- InChI
- InChI=1S/C6H15NO3/c8-4-1-7(2-5-9)3-6-10/h8-10H,1-6H2
- InChI Key
- GSEJCLTVZPLZKY-UHFFFAOYSA-N
- Formula
- C6H15NO3
- SMILES
- OCCN(CCO)CCO
- Molecular Weight1
- 149.19
- CAS
- 102-71-6
- Other Names
-
- 2,2',2''-Nitrilotriethanol
- 2,2',2''-Nitrilotris[ethanol]
- 2,2',2''-nitrilotris-ethanol
- 2,2',2-Nitrilotris(ethanol)
- Alkanolamine 244
- DALTOGEN
- Ethanol, 2,2',2''-nitrilotri-
- Ethanol, 2,2',2''-nitrilotris-
- N(CH2CH2OH)3
- NSC 36718
- Nitrilo-2,2',2"-triethanol
- Nitrilotriethanol
- Sterolamide
- Sting-Kill
- TEA
- TRIETHYLOLAMINE
- TROLAMINE
- Tea (amino alcohol)
- Teoa
- Thiofaco T-35
- Tri(hydroxyethyl)amine
- Triaethanolamin-NG
- Triethanolamin
- Triethylamine, 2,2',2''-trihydroxy-
- Trihydroxytriethylamine
- Tris(2-hydroxyethyl)amine
- Tris(beta-hydroxyethyl)amine
- Tris(«beta»-hydroxyethyl)amine
- Tris(«beta»-hydroxyethyl)amine
- Trola
- 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).
- 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).
- NFPA Fire : NFPA Fire Rating.
- NFPA Health : NFPA Health Rating.
- NFPA Safety : NFPA Safety Rating.
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρl : Liquid Density (kg/m3).
- csound,fluid : Speed of sound in fluid (m/s).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tboilr : Boiling point at reduced pressure (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 |
|---|---|---|---|
| ΔcH°liquid | -3840.60 ± 1.50 | kJ/mol | NIST |
| ΔfG° | -300.04 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -558.30 ± 2.70 | kJ/mol | NIST |
| ΔfH°liquid | -664.20 ± 1.50 | kJ/mol | NIST |
| ΔfusH° | 26.58 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 105.90 ± 2.20 | kJ/mol | NIST |
| IE | [7.90; 8.70] | eV |
|
| IE | 7.90 | eV | NIST |
| IE | 8.70 | eV | NIST |
| log10WS | 1.31 | Crippen Calculated Property | |
| logPoct/wat | -1.735 | Crippen Calculated Property | |
| McVol | 122.990 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 1 | KDB | |
| NFPA Health | 1 | KDB | |
| NFPA Safety | 1 | KDB | |
| Pc | 4328.25 | kPa | Joback Calculated Property |
| Tboil | 608.55 | K | NIST |
| Tc | 782.14 | K | Joback Calculated Property |
| Tfus | [294.40; 294.75] | K |
|
| Tfus | 294.75 | K | NIST |
| Tfus | 294.72 ± 0.10 | K | NIST |
| Tfus | 294.40 ± 0.60 | K | NIST |
| Vc | 0.447 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [335.83; 379.07] | J/mol×K | [625.66; 782.14] |
|
| Cp,gas | 335.83 | J/mol×K | 625.66 | Joback Calculated Property |
| Cp,gas | 343.87 | J/mol×K | 651.74 | Joback Calculated Property |
| Cp,gas | 351.56 | J/mol×K | 677.82 | Joback Calculated Property |
| Cp,gas | 358.91 | J/mol×K | 703.90 | Joback Calculated Property |
| Cp,gas | 365.94 | J/mol×K | 729.98 | Joback Calculated Property |
| Cp,gas | 372.65 | J/mol×K | 756.06 | Joback Calculated Property |
| Cp,gas | 379.07 | J/mol×K | 782.14 | Joback Calculated Property |
| Cp,liquid | 389.00 | J/mol×K | 298.15 | NIST |
| η | [0.0379400; 0.3982000] | Pa×s | [303.15; 343.15] |
|
| η | 0.3982000 | Pa×s | 303.15 | Density... |
| η | 0.1959000 | Pa×s | 313.15 | Density... |
| η | 0.1036000 | Pa×s | 323.15 | Density... |
| η | 0.0608100 | Pa×s | 333.15 | Density... |
| η | 0.0379400 | Pa×s | 343.15 | Density... |
| ΔvapH | 79.30 | kJ/mol | 551.00 | NIST |
| Pvap | [8.35e-04; 0.51] | kPa | [365.00; 465.00] |
|
| Pvap | 8.35e-04 | kPa | 365.00 | Thermog... |
| Pvap | 2.13e-03 | kPa | 375.00 | Thermog... |
| Pvap | 5.00e-03 | kPa | 385.00 | Thermog... |
| Pvap | 0.01 | kPa | 395.00 | Thermog... |
| Pvap | 0.02 | kPa | 405.00 | Thermog... |
| Pvap | 0.04 | kPa | 415.00 | Thermog... |
| Pvap | 0.08 | kPa | 425.00 | Thermog... |
| Pvap | 0.13 | kPa | 435.00 | Thermog... |
| Pvap | 0.22 | kPa | 445.00 | Thermog... |
| Pvap | 0.34 | kPa | 455.00 | Thermog... |
| Pvap | 0.51 | kPa | 465.00 | Thermog... |
| n0 | 1.48320 | 298.15 | Density... | |
| ρl | [1101.50; 1124.30] | kg/m3 | [293.15; 333.15] |
|
| ρl | 1124.30 | kg/m3 | 293.15 | Density... |
| ρl | 1120.99 | kg/m3 | 298.15 | Densiti... |
| ρl | 1118.21 | kg/m3 | 303.15 | Densiti... |
| ρl | 1118.50 | kg/m3 | 303.15 | Density... |
| ρl | 1115.38 | kg/m3 | 308.15 | Densiti... |
| ρl | 1112.57 | kg/m3 | 313.15 | Densiti... |
| ρl | 1112.80 | kg/m3 | 313.15 | Density... |
| ρl | 1109.78 | kg/m3 | 318.15 | Densiti... |
| ρl | 1106.93 | kg/m3 | 323.15 | Densiti... |
| ρl | 1107.10 | kg/m3 | 323.15 | Density... |
| ρl | 1101.50 | kg/m3 | 333.15 | Density... |
| csound,fluid | [1570.58; 1631.10] | m/s | [288.15; 323.15] |
|
| csound,fluid | 1631.10 | m/s | 288.15 | Density... |
| csound,fluid | 1617.81 | m/s | 293.15 | Density... |
| csound,fluid | 1626.90 | m/s | 293.15 | Density... |
| csound,fluid | 1623.90 | m/s | 293.15 | Density... |
| csound,fluid | 1614.50 | m/s | 298.15 | Density... |
| csound,fluid | 1610.51 | m/s | 298.15 | Density... |
| csound,fluid | 1610.51 | m/s | 298.15 | Density... |
| csound,fluid | 1600.52 | m/s | 303.15 | Density... |
| csound,fluid | 1600.52 | m/s | 303.15 | Density... |
| csound,fluid | 1605.30 | m/s | 303.15 | Density... |
| csound,fluid | 1604.50 | m/s | 303.15 | Density... |
| csound,fluid | 1595.50 | m/s | 308.15 | Density... |
| csound,fluid | 1595.45 | m/s | 308.15 | Density... |
| csound,fluid | 1595.45 | m/s | 308.15 | Density... |
| csound,fluid | 1587.00 | m/s | 313.15 | Density... |
| csound,fluid | 1586.99 | m/s | 313.15 | Density... |
| csound,fluid | 1587.80 | m/s | 313.15 | Density... |
| csound,fluid | 1586.99 | m/s | 313.15 | Density... |
| csound,fluid | 1578.75 | m/s | 318.15 | Density... |
| csound,fluid | 1578.75 | m/s | 318.15 | Density... |
| csound,fluid | 1578.80 | m/s | 318.15 | Density... |
| csound,fluid | 1570.58 | m/s | 323.15 | Density... |
| csound,fluid | 1571.90 | m/s | 323.15 | Density... |
| csound,fluid | 1570.60 | m/s | 323.15 | Density... |
| csound,fluid | 1570.58 | m/s | 323.15 | Density... |
| γ | [0.04; 0.05] | N/m | [288.15; 343.15] |
|
| γ | 0.05 | N/m | 288.15 | Surface... |
| γ | 0.05 | N/m | 293.15 | Density... |
| γ | 0.05 | N/m | 293.15 | Surface... |
| γ | 0.05 | N/m | 298.15 | Density... |
| γ | 0.05 | N/m | 298.15 | Surface... |
| γ | 0.05 | N/m | 303.15 | Densiti... |
| γ | 0.05 | N/m | 303.15 | Surface... |
| γ | 0.05 | N/m | 303.15 | Density... |
| γ | 0.04 | N/m | 308.15 | Surface... |
| γ | 0.04 | N/m | 313.15 | Surface... |
| γ | 0.04 | N/m | 313.15 | Densiti... |
| γ | 0.05 | N/m | 313.15 | Density... |
| γ | 0.04 | N/m | 323.15 | Densiti... |
| γ | 0.04 | N/m | 323.15 | Density... |
| γ | 0.04 | N/m | 333.15 | Densiti... |
| γ | 0.04 | N/m | 343.15 | Densiti... |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 464.70 | K | 0.70 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [2.81e-07; 2423.48] | kPa | [294.35; 787.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 2.11675e+02 | |||
| Coefficient B | -2.09292e+04 | |||
| Coefficient C | -2.75376e+01 | |||
| Coefficient D | 1.02336e-05 | |||
| Temperature range, min. | 294.35 | |||
| Temperature range, max. | 787.00 | |||
| Pvap | 2.81e-07 | kPa | 294.35 | Calculated Property |
| Pvap | 2.55e-04 | kPa | 349.09 | Calculated Property |
| Pvap | 0.02 | kPa | 403.83 | Calculated Property |
| Pvap | 0.57 | kPa | 458.57 | Calculated Property |
| Pvap | 5.70 | kPa | 513.31 | Calculated Property |
| Pvap | 32.59 | kPa | 568.04 | Calculated Property |
| Pvap | 128.53 | kPa | 622.78 | Calculated Property |
| Pvap | 395.35 | kPa | 677.52 | Calculated Property |
| Pvap | 1031.90 | kPa | 732.26 | Calculated Property |
| Pvap | 2423.48 | kPa | 787.00 | Calculated Property |
Similar Compounds
![Ethanol, 2,2'-[(1-methylethyl)imino]bis-.](data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAAPoAAAD6CAIAAAAHjs1qAAAZYElEQVR4nO3de1xUZf4H8A83RRHjIoohlqHDyJCwctHlomVIGema5mUVTbxgm4oDsiaJJsZKJOtamm7WmlTbaqtl5lppbWhe1wuYICCYhXIRuchwHeZyfn8Mq2s/rjNnzjMz5/t++Y9yXuf5yuvDl+ecOed5rDiOAyHiYM26AEKEQ3EnIkJxJyJCcSciQnEnIkJxJyJCcSciQnEnIkJxJyJCcSciQnEnIkJxJyJCcSciYsu6ACJ6HIfSUlRXo1cvuLvD2fnXB2i1UKthZQU7u/bPoNFAo4GNDWxsOh+Kujth55dfsHQpBg+Gpyf8/eHjA1dX+Pvj7behVN4/7KOP0Ls3vLw6PM+SJejdGwsWdDkgdXfCyOHDmDULTU2wsoK/P4YORWsrcnJw+TJWrsSePThyBO7u/I5J3Z2wcPEipk9HUxMmTEBhIbKz8cUX+OorlJbi00/h7IzsbEyeDJWK32Ep7oSF2Fi0tiIkBF99hREj7v+7tTVmzMDXX8PODhcuYPt2foeluBPBnT6NS5cAYOtW9OrVzgHBwVi0CADFnZi/Y8cAwMsLQUEdHhMdDQA//YTr13kcmeJOBJeTAwCjR3d2zG9+A2trAMjO5nFkujNDBFdVBQCDBnV2TN++cHREXR2qq2FvDwC3bsHBof2DW1u7OTLFnQhOl86OPjO6p3dvAFAq2+JuZYU+fdo/UqOBWt2dkSnuRHAPPQQA9fVdHKZQAICTE3RLIXl4oKSk/SMXLsQHH3RnZJq7E8ENHQoAxcWdHVNSgpYWAHj0UR5HprgTwY0dCwDnz6OxscNjsrIAwM4OAQE8jkxxJ4KbOhX29mhsxJ497R+g1bbdcZ8ypcPLU71Q3IngBgxAbCwArF3b9nnTr7z2Gs6fh60t1qzhd2SKO2EhLQ1+fqirw7hxWLcOly+joQGVlTh6FJMnIzUVAFJSEBjI77B0Z4aw0LcvsrKwYAG++AKpqW35vqdfP7zxBpYt431YijthxMkJBw/i9Gl8/jkuXMCdO7C3h4cHnngCc+Y88CGURIIlS+Dq2uGpxo+HrW3bFXCnrGh9dyIeNHcngjt+HJ99xmRk6u5EWCoV/PyQn4+//x1z5gg8OHV3Iqzt25Gfj+HDMX268INTdycCqqnBiBGoqcHhw4iKEn586u5EQGvXoqYGERFMsg7q7kQ4eXnw9weA7Gz4+jIpgbo7EUp8PNRqLF/OKuug7k4Esn8/ZsyAiwuuXevsAyMjo+5OjE+pRFISAPzpTwyzDoo7EUJGBoqLIZNh8WK2hdBkhhhZaSmkUjQ04OhRTJzIthbq7sTIkpLQ0IDp05lnHdTdiXGdPYuQEPTqhdxcDB/Ouhrq7sR4OA5yOTgOiYmmkHVQdydGlJmJBQvg7o7CQvTvz7oagOJOjKWhAd7eKCvDhx9i3jzW1bShyQwxjrQ0lJUhIABz57Iu5T7q7sQIbtyAjw+USpw5gzFjWFdzH3V3YgSJiWhpwbx5JpV1UHcn/Pv+e0yYgH79UFiIhx9mXc0DqLsTPmk0mgu7drWtiGRiWQfFnfDrvffeC9q79+XQUKxaxbqWdtBkhvCmtrZWIpFUVVUdOHBg2rRprMtpB3V3wpuUlJSqqqonn3zSNLMO6u6EL/n5+X5+flqt9uLFi35+fqzLaR91d8KPhIQElUoVGxtrslkHdXfCi8OHD0+ePNnZ2fnatWsDBgxgXU6HqLsTQ7W2tiYmJgJ47bXXTDnroLgTw7399tuFhYVSqfTll19mXUsXaDJDDFJZWSmRSOrq6o4cOTJp0iTW5XSBujsxyNq1a+vq6p577jnTzzqouxND5OTkBAYGWltbX7lyxdvbm3U5XaPuTvQnl8s1Gk1cXJxZZB3U3Yne9u3bN3v27IEDBxYWFjo5ObEup1uouxN9NDc3r1mzBkBqaqq5ZB0Ud6KfzZs3//zzz/7+/gsXLmRdSw/QZIb0WGlpqbe3d2NjY1ZW1vjx41mX0wPU3UmPrV69urGxcebMmeaVdVB3Jz115syZ0NBQe3v7q1evPvroo6zL6Rnq7qQHtFqtXC7nOO6Pf/yj2WUd3enu5eXldXV1UqlUmIJEpbS09OTJky+++CLrQrqL4zgrKys3N7eCggIHBwfW5fQc16msrCxHR8cxY8ZotdrOjyR6mD17tp2dHesI9ExSUtKpU6dYf+f01EV3b2ho8Pb2Lisry8zMnD9/vmDfUzE4ffp0WFiYvb19Tk7O0KFDWZfTXXZ2djY2Nqyr0FeXPxCZmZkABg0aVFdXZ/wfP7HQaDSBgYEANmzYwLoWEek67lqtNjQ0FMCrr74qQEEisWvXLgBDhgxpaGhgXYuIdOtG5MWLF4ODg+3s7HJzc4ebxkLdZq2+vl4ikVRUVOzdu3fWrFmsyxGRbt2IDAgImDt3rlKp1D0mQQy0cePGioqKkJCQmTNnsq5FXLr7MVNFRYW3t7dCoTh69OhEE9hkx3xdv35dJpOpVKqzZ88GBQWxLkdcuvsxk7u7++rVqwHEx8er1WpjlmTh5HK5UqlcuHAhZZ2B7k/zW1padBP3nTt3GutSwtIdO3YMgKOjY1lZGetaxKgHcec4bv/+/QBcXFyqqqqMVJAFU6lUvr6+ADZv3sy6FpHqWdw5jtNN3HUPTpAe2bp1KwAvL6+WlhbWtYhUj5+IzMvL8/f3B5Cdna3rVaQ7ampqJBJJdXX1oUOHJk+ezLockerxE5EymWzx4sVqtTo+Pt4YBVmq5OTk6urqp556irLOkD7Pu99rVIcPH46KijJGWRaGfiWaCH2ed3dxcUlOTsZ/76nxXZIF0t29XbZsGWWdMf2m/CqVSiaTAcjIyODzUsISHThwAHQ7yzToGXfuf24hl5eX81iQhVEqlSNGjADwzjvvsK6FcPq/vBcREREVFVVfX79+/XqeftNYoIyMjKKiIh8fn9jYWNa1EMNezS4uLvb19VWpVOfOndM9vU3+1+3btyUSiUKh+OabbyIjI1mXQwx7NXv48OHLli2797ouXzVZjOTkDQqFYurUqZR1U2HgZKiurs7d3R3Avn37eJhbWZBz5zhX1ztPPrmsuLiYdS2kjaELb/Tv3z8lJQVAYmJiU1MTDz9/FoHjsGoVqqsHjB273cvLi3U5pA0P68wsXrw4MDDw5s2bGRkZhp/NMnz8MU6exKBBoPdhTAo/q4idOnUqPDzc3t6+oKDAjF6qN5KmJowciZIS7NkD81lCRhT4WUUsNDT0hRdeaG5ufvXVV3k5oVnbtAklJQgIwLx5rEshD+JtjcibN29KpdLm5ubjx4+Hh4fzck5zdPMmpFI0N+PECYSFsa6GPIi3NSI9PT1XrVrFcZxcLtdqtXyd1uwkJKCpCXPnUtZNEZ8rADc3N0ul0pKSkt27d8fExPB1WjNy8iTGjUOfPsjPh+gvYUwRnysA9+nTZ9OmTQCSkpIUCgWPZzYLWi3kcnAckpIo6yaK5wWv58yZExYWdvv27bS0NH7PbPreew8XL8LTEwkJrEshHeB/O4NLly4FBQXZ2trm5ubqHgYUA4UC3t6oqMCnn2LGDNbVkA7wv53B6NGj58+f39raqluXRiQ2bEBFBUJD8cILrEshHTPKZjX3ngT8+uuvn376ad7Pb2qKiyGTQa3Gf/6DgADW1ZCOGWWzmkGDBiUlJQFISEgQw5JjcXFobcWSJZR1U2esrchaW1t9fX2Lioq2b9++bNkyYwxhIo4dQ2Qk+vdHYSHc3VlXQzplrK3IevXqlZ6eDmDdunXV1dVGGoU5lQorVgDAa69R1s2AEXfee/755yMjI2tra3VPCFukbdtQWIjhw2HRv8Ash3H3Vb169aqfnx/HcdnZ2Y8//rjxBmLizh1IJLh7F//6F559lnU1pBuMu6+qj4/P0qVLNRqNXC436kBMJCfj7l1MnEhZNxtG3zW7trZ2xIgR1dXVX3zxxZQpU4w6lpAuX0ZAAKyskJMDmYx1NaR7jL5rtrOzs25ljoSEBEtacszBARMnYvlyyro5MXp3B6BWq0ePHn3lypX09HQL+6hVrYatLesiSLcJEXcA3333XUREhKOjY2Fh4eDBgwUY0UA7dqC+Hg89hJdeauerp0/jhx8wbBhoKzEzI9iaB7qJ+8KFCwUb0RCenhzAAdyBA+189fXXOYB7+mnByyKGMfrc/Z4tW7b07t17z54958+fF2xQwy1fjro61kUQnggXdy8vr7i4OK1Wu3LlSs5Mlhxzc0N5OTZsYF0H4YlwcQewbt26wYMHnzlzZu/evUKOq7fkZNjaYts2XLrEuhTCB0Hj7ujo+PrrrwNYvXp1Y2OjkEPrRyrFwoXQaPDSSxDx6+aWQ9C4A4iJiQkKCrp169bmzZsFHlo/aWlwdcX589i5k3UpxGBC3zS2trZ+6623QkND33zzzYiICA8PD8PPaWVlzXGPGH4enSFDYGd3/68uLli/HitXYu1aTJsGc7iJSjrG5H5QZGRk3759+fov9Ov3sO6mIS9/fvyR4/57I/KbbziO49Rqzt+fA7jZs9vqpxuRZorBR4Jarfb27dtNTU1ubm4ODg6Gn9DBYRCPFwK9ev36X2xs8M47CAvD3r1YtAgREbyNRQTGIO4ffPDB5cuXhwwZUlBQwEvcBRASgpgY7N6NuDhcvsy6GqIvoS9V6+vr161bB+DNN980l6zrpKfD1RX5+Xj3XdalEH0JHffU1NTy8vLf/va3s2fPFnhoAw0YgE2bAGD9etTWsq6G6EXQuF+/fv2tt96ytrbeunWrlZWVkEPzYvFijBmD2lrs3s26FKIXQeOue+R9wYIFwcHBQo7LF2tr7NgBGxvcvcu6FKIX4eL+3XffHTp0yNHRMTU1VbBBeTd6dPuPBBOzIFDcNRpNfHw8gOTkZLN43r0TmzbRh03mSqDXO7Zt2xYXF/fYY49dvXq1d+/eAoxooCtX0NqKESPQv387X/3lF1RVoX9/iGbJVwshRNzvvZ198ODB3/3ud8YeTjB1dWhoAB+PQRCBCDGZ0S0kNmHCBEvK+okTkEgQG8u6DtITRu/ulrqyEq2pZI6M3t3j4+PVavXLL79sSVkH4OaGdesAYOVKtLayroZ0j3G7+8GDB59//nlnZ+eioiJXV1fjDcSESoXHH0dhIbZsQXw862pINxixu9/bwGPjxo2Wl3UAdnb485+B/27dQUyfEeO+ZcuWoqIi3TKRxhuFragoTJoEhYJe3zYPxprMiGe/moICjBoFjYZ2qjEDxurua9asUSgUU6dOteysA5BKsWzZ/U1ViSkzSncX216Td+9CIsGdO/jnP2nnPZPGf3fnOE4ul2u12vj4eDFkHYCTEzZuBICEBDQ1sa6GdIz/uH/yySc//PDDvc33RCI2FgEBuHkTW7awLoV0jOfJTHNzs1QqLSkp2b17d0xMDI9nNn0nT2LcOPTpg/x8DB3KuhrSHp67e1paWklJyejRo1988UV+z2z6wsIwbRqampCczLoU0gE+u/vNmzelUmlzc/Px48fDw8P5Oq0ZKSnByJFobsaJEwgLY10N+X/47O6JiYlNTU2///3vxZl1AEOHIj4eHAe5nNaUNEW8dfdTp06Fh4fb29vn5+c/8ghvS9iZnaYmjByJkhLs2QPxTehMHT/dXavVyuVyjuPWrFkj5qwD6NsXundxX3kFCgXrasiD+In7+++/f+HCBU9Pz8TERF5OaNaioxEaitu3kZ7OuhTyIB4mM/X19RKJpKKiYt++fTNpby4AwMWLCA6GrS1yc+l9VhPCQ3dPSUmpqKgICQmZMWOG4WezDAEBiI5GayuSkuiK1YQY2t2Li4t9fX1VKtW5c+cCAwP5KssClJVhxox/V1bGvfvu2xMmTGBdDgEM7+5yuVypVC5atIiy/isPP4yoqLPFxXkrVqxQq9WsyyEADNvO4NixYwAcHR3Ly8sNOY+lUiqVw4cPB7Bjxw7WtRCO4zj9465SqWQyGYCMjAweC7Iw+/fvB+Di4lJVVcW6FmJA3P/yl78A8PLyamlp4bEgyzNx4kQAut1kCVt6XqrW1NRIJJLq6uovv/zyueee43FyZXny8vL8/f0BZGdn+/r6si5H1PS8VF27dm11dXVERARlvUsymWzJkiVqtVoul7OuRez06e7UrnqKfhmaCH26u25hsOXLl1PWu8nFxUW3I5Xuvi3rckSsp5N9utWgH5VKpesOmzdvZl2LePUs7i0tLbobyTt37jRSQRbs3scUZWVlrGsRqZ5NZjIyMoqLi2Uy2eLFi43wm8bC6a7s6+vr169fz7oWkerBpWpFRYW3t7dCoTh69KjuXjLpqevXr8tkMpVKdfbs2aCgINbliE4Puvvq1asVCsX06dMp63rz8vJasWLFvbdhWJcjOt3t7hcvXgwODrazs8vNzdVN34l+7r0esHfv3lmzZrEuR1y61d05jlu5cqVWq121ahVl3UCOjo4bN24EkJiY2NjYyLockenO9WxmZiaAQYMG1dXVGfO6WSw0Go3ueekNGzawrkVcup7MNDQ0eHt7l5WVZWZmzp8/X4gfQRE4ffp0WFgYLdwgsK4nM2lpaWVlZQEBAdHR0QIUJBIhISEzZ85sbm4W1UqazHXR3W/cuOHj46NUKk+cOBFG62Lx6tatW1KptLGxMT09XffmgFmQSqVeXl6sq9BX53OdvLy8sWPHRkdHCzGxEp/169eb3UwmOjp6+/btrL9zeup67s5xXFNTk4ODgzDfTVFpaWkpKipas2YN60K6q76+/uTJk+Z7ySHEJvHEksydO/eTTz6ZOXPmvn37WNfSYxR30jOlpaXe3t6NjY1ZWVnjx49nXU7PGH3XbGJhPDw8dNvlyuVyjUbDupyeoe5Oeqy5udnHx+fnn3/etWvXkiVLWJfTAxR3oo99+/bNnj174MCBhYWFTk5OrMvpLprMEH3MmjVr/PjxlZWVqbrlvc0EdXeip5ycnMDAQBsbmx9//NHb25t1Od1C3Z3oyd/fPyYmprW11YwW9afuTvRXWVkpkUjq6uqOHDkyadIk1uV0jbo70d/AgQOTk5MBJCQkqFQq1uV0jeJODBIXFyeRSAoKCnbs2MG6lq7RZIYY6ssvv5wyZYqzs/O1a9cGDBjAupzOUHcnhpo8efIzzzxTW1tr+guKUHcnPMjPz/fz89NqtZcuXRo1ahTrcjpE3Z3wYOTIkX/4wx80Go2Jr3JM3Z3wo7a2ViKRVFVVHThwYNq0aazLaR91d8IPZ2fnlJQUAImJiS0tLazLaR/FnfBm6dKlo0aNunHjhm4jIxNEcSe8sbGx0QW99tAhlJezLqcdNHcnPPtpxYrHtm/H/PnIzGRdy69R3AnffvoJMhmUSpw5gzFjWFfzAJrMEL499hji48FxkMthYs2UujsxgoYGeHujrAwffoh581hXcx91d2IE/fph0yYASEpCQwPrau6juBPjmD8fwcEoLUV6OutS7qPJDDGas2cREoJevZCbC9PYFoC6OzGasWMxdy6USpjMKsfU3YkxlZZCKkVDA44ehQls6UXdnRiThwdeeQUA4uOhVrOuhuJOjC0xEcOGIS8Pf/sb61JoMkMEsH8/ZsyAiwuKiuDiwrAQ6u7E+F54AU88gZoasF5yjLo7EUReHvz9ASAnB+x25qHuTgQhk2HRIqjVYPp2H3V3IpSaGowYgZoaHD6MqCgmJVB3J0JxcUFyMgDI5VAqmZRAcScCWrECMhmKi/HOO0zGp8kMEdaxY4iMRP/+KCyEu7vAg1N3J8KaOBHPPguFAn/9q/CDU3cngissRFYWFi+GjY3AI1PciYjYsi6AiNvx4/j8c1y6hOpq9OoFDw+Eh2POHHh6PnDMtm1wc8POne2fZMcO/PvfGD8eK1Z0MZyQO9ITcl9lJTdxIge088fenktN5bTatiP37OEAztOzw1PFxHAAFx3d5Zh0qUpYUCgwbhyOHUP//khJQW4uGhpw5w6+/RZTp6KlBcnJbU8O84riTlhISEBBAVxdcfo01q+HTAYHBwwYgKeewuefY+NGAMjIwPff8zssxZ0IrrQUH34IAJs3t/+4WHIywsLAcXjjDX5HprgTwR08CJUKTk6YM6f9A6ys2i46v/0WtbU8jkxxJ4I7dw4AgoPRu3eHx4wbBwBaLc6f53FkuhFJBFdWBgDDhnV2jLs7HBzQ2IjSUlhbA0BNDZYsaf/gU6e6OTLFnQhOoQAAB4cuDuvXD42NUCjg5AQAjY14/30DR6a4E8Hpgt7lDh9NTQDQr1/bX93c8PHH7R+5ZQu++aY7I1PcieB0e6/qpjQdUSjaFpd0c2u7WrW3R2Rk+wfv3dvNkelSlQguIAAALlzobDnse1/VHcwTijsR3DPPAMCtW/jhhw6P+egjABg1Ch4ePI5McSeC8/dHeDgAxMejubmdA06daov7ypX8jkxxJyzs3Al7e1y6hMhI5Off/3etFv/4B6KioNHgiSewYAG/w9KlKmFBJsPhw5g2DSdPwscHvr4YNgwtLcjJwZ07ABAejs8+a7vjzh+KO2HkqadQUIBNm/DZZ8jNRW4uAFhbIygIsbGIibn/rpOdHRwcOrtPb28PBwfY23c5Jr3NRExAeTnu3Gl7vcPR0XjjUNyJiNClKhERijsREYo7ERGKOxERijsREYo7ERGKOxERijsREYo7ERGKOxERijsREYo7ERGKOxGR/wMPebeKfM3UHAAAAABJRU5ErkJggg==)
Find more compounds similar to Triethanolamine.
Mixtures
- 2-Pyrrolidinone, 1-methyl- + Triethanolamine
- 2-Propanol, 1-amino- + Triethanolamine + Water
- Triethanolamine + 1-Propanol, 3-amino- + Water
- Triethanolamine + Water
- Triethanolamine + Ethanol, 2-(methylamino)- + Water
- Ethanol, 2-(ethylamino)- + Triethanolamine + Water
- Carbon dioxide + Triethanolamine + Water
- Triethanolamine + Water + Thiophene, tetrahydro-, 1,1-dioxide
- 1-Ethyl-2-pyrrolidinone + Triethanolamine
- Ethanol, 2-(2-butoxyethoxy)- + Triethanolamine
- 2-Propanol, 2-methyl- + Triethanolamine
- 2-Propanol, 2-methyl- + Triethanolamine + Water
- Ethanol + Triethanolamine
- Ethanol + Triethanolamine + Water
- Monoethanolamine + Triethanolamine
- 2-Propanol, 1-amino-, (R)- + Triethanolamine
- Triethanolamine + 1-Propanol, 3-amino-
- Choline chloride + Triethanolamine
- n-Hexane + Triethanolamine
- n-Hexane + Choline chloride + Triethanolamine
Find more mixtures with Triethanolamine.
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Crippen Method
- Density, transport properties and electrochemical potential windows for the 2-hydroxy-N,N,N-trimethylethanaminium chlorides based ionic liquids at several temperatures
- Effective extraction of benzene and thiophene by novel deep eutectic solvents from hexane / aromatic mixture at different temperatures
- Solubility of CO2 in the solvent system (water + monoethanolamine + triethanolamine)
- Density, speed of sound, viscosity, refractive index and surface tension of N-methyl-2-pyrrolidone + diethanolamine (or triethanolamine) from T = (293.15 to 323.15) K
- Excess molar enthalpies for binary mixtures of different amines with water
- Density and viscosity measurements of aqueous amines at high pressures: DEA-water, DMAE-water and TEA-water mixtures
- CO2 absorption with aqueous tertiary amine solutions: Equilibrium solubility and thermodynamic modeling
- Thermogravimetric measurement of the equilibrium vapour pressure: Application to water and triethanolamine
- Liquid-Liquid Equilibria for Benzene/Thiophene + Cyclohexane/Hexadecane + Deep Eutectic Solvents: Data and Correlation
- Surface Tension of aqueous vinary mixtures of 1-amino-2-propanol and 3-amino-1-propanol, and aqueous ternary mixtures of these amines with diethanolamine, triethanolamine, and 2-amino-2-methyl-1-propanol from (298.15 to 323.15) K
- Mutual Diffusion Coefficients of Some Aqueous Alkanolamines Solutions
- Densities and Viscosities of Aqueous Ternary Mixtures of 2-(Methylamino)ethanol and 2-(Ethylamino)ethanol with Diethanolamine, Triethanolamine, N-Methyldiethanolamine, or 2-Amino-1-methyl-1-propanol from 298.15 to 323.15 K
- Density, Viscosity, and Performances of Carbon Dioxide Capture in 16 Absorbents of Amine + Ionic Liquid + H2O, Ionic Liquid + H2O, and Amine + H2O Systems
- Effect of 2,2',2''-Nitrilotrisethanol on the Vapor-Liquid Equilibria of the Ethanol + Water System at Atmospheric Pressure
- Densities, Viscosities, and Surface Tensions of Aqueous Mixtures of Sulfolane + Triethanolamine and Sulfolane + Diisopropanolamine
- Density, Speed of Sound, Refractive Index, and Viscosity of 1-Amino-2-Propanol {or Bis(2-hydroxypropyl)amine} + Triethanolamine + Water from T = (288.15 to 333.15) K
- Density, Speed of Sound, Viscosity, Surface Tension, and Excess Volume of N-Ethyl-2-pyrrolidone + Ethanolamine (or Diethanolamine or Triethanolamine) from T = (293.15 to 323.15) K
- Density and Viscosity for Binary Mixtures of Diethylene Glycol Monobutyl Ether with Monoethanolamine, Diethanolamine, and Triethanolamine from (293.15 to 333.15) K
- Bubble Point Determination for CO2 + Ethanol + Alkanolamines (Monoethanolamine, Diethanolamine, or Triethanolamine) at High Pressures
- Isobaric Vapor Liquid Equilibrium of tert-Butyl Alcohol + Water + Triethanolamine-Based Ionic Liquid Ternary Systems at 101.3 kPa
- Density and Speed of Sound of Binary Mixtures of N-Methyldiethanolamine and Triethanolamine with Ethanol
- Surface Tension of Aqueous Binary Mixtures of 2-(Methylamino)ethanol and 2-(Ethylamino)ethanol and Aqueous Ternary Mixtures of These Amines with Triethanolamine or N-Methyldiethanolamine from (293.15 to 323.15) K
- Surface Tension of Binary Mixtures of N-Methyldiethanolamine and Triethanolamine with Ethanol
- Density, Speed of Sound, and Isentropic Compressibility of Triethanolamine (or N-Methyldiethanolamine) + Water + Ethanol Solutions from t = (15 to 50) deg C
- Density, Speed of Sound, Isentropic Compressibility, and Excess Volume of (Monoethanolamine + 2-Amino-2-methyl-1-propanol), (Monoethanolamine + Triethanolamine), and (Monoethanolamine + N-Methyldiethanolamine) at Temperatures from (293.15 to 323.15) K
- Density, Speed of Sound, Isentropic Compressibility, and Excess Volume of Binary Mixtures of 1-Amino-2-propanol or 3-Amino-1-propanol with 2-Amino-2-methyl-1-propanol, Diethanolamine, or Triethanolamine from (293.15 to 323.15) K
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more. Take the time to validate and double check the source of the data.