- InChI
- InChI=1S/C8H15NO2/c1-7(2)8(10)11-6-5-9(3)4/h1,5-6H2,2-4H3
- InChI Key
- JKNCOURZONDCGV-UHFFFAOYSA-N
- Formula
- C8H15NO2
- SMILES
- C=C(C)C(=O)OCCN(C)C
- Molecular Weight1
- 157.21
- CAS
- 2867-47-2
- Other Names
-
- 2-(N,N-Dimethylamino)ethyl methacrylate
- 2-(dimethylamino)ethyl methacrylate
- 2-(dimethylamino)ethyl methylpropenoate
- 2-Dimethylaminoethylester kyseliny methakrylove
- 2-Propenoic acid, 2-methyl-, 2-(dimethylamino)ethyl ester
- 2-methyl-2-propenoic acid 2-(dimethylamino)ethyl ester
- Ageflex FM-1
- DMAEMA
- Ethanol, 2-(dimethylamino)-, methacrylate
- N,N-(Dimethylamino)ethyl methacrylate
- N,N-Dimethylethanolamine methacrylate
- NSC 20959
- UN 2522
- USAF RH-3
- methacrylic acid, 2-(dimethylamino)ethyl ester
- methylpropenoic acid, 2-(dimethylamino)ethyl ester
- «beta»-(Dimethylamino)ethyl methacrylate
- «beta»-(N,N-Dimethylamino)ethyl methacrylate
- ω : Acentric Factor.
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- 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).
- ρl : Liquid Density (kg/m3).
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- 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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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.5081 | Relay (1.0) Calculated Property | |
| ΔfG° | -27.37 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -328.25 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 19.69 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 52.76 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 8.45 | eV | Relay (1.0) Calculated Property |
| log10WS | -0.04 | Relay (1.0) Calculated Property | |
| logPoct/wat | 0.667 | Crippen Calculated Property | |
| McVol | 136.700 | ml/mol | McGowan Calculated Property |
| Pc | 2784.72 | kPa | Joback Calculated Property |
| Tboil | 460.20 | K | NIST |
| Tc | 631.79 | K | Relay (1.0) Calculated Property |
| Tfus | 237.70 ± 0.20 | K | NIST |
| Vc | 0.513 | m3/kmol | Relay (1.0) Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [294.36; 362.89] | J/mol×K | [467.73; 647.71] | 
|
| Cp,gas | 294.36 | J/mol×K | 467.73 | Joback Calculated Property |
| Cp,gas | 307.11 | J/mol×K | 497.73 | Joback Calculated Property |
| Cp,gas | 319.31 | J/mol×K | 527.72 | Joback Calculated Property |
| Cp,gas | 330.98 | J/mol×K | 557.72 | Joback Calculated Property |
| Cp,gas | 342.12 | J/mol×K | 587.72 | Joback Calculated Property |
| Cp,gas | 352.76 | J/mol×K | 617.71 | Joback Calculated Property |
| Cp,gas | 362.89 | J/mol×K | 647.71 | Joback Calculated Property |
| ΔfusH | [16.85; 16.85] | kJ/mol | [237.70; 237.70] |
|
| ΔfusH | 16.85 | kJ/mol | 237.70 | NIST |
| ΔfusH | 16.85 | kJ/mol | 237.70 | NIST |
| ΔvapH | 48.80 | kJ/mol | 416.00 | NIST |
| ΔfusS | 70.90 | J/mol×K | 237.70 | NIST |
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 293.15 | 100.00 | 933.13 |
| 293.15 | 5000.00 | 936.87 |
| 293.15 | 10000.00 | 940.43 |
| 293.15 | 15000.00 | 943.83 |
| 293.15 | 20000.00 | 947.11 |
| 293.15 | 25000.00 | 950.3 |
| 293.15 | 30000.00 | 953.43 |
| 293.15 | 35000.00 | 956.52 |
| 303.15 | 100.00 | 923.03 |
| 303.15 | 5000.00 | 926.88 |
| 303.15 | 10000.00 | 930.61 |
| 303.15 | 15000.00 | 934.24 |
| 303.15 | 20000.00 | 937.79 |
| 303.15 | 25000.00 | 941.28 |
| 303.15 | 30000.00 | 944.74 |
| 303.15 | 35000.00 | 948.19 |
| 313.15 | 100.00 | 914.01 |
| 313.15 | 5000.00 | 917.99 |
| 313.15 | 10000.00 | 921.97 |
| 313.15 | 15000.00 | 925.87 |
| 313.15 | 20000.00 | 929.71 |
| 313.15 | 25000.00 | 933.48 |
| 313.15 | 30000.00 | 937.2 |
| 313.15 | 35000.00 | 940.87 |
| Reference | ||
Similar Compounds
Find more compounds similar to (Dimethylamino)ethyl methacrylate.
Mixtures
- (Dimethylamino)ethyl methacrylate + Methyl Alcohol
- (Dimethylamino)ethyl methacrylate + Ethanol
- 1-Propanol + (Dimethylamino)ethyl methacrylate
- (Dimethylamino)ethyl methacrylate + 1-Butanol
- (Dimethylamino)ethyl methacrylate + 1-Pentanol
- (Dimethylamino)ethyl methacrylate + Carbon dioxide
Sources
- Cheméo Relay (1.0)
- Crippen Method
- Crippen Method
- Effect of cosolvent on the phase behavior of binary and ternary mixture for the poly(2- dimethylaminoethyl methacrylate) in supercritical solvents
- Density and Derived Properties of Binary Mixtures Containing {2-(Dimethylamino)ethyl Methacrylate + Alcohols} at Temperatures from T = (293.15 to 313.15) K and Pressures of up to 35 MPa
- Joback Method
- McGowan Method
- NIST Webbook
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