623-11-0 Purity
98%
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Specification
Shiflett, Mark B.,et al. Journal of Chemical & Engineering Data, 2009, 54(1), 108-114.
The solubility of carbon dioxide (CO2) in the ionic liquids 1-ethyl-3-methylimidazolium acetate ([emim][Ac]) and 1-ethyl-3-methylimidazolium trifluoroacetate ([emim][TFA]), along with a mixture maintaining a mole ratio of 49.98 ([emim][Ac]) to 50.02 ([emim][TFA]), was investigated using a gravimetric microbalance. This was conducted at three temperatures (298.1, 323.1, and 348.1 K) and pressures reaching approximately 2 MPa.
Key Findings
· The [emim][Ac] demonstrated a strong, reversible chemical absorption of CO2, exhibiting distinctive phase behavior characterized by an asymmetrical solubility with respect to CO2 concentration.
· In contrast, [emim][TFA] displayed only physical absorption of CO2. The substantial solubility observed between CO2 and [emim][Ac] diminishes significantly when the acetate anion's methyl group (CH3-COO-) is substituted with a fluorinated methyl group (CF3-COO-), as the CF3 group withdraws electron density, decreasing the Lewis basicity of the anion and subsequently lowering CO2 solubility and the formation of chemical complexes.
· The ionic liquid mixture containing equal moles of [emim][Ac] and [emim][TFA] exhibited both chemical and physical absorption effects, with CO2 solubility accurately predicted at a fixed pressure using either a molar average of the pure component solubilities or a linear isobaric model from the ternary phase diagram. Additionally, binary pressure-temperature (PTx) data at 298.1 K was analyzed using an equation-of-state (EOS) model, yielding reasonable predictions for higher temperatures and the ternary system.
Liu, Baoyou, et al. Molecules, 2021, 26(22), 6953.
The study investigated the NO2 viscosity and absorption capacity of binary blends of 1-ethyl-3-methylidazolium trifluoroacetate ([EMIM][TFA]) and triethanolamine (TEA) at atmospheric pressure, across a temperature range of 303.15-343.15 K and various mole fractions of [EMIM][TFA]. The results indicate that the ([EMIM][TFA] + TEA) blends hold significant promise as alternative absorbents for industrial denitrification due to their effective absorption properties and low viscosity.
Key Findings
· The dependence of [EMIM][TFA] mole fraction on viscosity and absorption capacity was demonstrated.
· Introducing a small amount of [EMIM][TFA] to TEA resulted in a rapid decrease in both viscosity and absorption capacity of the blends. Nonetheless, further increases in [EMIM][TFA] beyond a certain point did not notably reduce viscosity or absorption.
· Additionally, temperature did not markedly influence viscosity and absorption capacity compared to the mole fraction of the solution.
· The optimal blend viscosity and absorption capacity were achieved at a [EMIM][TFA] mole fraction of 0.58 with results of 35.51 mPa·s viscosity and 0.7927 g·g-1 absorption capacity.
· After six cycles of absorption and desorption testing at 303.15 K the ([EMIM][TFA] + TEA) blend showed slightly decreased absorption but increased desorption.
The molecular formula is C8H11F3N2O2.
The molecular weight is 224.18 g/mol.
The synonyms include 1-ETHYL-3-METHYLIMIDAZOLIUM TRIFLUOROACETATE, 174899-65-1, MFCD08458492, and 1-ethyl-3-methylimidazol-3-ium;2,2,2-trifluoroacetate.
The component compounds are 1-Ethyl-3-methylimidazolium (CID 174076) and Trifluoroacetic Acid (CID 6422).
The IUPAC name is 1-ethyl-3-methylimidazol-3-ium;2,2,2-trifluoroacetate.
The InChI is InChI=1S/C6H11N2.C2HF3O2/c1-3-8-5-4-7(2)6-8;3-2(4,5)1(6)7/h4-6H,3H2,1-2H3;(H,6,7)/q+1;/p-1.
The InChIKey is JOKVYNJKBRLDAT-UHFFFAOYSA-M.
The canonical SMILES is CCN1C=C[N+](=C1)C.C(=O)(C(F)(F)F)[O-].
The CAS number is 174899-65-1.
The EC number is 801-288-8.
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