- InChI
- InChI=1S/C3H6O3/c1-5-3(4)6-2/h1-2H3
- InChI Key
- IEJIGPNLZYLLBP-UHFFFAOYSA-N
- Formula
- C3H6O3
- SMILES
- COC(=O)OC
- Molecular Weight1
- 90.08
- CAS
- 616-38-6
- Other Names
-
- CH3OCOOCH3
- Dimethyl carbonate
- Dimethyl ester of carbonic acid
- Methyl carbonate
- Methyl carbonate ((MeO)2CO)
- UN 1161
- ω : Acentric Factor.
- PAff : Proton affinity (kJ/mol).
- BasG : Gas basicity (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).
- 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).
- IE : Ionization energy (eV).
- 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.
- ρc : Critical density (kg/m3).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Vc : Critical Volume (m3/kmol).
- 1: Molecular weight from the IUPAC atomic weights tables.
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Contents
Physical Properties
Temperature Dependent Properties
Datasets
Refractive index (Na D-line)
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Refractive index (Na D-line) - Liquid |
| 93.00 | 298.15 | 1.3664 |
| Reference | ||
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 288.15 | 100.00 | 1076.5 |
| 288.15 | 5000.00 | 1080.6 |
| 288.15 | 10000.00 | 1084.8 |
| 288.15 | 20000.00 | 1092.8 |
| 288.15 | 30000.00 | 1100.3 |
| 288.15 | 40000.00 | 1107.5 |
| 298.15 | 100.00 | 1062.9 |
| 298.15 | 5000.00 | 1068.0 |
| 298.15 | 10000.00 | 1072.1 |
| 298.15 | 20000.00 | 1080.5 |
| 298.15 | 30000.00 | 1088.5 |
| 298.15 | 40000.00 | 1095.9 |
| 308.15 | 100.00 | 1049.4 |
| 308.15 | 5000.00 | 1054.6 |
| 308.15 | 10000.00 | 1059.4 |
| 308.15 | 20000.00 | 1068.3 |
| 308.15 | 30000.00 | 1076.7 |
| 308.15 | 40000.00 | 1084.5 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 288.15 | 100.00 | 1076.83 |
| 288.15 | 5000.00 | 1081.15 |
| 288.15 | 10000.00 | 1085.32 |
| 288.15 | 15000.00 | 1089.52 |
| 288.15 | 20000.00 | 1093.35 |
| 288.15 | 25000.00 | 1096.99 |
| 288.15 | 30000.00 | 1100.63 |
| 288.15 | 35000.00 | 1104.08 |
| 288.15 | 40000.00 | 1107.4 |
| 293.15 | 100.00 | 1070.06 |
| 293.15 | 5000.00 | 1074.62 |
| 293.15 | 10000.00 | 1078.93 |
| 293.15 | 15000.00 | 1083.01 |
| 293.15 | 20000.00 | 1087.08 |
| 293.15 | 25000.00 | 1091.03 |
| 293.15 | 30000.00 | 1094.75 |
| 293.15 | 35000.00 | 1098.34 |
| 293.15 | 40000.00 | 1101.84 |
| 298.15 | 100.00 | 1063.45 |
| 298.15 | 5000.00 | 1068.0 |
| 298.15 | 10000.00 | 1072.51 |
| 298.15 | 15000.00 | 1076.72 |
| 298.15 | 20000.00 | 1080.9 |
| 298.15 | 25000.00 | 1084.89 |
| 298.15 | 30000.00 | 1088.82 |
| 298.15 | 35000.00 | 1092.44 |
| 298.15 | 40000.00 | 1096.04 |
| 303.15 | 100.00 | 1056.61 |
| 303.15 | 5000.00 | 1061.47 |
| 303.15 | 10000.00 | 1066.02 |
| 303.15 | 15000.00 | 1070.49 |
| 303.15 | 20000.00 | 1074.79 |
| 303.15 | 25000.00 | 1078.99 |
| 303.15 | 30000.00 | 1082.9 |
| 303.15 | 35000.00 | 1086.6 |
| 303.15 | 40000.00 | 1090.4 |
| 308.15 | 100.00 | 1049.91 |
| 308.15 | 5000.00 | 1054.84 |
| 308.15 | 10000.00 | 1059.69 |
| 308.15 | 15000.00 | 1064.3 |
| 308.15 | 20000.00 | 1068.73 |
| 308.15 | 25000.00 | 1073.0 |
| 308.15 | 30000.00 | 1077.1 |
| 308.15 | 35000.00 | 1080.78 |
| 308.15 | 40000.00 | 1084.38 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
| 100.00 | 283.15 | 1083.17 |
| 100.00 | 288.15 | 1076.43 |
| 100.00 | 293.15 | 1069.76 |
| 100.00 | 298.15 | 1063.1 |
| 100.00 | 303.15 | 1056.41 |
| 100.00 | 308.15 | 1049.66 |
| 100.00 | 313.15 | 1042.86 |
| 100.00 | 318.15 | 1036.04 |
| 100.00 | 323.15 | 1029.21 |
| 100.00 | 328.15 | 1022.24 |
| 5000.00 | 283.15 | 1087.33 |
| 5000.00 | 288.15 | 1080.8 |
| 5000.00 | 293.15 | 1074.22 |
| 5000.00 | 298.15 | 1067.7 |
| 5000.00 | 303.15 | 1061.17 |
| 5000.00 | 308.15 | 1054.59 |
| 5000.00 | 313.15 | 1047.94 |
| 5000.00 | 318.15 | 1041.3 |
| 5000.00 | 323.15 | 1034.63 |
| 5000.00 | 328.15 | 1027.92 |
| 10000.00 | 283.15 | 1091.39 |
| 10000.00 | 288.15 | 1085.02 |
| 10000.00 | 293.15 | 1078.58 |
| 10000.00 | 298.15 | 1072.21 |
| 10000.00 | 303.15 | 1065.82 |
| 10000.00 | 308.15 | 1059.39 |
| 10000.00 | 313.15 | 1052.91 |
| 10000.00 | 318.15 | 1046.44 |
| 10000.00 | 323.15 | 1039.95 |
| 10000.00 | 328.15 | 1033.45 |
| 15000.00 | 283.15 | 1095.34 |
| 15000.00 | 288.15 | 1089.07 |
| 15000.00 | 293.15 | 1082.76 |
| 15000.00 | 298.15 | 1076.52 |
| 15000.00 | 303.15 | 1070.29 |
| 15000.00 | 308.15 | 1064.0 |
| 15000.00 | 313.15 | 1057.67 |
| 15000.00 | 318.15 | 1051.36 |
| 15000.00 | 323.15 | 1045.04 |
| 15000.00 | 328.15 | 1038.69 |
| 20000.00 | 283.15 | 1099.13 |
| 20000.00 | 288.15 | 1093.0 |
| 20000.00 | 293.15 | 1086.83 |
| 20000.00 | 298.15 | 1080.7 |
| 20000.00 | 303.15 | 1074.59 |
| 20000.00 | 308.15 | 1068.43 |
| 20000.00 | 313.15 | 1062.22 |
| 20000.00 | 318.15 | 1056.08 |
| 20000.00 | 323.15 | 1049.91 |
| 20000.00 | 328.15 | 1043.71 |
| 25000.00 | 283.15 | 1102.79 |
| 25000.00 | 288.15 | 1096.79 |
| 25000.00 | 293.15 | 1090.73 |
| 25000.00 | 298.15 | 1084.74 |
| 25000.00 | 303.15 | 1078.74 |
| 25000.00 | 308.15 | 1072.65 |
| 25000.00 | 313.15 | 1066.6 |
| 25000.00 | 318.15 | 1060.6 |
| 25000.00 | 323.15 | 1054.58 |
| 25000.00 | 328.15 | 1048.53 |
| 30000.00 | 283.15 | 1106.39 |
| 30000.00 | 288.15 | 1100.48 |
| 30000.00 | 293.15 | 1094.5 |
| 30000.00 | 298.15 | 1088.62 |
| 30000.00 | 303.15 | 1082.75 |
| 30000.00 | 308.15 | 1076.8 |
| 30000.00 | 313.15 | 1070.82 |
| 30000.00 | 318.15 | 1064.95 |
| 30000.00 | 323.15 | 1059.07 |
| 30000.00 | 328.15 | 1053.14 |
| 35000.00 | 283.15 | 1109.85 |
| 35000.00 | 288.15 | 1104.03 |
| 35000.00 | 293.15 | 1098.19 |
| 35000.00 | 298.15 | 1092.39 |
| 35000.00 | 303.15 | 1086.6 |
| 35000.00 | 308.15 | 1080.78 |
| 35000.00 | 313.15 | 1074.93 |
| 35000.00 | 318.15 | 1069.15 |
| 35000.00 | 323.15 | 1063.39 |
| 35000.00 | 328.15 | 1057.57 |
| 40000.00 | 283.15 | 1113.17 |
| 40000.00 | 288.15 | 1107.5 |
| 40000.00 | 293.15 | 1101.74 |
| 40000.00 | 298.15 | 1096.04 |
| 40000.00 | 303.15 | 1090.35 |
| 40000.00 | 308.15 | 1084.63 |
| 40000.00 | 313.15 | 1078.87 |
| 40000.00 | 318.15 | 1073.21 |
| 40000.00 | 323.15 | 1067.56 |
| 40000.00 | 328.15 | 1061.87 |
| Reference | ||
Similar Compounds
Find more compounds similar to Carbonic acid, dimethyl ester.
Mixtures
- p-Xylene + Carbonic acid, dimethyl ester
- Carbonic acid, dimethyl ester + Decane
- p-Xylene + Carbonic acid, dimethyl ester + Decane
- Carbonic acid, dimethyl ester + Methyl Alcohol
- Carbonic acid, dimethyl ester + Water
- Carbonic acid, dimethyl ester + Methyl Alcohol + Water
- Carbonic acid, dimethyl ester + Ethanol
- Carbonic acid, dimethyl ester + Pentane, 2,2,4-trimethyl-
- Carbonic acid, dimethyl ester + Ethanol + Pentane, 2,2,4-trimethyl-
- Benzene + Carbonic acid, dimethyl ester
- Toluene + Carbonic acid, dimethyl ester
- Benzene + Carbonic acid, dimethyl ester + Ethanol
- Toluene + Carbonic acid, dimethyl ester + Ethanol
- Carbonic acid, dimethyl ester + Carbonic acid, methyl phenyl ester
- Carbonic acid, dimethyl ester + Diphenyl carbonate
- Carbonic acid, dimethyl ester + Anisole + Water
- Carbonic acid, dimethyl ester + Anisole
- Carbonic acid, dimethyl ester + Phenol
- Carbonic acid, dimethyl ester + Methyl formate
- Carbonic acid, dimethyl ester + Methylal
Find more mixtures with Carbonic acid, dimethyl ester.
Sources
- Cheméo Relay (1.0)
- Crippen Method
- Crippen Method
- Isobaric molar heat capacities of the ternary system dimethyl carbonate + p-xylene + n-decane
- Measurements of isothermal vapor-liquid equilibrium of binary methanol/dimethyl carbonate system under pressure
- Liquid liquid equlibria of the system dimethyl carbonate + methanol +water at different temperatures
- Liquid liquid equilibria of 1,3-dimethylimidazolium methyl sulfate with ketones, dialkyl carbonates and acetates
- Isothermal vapor liquid equilibrium at 333.15K and excess molar volumes and refractive indices at 298.15K for the mixtures of di-methyl carbonate, ethanol and 2,2,4-trimethylpentane
- Vapor pressures and flash points for binary mixtures of tricyclo [5.2.1.0^(2.6)] decane and dimethyl carbonate
- High-pressure phase behavior of binary and ternary mixtures containing ionic liquid [C6-mim][Tf2N], dimethyl carbonate and carbon dioxide
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
- Liquid-liquid equilibria of ternary mixtures of dimethyl carbonate, diphenyl carbonate, phenol and water at 358.15 K
- Isothermal vapor-liquid equilibrium at T = 333.15 K and excess volumes and molar refractivity deviation at T = 298.15 K for the ternary mixtures {di-methyl carbonate (DMC) + ethanol + benzene} and {DMC+ ethanol + toluene}
- Experimental determination and calculation of the critical curves for the binary systems of CO2 containing ketone, alkane, ester and alcohol, respectively
- Selection of entrainers for the separation of the binary azeotropic system methanol + dimethyl carbonate by extractive distillation
- Measurement of VLE data of carbon dioxide + dimethyl carbonate system for the direct synthesis of dimethyl carbonate using supercritical CO2 and methanol
- Isobaric vapor-liquid equilibrium for methanol + dimethylcarbonate + phosphoric-based ionic liquids
- Isobaric vapor-liquid equilibrium at 101.3 kPa and excess properties at 298.15 K for binary mixtures of methyl phenyl carbonate with methanol or dimethyl carbonate
- Solid-liquid equilibria and the physical properties of binary systems of diphenyl carbonate, dimethyl carbonate, methyl phenyl carbonate, anisole, methanol and phenol
- Ternary liquid-liquid equilibria and binary excess and deviation properties at constant temperature for mixtures of dimethyl carbonate, anisole, methanol, phenol and water
- A study on the liquid-liquid equilibrium of 1-alkyl-3-methylimidazolium dialkylphosphate with methanol and dimethyl carbonate
- The solid-liquid equilitbrium, excess molar volume and refractive deviation properties of binary systems containing dimethyl carbonate, anisole and phenol
- Isobaric vapor-liquid equilibria for binary mixtures from methyl methanoate, dimethoxymethane and dimethyl carbonate at 101.33 kPa
- Ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate: An efficient entrainer to separate methanol + dimethyl carbonate azeotropic mixture
- Separation of methanol + dimethyl carbonate azeotropic mixture using ionic liquids as entrainers
- Solubilities of six lithium salts in five non-aqueous solvents and in a few of their binary mixtures
- Effect of bis(trifluoromethylsulfonyl)imide-based ionic liquids on the isobaric vapor - liquid equilibrium behavior of ethanol + dimethyl carbonate at 101.3 kPa
- Solid-liquid equilibria and thermo-physical properties of liquid electrolyte systems for lithium ion batteries
- Measurement and correlation of the isobaric vapor-liquid equilibria of methanol + methyl carbonate + Bis(trifluoromethylsulfonyl)imide-based ionic liquidsat 101.3 kPa
- Solid-liquid equilibria for selected binary systems containing diphenyl carbonate
- Liquid-liquid measurement and correlation for separation of azeotrope (dimethyl carbonate and ethanol) with different imidazolium-based ionic liquids
- Isothermal vapor-liquid equilibria at 383.15-413.15 K for the binary system methanol + dimethyl carbonate and the pressure dependency of the azeotropic point
- Permittivity and density of binary systems of {dimethyl or diethyl carbonate} + n-dodecane from T=(288.15 to 328.15) K
- VLE of the binary systems (dimethyl carbonate with 2-propanol or 2-butanol) and (diethyl carbonate with methylcyclohexane) at 101.3 kPa
- Dynamic viscosities of the ternary liquid mixtures (dimethyl carbonate + methanol + ethanol) and (dimethyl carbonate + methanol + hexane) at several temperatures
- Excess molar enthalpies of dimethyl carbonate and (butanol isomers and 1-pentanol) at T = (298.15, 313.15, and 328.15) K and p = (0.1, 1.0, and 10.0) MPa
- Properties of ionic liquid HMIMPF6 with carbonates, ketones and alkyl acetates
- High-pressure phase equilibrium for the binary systems of {carbon dioxide (1) + dimethyl carbonate (2)} and {carbon dioxide (1) + diethyl carbonate (2)} at temperatures of 273 K, 283 K, and 293 K
- Vapour pressure and enthalpy of vaporization of aliphatic dialkyl carbonates
- Efficient determination of crystallisation and melting points at low cooling and heating rates with novel computer controlled equipment
- Density, excess volume, and excess coefficient of thermal expansion of the binary systems of dimethyl carbonate with butyl methacrylate, allyl methacrylate, styrene, and vinyl acetate at T = (293.15, 303.15, and 313.15) K
- Ebulliometric determination and prediction of (vapor + liquid) equilibria for binary and ternary mixtures containing alcohols (C1 C4) and dimethyl carbonate
- Interactions of volatile organic compounds with the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
- Low pressure carbon dioxide solubility in pure electrolyte solvents for lithium-ion batteries as a function of temperature. Measurement and prediction
- Measurement of (vapor + liquid) equilibrium for the systems {methanol + dimethyl carbonate} and {methanol + dimethyl carbonate + tetramethylammonium bicarbonate} at p = (34.43, 67.74) kPa
- Interactions of volatile organic compounds with the ionic liquids 1-butyl-1-methylpyrrolidinium tetracyanoborate and 1-butyl-1-methylpyrrolidinium bis(oxalato)borate
- Volumetric properties of dialkyl carbonate + n-alkane mixtures at high pressures: Experimental measurement and Nitta-Chao model prediction
- Low pressure carbon dioxide solubility in lithium-ion batteries based electrolytes as a function of temperature. Measurement and prediction
- Ternary (liquid + liquid) equilibria for (water + 1-propanol + dimethyl carbonate, or diethyl carbonate) systems at several temperatures
- Infinite dilution activity coefficients of volatile organic compounds in two ionic liquids composed of the tris(pentafluoroethyl) trifluorophosphate ([FAP]) anion and a functionalized cation
- Experimental and Nitta-Chao model prediction of high pressure density of p-xylene with dialkyl carbonates or n-alkanes
- Low pressure methane solubility in lithium-ion batteries based solvents and electrolytes as a function of temperature. Measurement and prediction
- Investigation of solute-solvent interactions in {1-butyl-3-methyl imidazoliumBis(trifluoromethylsulfonyl)imide + dimethylcarbonate} mixture using physicochemical properties
- Ternary liquid-liquid equilibria for systems containing (dimethyl carbonate or methyl acetate + methanol + 1-methylmidazole hydrogen sulfate) at 298.15 K and 318.15 K
- Volumetric properties of binary mixtures of ionic liquid with tributyl phosphate and dimethyl carbonate
- Density and viscosity of four binary mixtures of [C2mmim][NTf2]/[C4mmim][NTf2] + dimethyl carbonate/diethyl carbonate
- Vapour-liquid equilibrium measurements and extractive distillation process design for separation of azeotropic mixture (dimethyl carbonate + ethanol)
- Thermodynamic and spectroscopic study of binary mixtures containing {dimethyl carbonate (DMC) + alcohols} at T = (288.15-308.15) K and p = (0.1-40) MPa: Experimental study and modelling
- Thermodynamic behaviour of the binary systems dimethyl carbonate + n-octane or n-nonane
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- Determination of Ternary Liquid Liquid Equilibria for Dimethyl Carbonate + 2-Methyl-1-propanol or 2-Methyl-2-propanol + Water Systems at T = 303.15 and 313.15 K
- Separation Effects of Renewable Solvent Ethyl Lactate on the Vapor Liquid Equilibria of the Methanol + Dimethyl Carbonate Azeotropic System
- Vapor Pressures and Thermophysical Properties of Dimethyl Carbonate, Diethyl Carbonate, and Dipropyl Carbonate
- Isobaric Vapor Liquid Equilibrium Data for the Binary Systems of Dimethyl Carbonate with Xylene Isomers at 93.13 kPa
- Measurement and Correlation of the Electrical Conductivity of the Ionic Liquid [BMIM][TFSI] in Binary Organic Solvents
- Vapor-Liquid Equilibrium Data for Binary Mixtures of Dimethyl Carbonate with Methyl Acetate, Ethyl Acetate, n-Propyl Acetate, Isopropyl Acetate, n-Butyl Acetate, and Isoamyl Acetate at 93.13 kPa
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- Measurement and Correlation of Vapor-Liquid Equilibrium for Binary Systems of Dimethyl Carbonate with Butyl Butyrate, o-Xylene, and Cyclohexanone at 101.3 kPa
- Excess Molar Entalpies of Dimethyl Carbonate with o-Xylene, m-Xylene, p-Xylene, Ethylbenzene, or Ethyl Benzoate at 298.15 K
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- Densities and Excess Molar Properties of Dimethyl Carbonate with Alkanes (C6 to C10) and VLE of Dimethyl Carbonate with Alkanes (C9 to C10) at 101.3 kPa
- Vapor-Liquid Equilibria of Binary Carbon Dioxide + Alkyl Carbonate Mixture Systems
- Densities, Viscosities, and Refractive Indices of New Mixtures of Poly(ethylene glycols) + Dialkyl Carbonates at 313.15 K
- prTx Data for the Dimethyl Carbonate + Decane system
- Measurement of Isobaric Vapor - Liquid Equilibria of Dimethyl Carbonate with Acetone, 2-Butanone and 2-Pentanone at 101.3 kPa and Density and Speed of Sound at 298.15 K
- Excess Properties of Binary Mixtures of Esters of Carbonic Acid + Three Aryl Alcohols at 308.15 K
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- Isobaric Vapor-Liquid Equilibria of Binary Mixtures Containing the Carbonate Group -OCOO-
- Density, Viscosity, and Speed of Sound of Dialkyl Carbonates with Cyclopentane and Methyl Cyclohexane at Several Temperatures
- Excess Molar Enthalpies of Dimethyl Carbonate and (Methanol, Ethanol, 1-Propanol, and 2-Propanol) at T = (298.15, 313.15, and 328.15) K and p = (0.1, 1.0, and 10.0) MPa
- Excess Molar Enthalpies of the Binary Carbon Dioxide + Dimethyl Carbonate System at Temperatures of (298.15 to 308.15) K and Pressures of (5.0 to 7.5) MPa
- 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
- Ebulliometric Determination of Vapor-Liquid Equilibria for Methanol + Ethanol + Dimethyl Carbonate
- Densities and Surface Tensions of Trimethylbenzene + Dimethyl Carbonate or + Diethyl Carbonate at 298.15 K and 313.15 K
- Measurement and Correlation of Vapor-Liquid Equilibria at T ) 333.15 K and Excess Molar Volumes at T ) 298.15 K for Ethanol + Dimethyl Carbonate (DMC), DMC + 1-Propanol, and DMC + 1-Butanol
- Excess Molar Volumes at 298.15 K and Isothermal Vapor-Liquid Equilibria at 333.15 K for the Binary Mixtures of Dimethyl Carbonate with Benzene, Toluene, n-Heptane, and Isooctane
- CO2 Capture with Physical Solvent Dimethyl Carbonate at High Pressures
- Densities, Excess Molar Volumes, Isothermal Compressibilities, and Isobaric Expansivities of Dimethyl Carbonate + Cyclohexane Systems at Temperatures from (293.15 to 313.15) K and Pressures from (0.1 to 40) MPa
- Experimental Isobaric Vapor-Liquid Equilibrium for Binary Systems of Ethyl Methyl Carbonate + Methanol, + Ethanol, + Dimethyl Carbonate, or + Diethyl Carbonate at 101.3 kPa
- Density, Excess Molar Volume and Conductivity of Binary Mixtures of the Ionic Liquid 1,2-Dimethyl-3-hexylimidazolium Bis(trifluoromethylsulfonyl)imide and Dimethyl Carbonate
- Experimental Measurements and Correlations of Liquid-Liquid Equilibria for the Ternary and Quaternary Mixtures Formed by Dialkyl Carbonates at T = 298.15 K
- Solid-Liquid Equilibria in Three Binary Mixtures Containing Diphenyl Carbonate
- Measurement and Calculation of Liquid Liquid Equilibria of Ternary and Quaternary Systems Containing Water, Propan-1-ol, and 2,2,4-Trimethylpentane (TMP) with 2,2'-Oxybis(propane) (DIPE) or Dimethyl Carbonate (DMC)
- Isobaric Vapor Liquid Equilibrium for Methanol + Dimethyl Carbonate + 1-Octyl-3-methylimidazolium Tetrafluoroborate
- Organic Salt Effect of Tetramethylammonium Bicarbonate on Vapor-Liquid Equilibrium of the Dimehyl Carbonate + Methanol System
- Interactions of Volatile Organic Compounds with the Ionic Liquid 1-Butyl-1-methylpyrrolidinium Dicyanamide
- Liquid-Liquid Equilibria for the System Dimethyl Carbonate + Methanol + Glycerol in the Temperature Range of (303.15 to 333.15) K
- Surface Tension of Dialkyl Carbonates + (Alkanes or 1,4-Dimethylbenzene) and 1,4-Dimethylbenzene + Alkanes Binary Mixtures at T = 308.15 K
- Isobaric Vapor Liquid Equilibrium for Methanol + Dimethyl Carbonate + 1-Butyl-3-methylimidazolium Dibutylphosphate
- Liquid Liquid Equilibria for Ternary Mixtures of Methylphenyl Carbonate, Dimethyl Carbonate, Diphenyl Carbonate, Anisole, Methanol, Phenol, and Water at Several Temperatures
- Liquid Phase Equilibria of the Water + Acetic Acid + Dimethyl Carbonate Ternary System at Several Temperatures
- Liquid Phase Equilibria of Water + Formic Acid + Dimethyl Carbonate Ternary System at Several Temperatures
- Isobaric Vapor Liquid Equilibrium for Methanol + Dimethyl Carbonate + Trifluoromethanesulfonate-based Ionic Liquids at 101.3 kPa
- Measurements and Correlation of Liquid Liquid Equilibria of (Water + Ethanol + Dimethyl Carbonate + 2,2,4-Trimethylpentane or n-Heptane) and (Water + Dimethyl Carbonate + n-Heptane + Toluene)
- Vapor-Liquid Equilibrium Data of the Binary Systems in Oxidative Carbonylation of Dimethyl Ether Synthesizing Dimethyl Carbonate
- Analysis of Surface Tension, Density, and Speed of Sound for the Ternary Mixture Dimethyl Carbonate + p-Xylene + n-Octane
- Solubility of HFC134a (1,1,1,2-Tetrafluoroethane) in Two Dialkyl Carbonates
- Mutual Diffusion Coefficients of Diethyl Carbonate and Diethyl Adipate in Heptane at T = (278.15 to 338.15) K under Atmospheric Pressure
- 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
- Phase Behavior, Densities, and Isothermal Compressibility of (Carbon Dioxide + Dimethyl Carbonate)
- Measurements and Correlation of Liquid-Liquid Equilibria Containing Dimethyl Carbonate and Diethyl Carbonate at T = 298.15 K
- Isothermal Vapor-Liquid Equilibrium Data at T = 333.15 K and Excess Molar Volumes and Refractive Indices at T = 298.15 K for the Dimethyl Carbonate + Methanol and Isopropanol + Water with Ionic Liquids
- Joback Method
- McGowan Method
- NIST Webbook
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Outlier This icon means
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property mean.