas | 0.07 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λliquid | [0.23; 0.16] | W/m×K | [224.85; 514.85] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is λliquid in W/m×K, T in K | |||
| Coefficient A | -9.62410e-02 | |||
| Coefficient B | 6.78320e+00 | |||
| Coefficient C | -1.03850e+00 | |||
| Coefficient D | -3.28410e-04 | |||
| Coefficient E | -6.97820e-07 | |||
| Temperature range, min. | 224.85 | |||
| Temperature range, max. | 514.85 | |||
| λliquid | 0.23 | W/m×K | 224.85 | Calculated Property |
| λliquid | 0.22 | W/m×K | 257.07 | Calculated Property |
| λliquid | 0.21 | W/m×K | 289.29 | Calculated Property |
| λliquid | 0.21 | W/m×K | 321.52 | Calculated Property |
| λliquid | 0.20 | W/m×K | 353.74 | Calculated Property |
| λliquid | 0.19 | W/m×K | 385.96 | Calculated Property |
| λliquid | 0.18 | W/m×K | 418.18 | Calculated Property |
| λliquid | 0.17 | W/m×K | 450.41 | Calculated Property |
| λliquid | 0.16 | W/m×K | 482.63 | Calculated Property |
| λliquid | 0.16 | W/m×K | 514.85 | Calculated Property |
Similar Compounds
Find more compounds similar to 1,3-Dioxolan-2-one, 4-methyl-.
Mixtures
- 1,3-Dioxolan-2-one, 4-methyl- + Water
- Benzene + 1,3-Dioxolan-2-one, 4-methyl-
- 1,3-Dioxolan-2-one, 4-methyl- + Toluene
- 1,3-Dioxolan-2-one, 4-methyl- + Benzene, ethyl-
- 1,3-Dioxolan-2-one, 4-methyl- + Styrene
- 1,3-Dioxolan-2-one, 4-methyl- + Methyl Alcohol
- 1,3-Dioxolan-2-one, 4-methyl- + sodium iodide + Methyl Alcohol
- 1,3-Dioxolan-2-one, 4-methyl- + sodium iodide
- 1,3-Dioxolan-2-one, 4-methyl- + Lithium fluoride
- 1,3-Dioxolan-2-one, 4-methyl- + Lithium fluoride + Water
- 1,3-Dioxolan-2-one, 4-methyl- + Carbon dioxide
- 1,3-Dioxolan-2-one, 4-methyl- + 2-Pyrrolidinone, 1-methyl-
- 1,3-Dioxolan-2-one, 4-methyl- + p-Xylene
- 1,3-Dioxolan-2-one, 4-methyl- + o-Xylene
- 1,3-Dioxolan-2-one, 4-methyl- + Benzene, 1,3-dimethyl-
- 1,3-Dioxolan-2-one, 4-methyl- + Water + Phosphoric Acid
- 1,3-Dioxolan-2-one, 4-methyl- + Pentanoic acid + Water
- 1,3-Dioxolan-2-one, 4-methyl- + Pentanoic acid, 4-oxo- + Water
- 1,3-Dioxolan-2-one, 4-methyl- + Methane
- 1,3-Dioxolan-2-one, 4-methyl- + lithium bromide
Find more mixtures with 1,3-Dioxolan-2-one, 4-methyl-.
Sources
- Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
- PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
- ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
- Crippen Method
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- Thermodynamic of LiF dissolution in alkylcarbonates and some of their mixtures with water
- 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
- Determination of solvation and specific interaction enthalpies of adamantane derivatives in aprotic solvents
- 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
- Water as a solute in aprotic dipolar solvents. 2. D2O-H2O solute isotope effects on the enthalpy of water dissolution in nitromethane, acetonitrile and propylene carbonate at 298.15 K
- Solution Enthalpies of 1,4-Dioxane: Study of Solvent Effects Through Quantitative Structure-Property Relationships
- Examination of hydrogen-bonding interactions between dissolved solutes and alkylbenzene solvents based on Abraham model correlations derived from measured enthalpies of solvation
- Use of quantitative structure property relationships to study the solvation process of 18-crown-6
- Thermodynamics of hydrogen bonding and van der Waals interactions of organic solutes in solutions of imidazolium based ionic liquids: "structure-property" relationships
- 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
- Vapor Pressures and Thermophysical Properties of Ethylene Carbonate, Propylene Carbonate, -Valerolactone, and -Butyrolactone
- 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
- Enthalpies of Solution of 1-Butyl-3-methylimidazolium Tetrafluoroborate in 15 Solvents at 298.15 K
- Joback Method
- McGowan Method
- NIST Webbook
- NCMS SOLV-DB
- The Yaws Handbook of Vapor Pressure
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