![Ethanol, 2-[(2-aminoethyl)amino]-](data:image/png;base64, iVBORw0KGgoAAAANSUhEUgAAAPoAAAD6CAIAAAAHjs1qAAANjUlEQVR4nO3da1BU9R/H8e/uApIiKBcXRDTIUCscR8p7immTEep0YXTG2YkehGbOllNJMzSzJo2SNeP6QJNHtZPTFNNfp/WaUDo1lRKEqIRp3kgwxUBhVXbZ3e//wVlBYNUD7AX8fl7DA/fs2bM/lveePTdQw8wEIIM22AMACBzkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQVTl7nRSa2vXiXY7tbV5n99up6Ymcjo7Tbx+3ctCAO6quZlaWny7SFW5f/QRPfxw14mzZ1Nurvf5v/iCoqPp3Xc7TRw/njZt6vkAQZq2Nlq7lhITKSqKIiNp1Chat65j3fn66zRrVteHjB5NBQVqlu2vjRmtlrZsoYoKPy0eHlwGA23aRPn5dOIEHTtGa9bQxo1kMHjudTq9bFQ4HORyqVl2iE9H2iEigjIzacUKOnyYdDo/PQk8cEpL6Ztv6LvvaNEiz5S0NIqPpyVLaPlyysjo4+L9uKu6cSP9+Sd99pn/ngEeODt3kl5PCxd2mvjKKxQbSzt39n3xatfuzc302mudppw9S489dq+HJCXRe+9Rfj699BKNHNnbAQZPSUnJ6tWr3W739u3bJ0+eHOzh9IzT6Vy1atXu3bunT5/+5ZdfhoeHB3tE6pw+TSkppNF0mqjVUkoKnT7tuVlbS2+/3WkG1Xu0atfuGg1FR3f6ClHxTnn/fYqLo3feUfkk/cWNGzdMJtNzzz1XXV198uTJqVOnLl++vKGhIdjjUuvgwYPp6elFRUV1dXXffvttcnLy3r17gz0oddraaPBgL9OHDCGHw/Nvl4tstk5fzGqXzyqYTKzXd504ZQrn5Hiff9s2joz0/Hv/ftZo+NAhjo/n9evVPFswud1ui8USHx9PRBqNJjk5ecmSJSEhIUQUHR1tNpvb2tqCPcZ7qa2tNdzeq0tKSlq0aNHQoUOVm/Pnz6+urg72AO9nyRJOTfUyfexYXraMmTknh6dM6XqvXs8mk5rF+z13Zn7xRZ40iUeM4PXrubmZ8/O5qUnN0wbakSNHpk2bpsQxZcqU3377TZleU1OzYMECZfr48eP37t0b3HF6ZbPZTCaTstEyZMgQk8l069YtZnY4HGazOSoqiohCQ0ONRuO1a9eCPVhvGhqYmbdsYZ2OL17sdNe5c6zVclERc//IvamJv/6arVa225m75V5byxERTMTr1/OaNUzE0dFsNrPTqebJA+HixYsGg0Gj0RBRYmKixWJxu91d5rFarSkpKUr0WVlZf//9d1CG2p3b7S4uLk5KSlI+kbKzsy9cuNBlnqtXrxqNRp1OR0QxMTFms9nZf179f/5hg4H1er52ja9d44QEzszkGzc899ps/OyznJjIzc3M/SD3ixd5/Hhet45XreKMDOZuuTNzYaEn98pKnj2biZiIJ0zg/fvVPL8f3bx5s7CwMCIigogeeuihvLy8lpaWu81st9vNZnNkZGT7mvL69euBHG13ZWVlM2bMUN6ETz311C+//HKPmSsqKp5++mll5smTJ//0008BG6d3Nhvn53N4OBPxkCFcWsrMfOQIJyRwXBwvXMhZWRwby4mJXF7ueUgAcj9+nHfu7DrxwAE+fJiZ2W7n9jVdUhJfvsxnznSd3+Hg4mKuqfHctFo5OdkTfVYWnz2rZhS+Z7VaH759ujgrK+vcuXNqHlVfX5+bm6vVaokoISGhqKjI5XL5eaRe1NXVtQ9j5MiR6ofRu+/ax9xuLi7mMWOYiDUazs7m8+c77m1p4e3bOT+f8/P5q6/YZuu46+BB3rGj69IsFv79dzVPqyp3lWw2jo9nh0PVzHY7m808dCgTcVgYG42eD6vA6Pt6rry8fObMmcoS0tPTf/75Z3+M0yvlQ0bZBw0LCzMajc09fO169Jnme+XlPHOmZ22Xns4BfOl8lrvbzTk5vGFDzx5VV8e5uazVMhGPHMlFRezvFaUPt2KVjeYxY8YQUUZGaZc1lJ9YrTxxYlNMTJyybj7bh09GNXssPlZf3/HzTkgIxM+7M9/k7nDwypW8ciX37uUqK+MZMzzv9ief5Htuf/aen45R2Gy2tWs3xsS4le3PggK+ebPvS/WispLnzPG8SkuX/u/QoUM+Wezdjkf5mPJpHhnZ8WkejN0eH+R+6RLPnMmLF3NJCZeUcGNjbxbicvHnn3NCgmdb7tVXub7el2uakpKSx26fBPbHEWjl6IJGw0Q8ahRbLL1853t19SobjazT+eugVpezDQaD4dKlS758AquVU1I69tXOnPHlwnvCB7n/8Qfn5XV89eV7sdnYZOLwcNbpnGlpU9sPHvfFyZMnMzMzldDHjRu3Z8+ePi7wHg4d4kmTPD/WOXO4srKvC3Q42GzmqCgm4tBQNhr9eMpCOXI/aNCg9iP3ra2tfVxmVVWVaelSzzs1LY1/+MEnQ+01X+6q+sqZM2w07lICTUlJ2dF9T1ydxsbGvLy8sLAwIho+fHhhYaFdOS/gTy4XWyys1zMRa7VsMPC///ZyUSUl/PjjnjfP/Pl84oRPB3oXp0+fzs7OVl78sWPHFhcX9245DQ0NK1asUPaRji5YwFu39ofzLP0xd8WPP/44ceJE5XWfO3duVVWV+se6XC6LxRIXF0dEWq3WYDBcvnzZf0PtrqmJ8/J40CAm4ogINpm4RyvKv/7irCxP6KmpvGuX3wZ6F6WlpWlpacqL/8wzzxw7dkz9Y9va2oqKimJjY4koJCQkNze3QTlj2g/039z5drUjRozoUbV9eZ/41qlTnJ3tqfbRR1lZUZ47x/Pndz0r8uGH/MEHzJ3fJ8OGcWFhz94nPqRUq6wylGqvXLly30eVlpY+8cQTyos/b96848ePB2Co6vXr3BV3bpMMGzbsHtskXS6QslgsAR6qV3v28LhxnugzM/noUc92zp0HoF5+mbOy+PvvOTaWiVin4+XLWUVdfvfff/8ZjUblIrnhw4ff4yK5U6dO+WQryK8GQO6KO/c4U1NTd+/efee9d7tAqp9wOLioiGNjOSeHjx9nIp42jSdO5PZylNwvXODBgzkjg48eDepwu6mpqXn++efvdpGcP/Zx/WTA5K7ofjzR6XRu3ry5/SBadnZ2bW1tsIfp3ZUrfOWKJ/f9+3noUP7kE89dSu7M3J8v0bVarY888kj71Qe//vqrsrWp1+vbtzb/7fWOeUAMsNyZ2W63b9y4sf06rdDQUOUHMH369LKysmCP7v6U3Kuq+OOPOSKClYsX23Pv51pbWzds2KBcfUBEyjk7Ipo1a1ZFRUWwR3d/Ay93hXItgHICXKfTFRQUBOU6rV5oz91u5wkTePFi5oGTu6K+vl75bUaNRqPX6wNx9YGP+OsvEfhbTEzM5s2b586dW15ebjQalaM3A0tYGG3bRhkZtG9fsIfSQwkJCRUVFTt27KioqFi9erVyzHFA0LD63/MDXzhxgtLSqKqKlIOly5ZRZSWlppLLRbt2BXtwDzr8jcgg+/RTqqujAweCPQ4ZkHuQJSTQunV061awxyHDQN12H7iioig7m24f0iAievNNqq6m278HC36E3AMtPJxyckiv75gSEkJvvUWNjcEbkxjYmAm0I0fohReoy99o2rqV3ngjSAOSBLmDIMgdBEHuIAh2VYNjxoxOf/a+sZFGjw7eaMRA7sFRUEB3nnrfto3Onw/aYORA7sExbx4lJXXc3LcPuQcCtt1BEOQOgiB3EAQXAAea8n8sjxhB2jtWNS0t5HBQTEzwhiUDcgdBsDEDgiB3EAS5gyDIHQRB7iAIcgdBkDsIgtxBEOQOgiB3EAS5gyDIHQRB7iAIcgdBkDsIgtxBEOQOgiB3EAS5gyDIHQRB7iAIcgdBkDsIgtxBEOQOgiB3EAS5gyDIHQRB7iAIcgdBkDsIgtxBEOQOgiB3EAS5gyDIHQRB7iAIcgdBkDsIgtxBEOQOgiB3EAS5gyDIHQRB7iAIcgdBkDsIgtxBEOQOgiB3EAS5gyDIHQRB7iAIcgdBkDsIgtxBEOQOgiB3EAS5gyDIHQRB7iAIcgdBkDsIgtxBEOQOgiB3EAS5gyDIHQRB7iAIcgdBkDsIgtxBEOQOgiB3EAS5gyDIHQRB7iAIcgdBkDsIgtxBEOQOgiB3EAS5gyDIHQRB7iAIcgdBkDsIgtxBEOQOgiB3EAS5gyDIHQRB7iAIcgdBkDsIgtxBEOQOgiB3EAS5gyDIHQRB7iAIcgdBkDsI8n8Q/NL0uzjTsgAAAABJRU5ErkJggg== "Ethanol, 2-[(2-aminoethyl)amino]-")
- Name
- Ethanol, 2-[(2-aminoethyl)amino]-
- InChI
- InChI=1S/C4H12N2O/c5-1-2-6-3-4-7/h6-7H,1-5H2
- InChI Key
- LHIJANUOQQMGNT-UHFFFAOYSA-N
- Formula
- C4H12N2O
- SMILES
- NCCNCCO
- Mol. Weight (g/mol)
- 104.15
- CAS
- 111-41-1
- Name
- Water
- InChI
- InChI=1S/H2O/h1H2
- InChI Key
- XLYOFNOQVPJJNP-UHFFFAOYSA-N
- Formula
- H2O
- SMILES
- O
- Mol. Weight (g/mol)
- 18.02
- CAS
- 7732-18-5
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Datasets
- Mass fraction
- Cp,liquid - Molar heat capacity at constant pressure, J/K/mol (2)
- η - Viscosity, Pa*s (2)
- Excess molar enthalpy (molar enthalpy (2)
- Pvap - Vapor or sublimation pressure, kPa
- n0 - Refractive index (Na D-line) (2)
- ρl - Mass density, kg/m3
- Tboil(P) - Boiling temperature at pressure P, K
Mass fraction of Ethanol, 2-[(2-aminoethyl)amino]- (1) [ref]
Operational condition: Pressure, kPa = 86.66 (Liquid)
| Mass fraction of Ethanol, 2-[(2-aminoethyl)amino]- (1) - Liquid | Mass fraction of Ethanol, 2-[(2-aminoethyl)amino]- (1) - Gas |
|---|---|
| 0.0580 | 0.0000 |
| 0.1010 | 0.0000 |
| 0.1500 | 0.0000 |
| 0.2440 | 0.0000 |
| 0.3530 | 0.0000 |
| 0.4340 | 0.0000 |
| 0.4830 | 0.0000 |
| 0.5380 | 0.0000 |
| 0.5740 | 0.0000 |
| 0.6070 | 0.0000 |
| 0.6590 | 0.0000 |
| 0.7050 | 0.0000 |
| 0.6900 | 0.0000 |
| 0.8860 | 0.0000 |
| 0.8840 | 0.0100 |
| 0.9700 | 0.3020 |
| 0.9800 | 0.9800 |
Molar heat capacity at constant pressure, J/K/mol [ref]
Operational condition: Pressure, kPa = 100 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Molality, mol/kg of Ethanol, 2-[(2-aminoethyl)amino]- (1) - Liquid | Molar heat capacity at constant pressure, J/K/mol - Liquid |
| 304.15 | 0.5100 | 71.78 |
| 314.15 | 0.5100 | 72.70 |
| 324.15 | 0.5100 | 74.22 |
| 334.15 | 0.5100 | 77.23 |
| 304.15 | 1.07 | 73.82 |
| 314.15 | 1.07 | 74.84 |
| 324.15 | 1.07 | 75.87 |
| 334.15 | 1.07 | 78.93 |
| 304.15 | 2.4 | 78.89 |
| 314.15 | 2.4 | 80.19 |
| 324.15 | 2.4 | 81.74 |
| 334.15 | 2.4 | 84.59 |
| 304.15 | 4.11 | 84.65 |
| 314.15 | 4.11 | 85.94 |
| 324.15 | 4.11 | 87.31 |
| 334.15 | 4.11 | 91.48 |
Molar heat capacity at constant pressure, J/K/mol [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol, 2-[(2-aminoethyl)amino]- (1) - Liquid | Molar heat capacity at constant pressure, J/K/mol - Liquid |
| 303.15 | 0.0999 | 100.00 |
| 303.15 | 0.1999 | 121.00 |
| 303.15 | 0.2995 | 141.00 |
| 303.15 | 0.4000 | 161.00 |
| 303.15 | 0.5002 | 181.00 |
| 303.15 | 0.5997 | 201.00 |
| 303.15 | 0.7011 | 221.00 |
| 303.15 | 0.8003 | 240.00 |
| 303.15 | 0.8979 | 258.00 |
| 303.15 | 1.0000 | 279.00 |
| 308.15 | 0.0999 | 103.00 |
| 308.15 | 0.1999 | 125.00 |
| 308.15 | 0.2995 | 145.00 |
| 308.15 | 0.4000 | 165.00 |
| 308.15 | 0.5002 | 185.00 |
| 308.15 | 0.5997 | 205.00 |
| 308.15 | 0.7011 | 226.00 |
| 308.15 | 0.8003 | 245.00 |
| 308.15 | 0.8979 | 263.00 |
| 308.15 | 1.0000 | 284.00 |
| 313.15 | 0.0999 | 104.00 |
| 313.15 | 0.1999 | 127.00 |
| 313.15 | 0.2995 | 147.00 |
| 313.15 | 0.4000 | 167.00 |
| 313.15 | 0.5002 | 187.00 |
| 313.15 | 0.5997 | 207.00 |
| 313.15 | 0.7011 | 227.00 |
| 313.15 | 0.8003 | 247.00 |
| 313.15 | 0.8979 | 265.00 |
| 313.15 | 1.0000 | 285.00 |
| 318.15 | 0.0999 | 106.00 |
| 318.15 | 0.1999 | 129.00 |
| 318.15 | 0.2995 | 150.00 |
| 318.15 | 0.4000 | 170.00 |
| 318.15 | 0.5002 | 190.00 |
| 318.15 | 0.5997 | 209.00 |
| 318.15 | 0.7011 | 229.00 |
| 318.15 | 0.8003 | 249.00 |
| 318.15 | 0.8979 | 266.00 |
| 318.15 | 1.0000 | 286.00 |
| 323.15 | 0.0999 | 107.00 |
| 323.15 | 0.1999 | 131.00 |
| 323.15 | 0.2995 | 152.00 |
| 323.15 | 0.4000 | 172.00 |
| 323.15 | 0.5002 | 192.00 |
| 323.15 | 0.5997 | 211.00 |
| 323.15 | 0.7011 | 231.00 |
| 323.15 | 0.8003 | 250.00 |
| 323.15 | 0.8979 | 267.00 |
| 323.15 | 1.0000 | 287.00 |
| 328.15 | 0.0999 | 110.00 |
| 328.15 | 0.1999 | 134.00 |
| 328.15 | 0.2995 | 155.00 |
| 328.15 | 0.4000 | 175.00 |
| 328.15 | 0.5002 | 195.00 |
| 328.15 | 0.5997 | 214.00 |
| 328.15 | 0.7011 | 233.00 |
| 328.15 | 0.8003 | 252.00 |
| 328.15 | 0.8979 | 269.00 |
| 328.15 | 1.0000 | 289.00 |
| 333.15 | 0.0999 | 112.00 |
| 333.15 | 0.1999 | 137.00 |
| 333.15 | 0.2995 | 158.00 |
| 333.15 | 0.4000 | 178.00 |
| 333.15 | 0.5002 | 197.00 |
| 333.15 | 0.5997 | 216.00 |
| 333.15 | 0.7011 | 235.00 |
| 333.15 | 0.8003 | 254.00 |
| 333.15 | 0.8979 | 271.00 |
| 333.15 | 1.0000 | 290.00 |
| 338.15 | 0.0999 | 116.00 |
| 338.15 | 0.1999 | 141.00 |
| 338.15 | 0.2995 | 162.00 |
| 338.15 | 0.4000 | 181.00 |
| 338.15 | 0.5002 | 201.00 |
| 338.15 | 0.5997 | 219.00 |
| 338.15 | 0.7011 | 238.00 |
| 338.15 | 0.8003 | 257.00 |
| 338.15 | 0.8979 | 273.00 |
| 338.15 | 1.0000 | 292.00 |
| 343.15 | 0.0999 | 120.00 |
| 343.15 | 0.1999 | 146.00 |
| 343.15 | 0.2995 | 167.00 |
| 343.15 | 0.4000 | 185.00 |
| 343.15 | 0.5002 | 204.00 |
| 343.15 | 0.5997 | 223.00 |
| 343.15 | 0.7011 | 241.00 |
| 343.15 | 0.8003 | 260.00 |
| 343.15 | 0.8979 | 275.00 |
| 343.15 | 1.0000 | 293.00 |
| 348.15 | 0.0999 | 124.00 |
| 348.15 | 0.1999 | 152.00 |
| 348.15 | 0.2995 | 172.00 |
| 348.15 | 0.4000 | 189.00 |
| 348.15 | 0.5002 | 208.00 |
| 348.15 | 0.5997 | 227.00 |
| 348.15 | 0.7011 | 244.00 |
| 348.15 | 0.8003 | 262.00 |
| 348.15 | 0.8979 | 277.00 |
| 348.15 | 1.0000 | 295.00 |
| 353.15 | 0.0999 | 130.00 |
| 353.15 | 0.1999 | 158.00 |
| 353.15 | 0.2995 | 177.00 |
| 353.15 | 0.4000 | 194.00 |
| 353.15 | 0.5002 | 213.00 |
| 353.15 | 0.5997 | 231.00 |
| 353.15 | 0.7011 | 248.00 |
| 353.15 | 0.8003 | 265.00 |
| 353.15 | 0.8979 | 279.00 |
| 353.15 | 1.0000 | 296.00 |
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol, 2-[(2-aminoethyl)amino]- (1) - Liquid | Viscosity, Pa*s - Liquid |
| 298.15 | 0.0000 | 0.0009 |
| 298.15 | 0.0500 | 0.0024 |
| 298.15 | 0.0700 | 0.0039 |
| 298.15 | 0.0999 | 0.0068 |
| 298.15 | 0.1992 | 0.0300 |
| 298.15 | 0.3000 | 0.0709 |
| 298.15 | 0.3997 | 0.1040 |
| 298.15 | 0.4991 | 0.1210 |
| 298.15 | 0.5990 | 0.1240 |
| 298.15 | 0.6991 | 0.1210 |
| 298.15 | 0.7997 | 0.1160 |
| 298.15 | 0.9002 | 0.1090 |
| 298.15 | 1.0000 | 0.0986 |
| 303.15 | 0.0000 | 0.0008 |
| 303.15 | 0.0500 | 0.0022 |
| 303.15 | 0.0700 | 0.0032 |
| 303.15 | 0.0999 | 0.0055 |
| 303.15 | 0.1992 | 0.0226 |
| 303.15 | 0.3000 | 0.0504 |
| 303.15 | 0.3997 | 0.0728 |
| 303.15 | 0.4991 | 0.0839 |
| 303.15 | 0.5990 | 0.0870 |
| 303.15 | 0.6991 | 0.0848 |
| 303.15 | 0.7997 | 0.0825 |
| 303.15 | 0.9002 | 0.0781 |
| 303.15 | 1.0000 | 0.0705 |
| 313.15 | 0.0000 | 0.0007 |
| 313.15 | 0.0500 | 0.0016 |
| 313.15 | 0.0700 | 0.0023 |
| 313.15 | 0.0999 | 0.0038 |
| 313.15 | 0.1992 | 0.0135 |
| 313.15 | 0.3000 | 0.0278 |
| 313.15 | 0.3997 | 0.0389 |
| 313.15 | 0.4991 | 0.0448 |
| 313.15 | 0.5990 | 0.0465 |
| 313.15 | 0.6991 | 0.0457 |
| 313.15 | 0.7997 | 0.0448 |
| 313.15 | 0.9002 | 0.0444 |
| 313.15 | 1.0000 | 0.0394 |
| 323.15 | 0.0000 | 0.0006 |
| 323.15 | 0.0500 | 0.0013 |
| 323.15 | 0.0700 | 0.0018 |
| 323.15 | 0.0999 | 0.0028 |
| 323.15 | 0.1992 | 0.0087 |
| 323.15 | 0.3000 | 0.0165 |
| 323.15 | 0.3997 | 0.0225 |
| 323.15 | 0.4991 | 0.0256 |
| 323.15 | 0.5990 | 0.0267 |
| 323.15 | 0.6991 | 0.0264 |
| 323.15 | 0.7997 | 0.0260 |
| 323.15 | 0.9002 | 0.0260 |
| 323.15 | 1.0000 | 0.0234 |
| 333.15 | 0.0000 | 0.0005 |
| 333.15 | 0.0500 | 0.0010 |
| 333.15 | 0.0700 | 0.0014 |
| 333.15 | 0.0999 | 0.0021 |
| 333.15 | 0.1992 | 0.0059 |
| 333.15 | 0.3000 | 0.0105 |
| 333.15 | 0.3997 | 0.0138 |
| 333.15 | 0.4991 | 0.0158 |
| 333.15 | 0.5990 | 0.0165 |
| 333.15 | 0.6991 | 0.0165 |
| 333.15 | 0.7997 | 0.0164 |
| 333.15 | 0.9002 | 0.0165 |
| 333.15 | 1.0000 | 0.0148 |
| 343.15 | 0.0000 | 0.0004 |
| 343.15 | 0.0500 | 0.0008 |
| 343.15 | 0.0700 | 0.0011 |
| 343.15 | 0.0999 | 0.0016 |
| 343.15 | 0.1992 | 0.0042 |
| 343.15 | 0.3000 | 0.0070 |
| 343.15 | 0.3997 | 0.0091 |
| 343.15 | 0.4991 | 0.0103 |
| 343.15 | 0.5990 | 0.0108 |
| 343.15 | 0.6991 | 0.0108 |
| 343.15 | 0.7997 | 0.0108 |
| 343.15 | 0.9002 | 0.0107 |
| 343.15 | 1.0000 | 0.0101 |
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mass fraction of Ethanol, 2-[(2-aminoethyl)amino]- (1) - Liquid | Viscosity, Pa*s - Liquid |
| 293.15 | 0.0500 | 0.0012 |
| 298.15 | 0.0500 | 0.0011 |
| 303.15 | 0.0500 | 0.0009 |
| 308.15 | 0.0500 | 0.0008 |
| 313.15 | 0.0500 | 0.0008 |
| 318.15 | 0.0500 | 0.0007 |
| 323.15 | 0.0500 | 0.0006 |
| 328.15 | 0.0500 | 0.0006 |
| 333.15 | 0.0500 | 0.0006 |
| 293.15 | 0.1000 | 0.0016 |
| 298.15 | 0.1000 | 0.0014 |
| 303.15 | 0.1000 | 0.0012 |
| 308.15 | 0.1000 | 0.0011 |
| 313.15 | 0.1000 | 0.0009 |
| 318.15 | 0.1000 | 0.0008 |
| 323.15 | 0.1000 | 0.0008 |
| 328.15 | 0.1000 | 0.0007 |
| 333.15 | 0.1000 | 0.0006 |
| 293.15 | 0.1500 | 0.0020 |
| 298.15 | 0.1500 | 0.0017 |
| 303.15 | 0.1500 | 0.0015 |
| 308.15 | 0.1500 | 0.0013 |
| 313.15 | 0.1500 | 0.0012 |
| 318.15 | 0.1500 | 0.0010 |
| 323.15 | 0.1500 | 0.0009 |
| 328.15 | 0.1500 | 0.0008 |
| 333.15 | 0.1500 | 0.0007 |
| 293.15 | 0.2000 | 0.0026 |
| 298.15 | 0.2000 | 0.0022 |
| 303.15 | 0.2000 | 0.0019 |
| 308.15 | 0.2000 | 0.0016 |
| 313.15 | 0.2000 | 0.0014 |
| 318.15 | 0.2000 | 0.0012 |
| 323.15 | 0.2000 | 0.0011 |
| 328.15 | 0.2000 | 0.0009 |
| 333.15 | 0.2000 | 0.0009 |
| 293.15 | 0.2500 | 0.0035 |
| 298.15 | 0.2500 | 0.0030 |
| 303.15 | 0.2500 | 0.0024 |
| 308.15 | 0.2500 | 0.0021 |
| 313.15 | 0.2500 | 0.0018 |
| 318.15 | 0.2500 | 0.0015 |
| 323.15 | 0.2500 | 0.0013 |
| 328.15 | 0.2500 | 0.0011 |
| 333.15 | 0.2500 | 0.0010 |
| 293.15 | 0.3000 | 0.0047 |
| 298.15 | 0.3000 | 0.0040 |
| 303.15 | 0.3000 | 0.0033 |
| 308.15 | 0.3000 | 0.0026 |
| 313.15 | 0.3000 | 0.0022 |
| 318.15 | 0.3000 | 0.0019 |
| 323.15 | 0.3000 | 0.0016 |
| 328.15 | 0.3000 | 0.0014 |
| 333.15 | 0.3000 | 0.0012 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
Operational conditions:
- Temperature, K = 303.15 (Liquid)
- Pressure, kPa = 100 (Liquid)
| Mole fraction of Ethanol, 2-[(2-aminoethyl)amino]- (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.1031 | -2.316 |
| 0.2020 | -3.609 |
| 0.3019 | -4.028 |
| 0.3567 | -4.163 |
| 0.4023 | -4.006 |
| 0.4991 | -3.681 |
| 0.5997 | -3.096 |
| 0.7027 | -2.421 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol, 2-[(2-aminoethyl)amino]- (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 298.15 | 0.0298 | -0.7710 |
| 298.15 | 0.0496 | -1.273 |
| 298.15 | 0.0699 | -1.713 |
| 298.15 | 0.0992 | -2.241 |
| 298.15 | 0.1503 | -3.0 |
| 298.15 | 0.2015 | -3.447 |
| 298.15 | 0.2962 | -3.909 |
| 298.15 | 0.2982 | -3.918 |
| 298.15 | 0.3484 | -4.009 |
| 298.15 | 0.3994 | -3.955 |
| 298.15 | 0.4454 | -3.771 |
| 298.15 | 0.4962 | -3.489 |
| 298.15 | 0.5050 | -3.433 |
| 298.15 | 0.5922 | -2.865 |
| 298.15 | 0.6969 | -2.192 |
| 298.15 | 0.7700 | -1.711 |
| 298.15 | 0.9077 | -0.7790 |
| 313.15 | 0.0299 | -0.9360 |
| 313.15 | 0.0498 | -1.317 |
| 313.15 | 0.0701 | -1.72 |
| 313.15 | 0.1000 | -2.338 |
| 313.15 | 0.1495 | -3.051 |
| 313.15 | 0.2002 | -3.62 |
| 313.15 | 0.2956 | -4.119 |
| 313.15 | 0.3547 | -4.234 |
| 313.15 | 0.4001 | -4.15 |
| 313.15 | 0.4461 | -3.976 |
| 313.15 | 0.4893 | -3.784 |
| 313.15 | 0.6009 | -3.148 |
| 313.15 | 0.6723 | -2.669 |
| 313.15 | 0.7961 | -1.714 |
| 313.15 | 0.9041 | -0.8880 |
| 323.15 | 0.0301 | -0.6170 |
| 323.15 | 0.0498 | -1.029 |
| 323.15 | 0.0697 | -1.594 |
| 323.15 | 0.0992 | -2.037 |
| 323.15 | 0.1491 | -2.915 |
| 323.15 | 0.1988 | -3.414 |
| 323.15 | 0.3014 | -3.815 |
| 323.15 | 0.3527 | -3.938 |
| 323.15 | 0.3958 | -3.916 |
| 323.15 | 0.4971 | -3.6 |
| 323.15 | 0.5908 | -3.027 |
| 323.15 | 0.7056 | -2.241 |
| 323.15 | 0.7484 | -1.939 |
| 323.15 | 0.8999 | -0.8200 |
Vapor or sublimation pressure, kPa [ref]
| Fixed | Measured | |
|---|---|---|
| Mass fraction of Ethanol, 2-[(2-aminoethyl)amino]- (1) - Liquid | Temperature, K - Liquid | Vapor or sublimation pressure, kPa - Liquid |
| 0.1000 | 313.20 | 7.00 |
| 0.1000 | 328.20 | 15.00 |
| 0.1000 | 343.20 | 28.70 |
| 0.1000 | 358.20 | 51.80 |
| 0.3000 | 358.20 | 46.20 |
Refractive index (Na D-line) [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol, 2-[(2-aminoethyl)amino]- (1) - Liquid | Refractive index (Na D-line) - Liquid |
| 298.15 | 0.0000 | 1.3326 |
| 298.15 | 0.0500 | 1.3701 |
| 298.15 | 0.0700 | 1.382 |
| 298.15 | 0.1000 | 1.398 |
| 298.15 | 0.2000 | 1.4331 |
| 298.15 | 0.3000 | 1.4525 |
| 298.15 | 0.4000 | 1.4632 |
| 298.15 | 0.5000 | 1.4703 |
| 298.15 | 0.5996 | 1.475 |
| 298.15 | 0.7011 | 1.4785 |
| 298.15 | 0.8002 | 1.481 |
| 298.15 | 0.8979 | 1.4829 |
| 298.15 | 1.0000 | 1.4845 |
| 303.15 | 0.0000 | 1.332 |
| 303.15 | 0.0500 | 1.3693 |
| 303.15 | 0.0700 | 1.3811 |
| 303.15 | 0.1000 | 1.3968 |
| 303.15 | 0.2000 | 1.4318 |
| 303.15 | 0.3000 | 1.4509 |
| 303.15 | 0.4000 | 1.4616 |
| 303.15 | 0.5000 | 1.4686 |
| 303.15 | 0.5996 | 1.4732 |
| 303.15 | 0.7011 | 1.4767 |
| 303.15 | 0.8002 | 1.4792 |
| 303.15 | 0.8979 | 1.481 |
| 303.15 | 1.0000 | 1.4827 |
| 313.15 | 0.0000 | 1.3307 |
| 313.15 | 0.0500 | 1.3675 |
| 313.15 | 0.0700 | 1.3791 |
| 313.15 | 0.1000 | 1.3945 |
| 313.15 | 0.2000 | 1.4289 |
| 313.15 | 0.3000 | 1.4476 |
| 313.15 | 0.4000 | 1.4581 |
| 313.15 | 0.5000 | 1.465 |
| 313.15 | 0.5996 | 1.4696 |
| 313.15 | 0.7011 | 1.4731 |
| 313.15 | 0.8002 | 1.4755 |
| 313.15 | 0.8979 | 1.4773 |
| 313.15 | 1.0000 | 1.4788 |
| 323.15 | 0.0000 | 1.3291 |
| 323.15 | 0.0500 | 1.3654 |
| 323.15 | 0.0700 | 1.377 |
| 323.15 | 0.1000 | 1.3921 |
| 323.15 | 0.2000 | 1.4258 |
| 323.15 | 0.3000 | 1.4443 |
| 323.15 | 0.4000 | 1.4546 |
| 323.15 | 0.5000 | 1.4615 |
| 323.15 | 0.5996 | 1.466 |
| 323.15 | 0.7011 | 1.4694 |
| 323.15 | 0.8002 | 1.4718 |
| 323.15 | 0.8979 | 1.4736 |
| 323.15 | 1.0000 | 1.4752 |
| 333.15 | 0.0000 | 1.3273 |
| 333.15 | 0.0500 | 1.3637 |
| 333.15 | 0.0700 | 1.3751 |
| 333.15 | 0.1000 | 1.3899 |
| 333.15 | 0.2000 | 1.4226 |
| 333.15 | 0.3000 | 1.4409 |
| 333.15 | 0.4000 | 1.4511 |
| 333.15 | 0.5000 | 1.4578 |
| 333.15 | 0.5996 | 1.4622 |
| 333.15 | 0.7011 | 1.4656 |
| 333.15 | 0.8002 | 1.4681 |
| 333.15 | 0.8979 | 1.4698 |
| 333.15 | 1.0000 | 1.4713 |
Refractive index (Na D-line) [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mass fraction of Ethanol, 2-[(2-aminoethyl)amino]- (1) - Liquid | Refractive index (Na D-line) - Liquid |
| 293.15 | 0.0500 | 1.3406 |
| 298.15 | 0.0500 | 1.3401 |
| 303.15 | 0.0500 | 1.3394 |
| 308.15 | 0.0500 | 1.3387 |
| 313.15 | 0.0500 | 1.3378 |
| 318.15 | 0.0500 | 1.3368 |
| 323.15 | 0.0500 | 1.3358 |
| 328.15 | 0.0500 | 1.3347 |
| 333.15 | 0.0500 | 1.3335 |
| 293.15 | 0.1000 | 1.3452 |
| 298.15 | 0.1000 | 1.3446 |
| 303.15 | 0.1000 | 1.3438 |
| 308.15 | 0.1000 | 1.343 |
| 313.15 | 0.1000 | 1.3421 |
| 318.15 | 0.1000 | 1.341 |
| 323.15 | 0.1000 | 1.3398 |
| 328.15 | 0.1000 | 1.3385 |
| 333.15 | 0.1000 | 1.3371 |
| 293.15 | 0.1500 | 1.351 |
| 298.15 | 0.1500 | 1.3504 |
| 303.15 | 0.1500 | 1.3496 |
| 308.15 | 0.1500 | 1.3487 |
| 313.15 | 0.1500 | 1.3476 |
| 318.15 | 0.1500 | 1.3464 |
| 323.15 | 0.1500 | 1.3451 |
| 328.15 | 0.1500 | 1.3436 |
| 333.15 | 0.1500 | 1.342 |
| 293.15 | 0.2000 | 1.3582 |
| 298.15 | 0.2000 | 1.3575 |
| 303.15 | 0.2000 | 1.3567 |
| 308.15 | 0.2000 | 1.3558 |
| 313.15 | 0.2000 | 1.3548 |
| 318.15 | 0.2000 | 1.3536 |
| 323.15 | 0.2000 | 1.3523 |
| 328.15 | 0.2000 | 1.3508 |
| 333.15 | 0.2000 | 1.3491 |
| 293.15 | 0.2500 | 1.366 |
| 298.15 | 0.2500 | 1.3652 |
| 303.15 | 0.2500 | 1.3643 |
| 308.15 | 0.2500 | 1.3633 |
| 313.15 | 0.2500 | 1.3622 |
| 318.15 | 0.2500 | 1.361 |
| 323.15 | 0.2500 | 1.3597 |
| 328.15 | 0.2500 | 1.3582 |
| 333.15 | 0.2500 | 1.3566 |
| 293.15 | 0.3000 | 1.3752 |
| 298.15 | 0.3000 | 1.3744 |
| 303.15 | 0.3000 | 1.3735 |
| 308.15 | 0.3000 | 1.3724 |
| 313.15 | 0.3000 | 1.3712 |
| 318.15 | 0.3000 | 1.3698 |
| 323.15 | 0.3000 | 1.3682 |
| 328.15 | 0.3000 | 1.3664 |
| 333.15 | 0.3000 | 1.3648 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol, 2-[(2-aminoethyl)amino]- (1) - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 0.0000 | 997.04 |
| 298.15 | 0.0500 | 1015.65 |
| 298.15 | 0.0700 | 1022.28 |
| 298.15 | 0.0999 | 1030.85 |
| 298.15 | 0.1992 | 1047.37 |
| 298.15 | 0.3000 | 1050.66 |
| 298.15 | 0.3997 | 1048.18 |
| 298.15 | 0.4991 | 1044.05 |
| 298.15 | 0.5990 | 1039.62 |
| 298.15 | 0.6991 | 1035.48 |
| 298.15 | 0.7997 | 1031.83 |
| 298.15 | 0.9002 | 1028.28 |
| 298.15 | 1.0000 | 1025.28 |
| 303.15 | 0.0000 | 995.64 |
| 303.15 | 0.0500 | 1013.65 |
| 303.15 | 0.0700 | 1020.01 |
| 303.15 | 0.0999 | 1028.24 |
| 303.15 | 0.1992 | 1044.02 |
| 303.15 | 0.3000 | 1047.05 |
| 303.15 | 0.3997 | 1044.5 |
| 303.15 | 0.4991 | 1040.33 |
| 303.15 | 0.5990 | 1035.89 |
| 303.15 | 0.6991 | 1031.74 |
| 303.15 | 0.7997 | 1028.11 |
| 303.15 | 0.9002 | 1024.57 |
| 303.15 | 1.0000 | 1021.53 |
| 313.15 | 0.0000 | 992.21 |
| 313.15 | 0.0500 | 1009.22 |
| 313.15 | 0.0700 | 1015.13 |
| 313.15 | 0.0999 | 1022.7 |
| 313.15 | 0.1992 | 1037.13 |
| 313.15 | 0.3000 | 1039.7 |
| 313.15 | 0.3997 | 1037.01 |
| 313.15 | 0.4991 | 1032.79 |
| 313.15 | 0.5990 | 1028.36 |
| 313.15 | 0.6991 | 1024.21 |
| 313.15 | 0.7997 | 1020.57 |
| 313.15 | 0.9002 | 1017.06 |
| 313.15 | 1.0000 | 1014.02 |
| 323.15 | 0.0000 | 988.03 |
| 323.15 | 0.0500 | 1004.24 |
| 323.15 | 0.0700 | 1009.76 |
| 323.15 | 0.0999 | 1016.8 |
| 323.15 | 0.1992 | 1030.03 |
| 323.15 | 0.3000 | 1032.15 |
| 323.15 | 0.3997 | 1029.37 |
| 323.15 | 0.4991 | 1025.13 |
| 323.15 | 0.5990 | 1020.71 |
| 323.15 | 0.6991 | 1016.59 |
| 323.15 | 0.7997 | 1012.96 |
| 323.15 | 0.9002 | 1009.48 |
| 323.15 | 1.0000 | 1006.44 |
| 333.15 | 0.0000 | 983.19 |
| 333.15 | 0.0500 | 998.75 |
| 333.15 | 0.0700 | 1003.89 |
| 333.15 | 0.0999 | 1010.53 |
| 333.15 | 0.1992 | 1022.69 |
| 333.15 | 0.3000 | 1024.44 |
| 333.15 | 0.3997 | 1021.57 |
| 333.15 | 0.4991 | 1017.35 |
| 333.15 | 0.5990 | 1012.96 |
| 333.15 | 0.6991 | 1008.88 |
| 333.15 | 0.7997 | 1005.3 |
| 333.15 | 0.9002 | 1001.84 |
| 333.15 | 1.0000 | 998.83 |
| 343.15 | 0.0000 | 977.75 |
| 343.15 | 0.0500 | 992.77 |
| 343.15 | 0.0700 | 997.34 |
| 343.15 | 0.0999 | 1003.89 |
| 343.15 | 0.1992 | 1015.09 |
| 343.15 | 0.3000 | 1016.53 |
| 343.15 | 0.3997 | 1013.6 |
| 343.15 | 0.4991 | 1009.42 |
| 343.15 | 0.5990 | 1005.1 |
| 343.15 | 0.6991 | 1001.06 |
| 343.15 | 0.7997 | 997.54 |
| 343.15 | 0.9002 | 994.11 |
| 343.15 | 1.0000 | 991.15 |
Boiling temperature at pressure P, K [ref]
Operational condition: Pressure, kPa = 86.66 (Liquid)
| Mass fraction of Ethanol, 2-[(2-aminoethyl)amino]- (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0580 | 369.65 |
| 0.1010 | 369.80 |
| 0.1500 | 370.61 |
| 0.2440 | 371.06 |
| 0.3530 | 372.49 |
| 0.4340 | 373.50 |
| 0.4830 | 374.87 |
| 0.5380 | 375.86 |
| 0.5740 | 376.86 |
| 0.6070 | 378.06 |
| 0.6590 | 380.81 |
| 0.7050 | 382.26 |
| 0.6900 | 381.56 |
| 0.8860 | 407.73 |
| 0.8840 | 412.22 |
| 0.9700 | 468.15 |
| 0.9800 | 515.15 |
Sources
- Molar excess enthalpy (HEm) for various {alkanolamine (1) + water (2)} systems at T = (298.15, 313.15, and 323.15) K
- Equilibrium solubility of carbon dioxide in aqueous 2-((2-aminoethyl)amino)ethanol and N-methyldiethanolamine solution and modeling by electrolyte mPR-CPA EoS
- Excess molar enthalpies for binary mixtures of different amines with water
- Measuring and correlating solubility of hydrogen sulfide in aqueous solution of 2-((2 aminoethyl)amino)ethanol
- Experimental Data and Modeling for Viscosity and Refractive Index of Aqueous Mixtures with 2-(Methylamino)ethanol (MAE) and Aminoethylethanolamine (AEEA)
- Heat of Absorption of CO2 and Heat Capacity Measurements in Aqueous Solutions of Benzylamine, N-(2-Aminoethyl)-ethanolamine, and Their Blends Using a Reaction Calorimeter
- Volumetric Properties, Viscosities, and Refractive Indices for Aqueous 2-((2-Aminoethyl)amino)ethanol Solutions from (298.15 to 343.15) K
- Molar Heat Capacity of Various Aqueous Alkanolamine Solutions from 303.15 K to 353.15 K
Note: These property values are available through the Cheméo API. A free account gives you an access key.