- InChI
- InChI=1S/C7H16O2/c1-3-4-5-9-6-7(2)8/h7-8H,3-6H2,1-2H3
- InChI Key
- RWNUSVWFHDHRCJ-UHFFFAOYSA-N
- Formula
- C7H16O2
- SMILES
- CCCCOCC(C)O
- Molecular Weight1
- 132.20
- CAS
- 5131-66-8
- Other Names
-
- 1,2-Propylene glycol 1-monobutyl ether
- 1-Butoxy-2-propanol
- 1-butoxypropan-2-ol
- 2-Hydroxy-3-butoxypropane
- NSC 2211
- Propasol solvent B
- Propylene glycol monobutyl ether
- Propylene glycol n-butyl ether
- n-Butoxypropanol
- propane, 1-butoxy-2-hydroxy-
- propyleneglycol, 1-butyl ether
- 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).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- 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).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- csound,fluid : Speed of sound in fluid (m/s).
- 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 |
|---|---|---|---|
| ΔfG° | -236.20 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -477.54 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 15.64 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 49.88 | kJ/mol | Joback Calculated Property |
| log10WS | -1.22 | Crippen Calculated Property | |
| logPoct/wat | 1.184 | Crippen Calculated Property | |
| McVol | 121.230 | ml/mol | McGowan Calculated Property |
| Pc | 3062.55 | kPa | Joback Calculated Property |
| Inp | [923.00; 948.00] |
|
|
| Inp | 936.20 | NIST | |
| Inp | 936.70 | NIST | |
| Inp | 928.00 | NIST | |
| Inp | 941.00 | NIST | |
| Inp | 945.00 | NIST | |
| Inp | 947.00 | NIST | |
| Inp | 948.00 | NIST | |
| Inp | 936.00 | NIST | |
| Inp | Outlier 923.00 | NIST | |
| Inp | 941.00 | NIST | |
| Inp | 936.20 | NIST | |
| I | 1363.50 | NIST | |
| Tboil | 443.35 | K | NIST |
| Tc | 637.45 | K | Joback Calculated Property |
| Tfus | 236.70 | K | Joback Calculated Property |
| Vc | 0.459 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [271.52; 330.41] | J/mol×K | [473.72; 637.45] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 270 280 290 300 310 320 330 500 550 600 | ||||
| Cp,gas | 271.52 | J/mol×K | 473.72 | Joback Calculated Property |
| Cp,gas | 282.22 | J/mol×K | 501.01 | Joback Calculated Property |
| Cp,gas | 292.56 | J/mol×K | 528.30 | Joback Calculated Property |
| Cp,gas | 302.54 | J/mol×K | 555.59 | Joback Calculated Property |
| Cp,gas | 312.18 | J/mol×K | 582.87 | Joback Calculated Property |
| Cp,gas | 321.47 | J/mol×K | 610.16 | Joback Calculated Property |
| Cp,gas | 330.41 | J/mol×K | 637.45 | Joback Calculated Property |
| Cp,liquid | [302.30; 335.50] | J/mol×K | [275.15; 339.15] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 300 305 310 315 320 325 330 335 280 300 320 340 | ||||
| Cp,liquid | 302.30 | J/mol×K | 275.15 | Heat ca... |
| Cp,liquid | 303.20 | J/mol×K | 276.65 | Heat ca... |
| Cp,liquid | 304.10 | J/mol×K | 278.15 | Heat ca... |
| Cp,liquid | 305.00 | J/mol×K | 279.65 | Heat ca... |
| Cp,liquid | 305.90 | J/mol×K | 281.15 | Heat ca... |
| Cp,liquid | 306.80 | J/mol×K | 282.65 | Heat ca... |
| Cp,liquid | 307.60 | J/mol×K | 284.15 | Heat ca... |
| Cp,liquid | 308.50 | J/mol×K | 285.65 | Heat ca... |
| Cp,liquid | 309.30 | J/mol×K | 287.15 | Heat ca... |
| Cp,liquid | 310.20 | J/mol×K | 288.65 | Heat ca... |
| Cp,liquid | 311.00 | J/mol×K | 290.15 | Heat ca... |
| Cp,liquid | 311.90 | J/mol×K | 291.65 | Heat ca... |
| Cp,liquid | 312.70 | J/mol×K | 293.15 | Heat ca... |
| Cp,liquid | 313.50 | J/mol×K | 294.65 | Heat ca... |
| Cp,liquid | 314.40 | J/mol×K | 296.15 | Heat ca... |
| Cp,liquid | 315.20 | J/mol×K | 297.65 | Heat ca... |
| Cp,liquid | 315.50 | J/mol×K | 298.15 | Heat ca... |
| Cp,liquid | 316.00 | J/mol×K | 299.15 | Heat ca... |
| Cp,liquid | 316.80 | J/mol×K | 300.65 | Heat ca... |
| Cp,liquid | 317.60 | J/mol×K | 302.15 | Heat ca... |
| Cp,liquid | 318.40 | J/mol×K | 303.65 | Heat ca... |
| Cp,liquid | 319.20 | J/mol×K | 305.15 | Heat ca... |
| Cp,liquid | 320.00 | J/mol×K | 306.65 | Heat ca... |
| Cp,liquid | 320.70 | J/mol×K | 308.15 | Heat ca... |
| Cp,liquid | 321.50 | J/mol×K | 309.65 | Heat ca... |
| Cp,liquid | 322.30 | J/mol×K | 311.15 | Heat ca... |
| Cp,liquid | 323.00 | J/mol×K | 312.65 | Heat ca... |
| Cp,liquid | 323.80 | J/mol×K | 314.15 | Heat ca... |
| Cp,liquid | 324.50 | J/mol×K | 315.65 | Heat ca... |
| Cp,liquid | 325.30 | J/mol×K | 317.15 | Heat ca... |
| Cp,liquid | 326.00 | J/mol×K | 318.65 | Heat ca... |
| Cp,liquid | 326.80 | J/mol×K | 320.15 | Heat ca... |
| Cp,liquid | 327.50 | J/mol×K | 321.65 | Heat ca... |
| Cp,liquid | 328.20 | J/mol×K | 323.15 | Heat ca... |
| Cp,liquid | 328.90 | J/mol×K | 324.65 | Heat ca... |
| Cp,liquid | 329.60 | J/mol×K | 326.15 | Heat ca... |
| Cp,liquid | 330.30 | J/mol×K | 327.65 | Heat ca... |
| Cp,liquid | 331.00 | J/mol×K | 329.15 | Heat ca... |
| Cp,liquid | 331.70 | J/mol×K | 330.65 | Heat ca... |
| Cp,liquid | 332.40 | J/mol×K | 332.15 | Heat ca... |
| Cp,liquid | 333.10 | J/mol×K | 333.65 | Heat ca... |
| Cp,liquid | 333.80 | J/mol×K | 335.15 | Heat ca... |
| Cp,liquid | 334.40 | J/mol×K | 336.65 | Heat ca... |
| Cp,liquid | 335.10 | J/mol×K | 338.15 | Heat ca... |
| Cp,liquid | 335.50 | J/mol×K | 339.15 | Heat ca... |
| η | [0.0001517; 0.0625947] | Pa×s | [236.70; 473.72] |
|
|
T(K) Dynamic viscosity (Pa×s) 0 0.01 0.02 0.03 0.04 0.05 0.06 300 400 | ||||
| η | 0.0625947 | Pa×s | 236.70 | Joback Calculated Property |
| η | 0.0111917 | Pa×s | 276.20 | Joback Calculated Property |
| η | 0.0030786 | Pa×s | 315.71 | Joback Calculated Property |
| η | 0.0011285 | Pa×s | 355.21 | Joback Calculated Property |
| η | 0.0005057 | Pa×s | 394.71 | Joback Calculated Property |
| η | 0.0002622 | Pa×s | 434.22 | Joback Calculated Property |
| η | 0.0001517 | Pa×s | 473.72 | Joback Calculated Property |
| ρl | [861.24; 879.03] | kg/m3 | [293.15; 313.15] |
|
|
T(K) Liquid Density (kg/m3) 860 865 870 875 880 295 300 305 310 | ||||
| ρl | 879.03 | kg/m3 | 293.15 | Molecul... |
| ρl | 874.63 | kg/m3 | 298.15 | Molecul... |
| ρl | 870.20 | kg/m3 | 303.15 | Molecul... |
| ρl | 865.74 | kg/m3 | 308.15 | Molecul... |
| ρl | 861.24 | kg/m3 | 313.15 | Molecul... |
| csound,fluid | [1207.02; 1297.59] | m/s | [288.15; 313.15] |
|
|
T(K) Speed of sound in fluid (m/s) 1200 1220 1240 1260 1280 1300 290 300 310 | ||||
| csound,fluid | 1297.59 | m/s | 288.15 | Densiti... |
| csound,fluid | 1278.98 | m/s | 293.15 | Thermod... |
| csound,fluid | 1279.95 | m/s | 293.15 | Densiti... |
| csound,fluid | 1260.90 | m/s | 298.15 | Thermod... |
| csound,fluid | 1261.87 | m/s | 298.15 | Densiti... |
| csound,fluid | 1242.94 | m/s | 303.15 | Thermod... |
| csound,fluid | 1243.85 | m/s | 303.15 | Densiti... |
| csound,fluid | 1224.91 | m/s | 308.15 | Thermod... |
| csound,fluid | 1225.83 | m/s | 308.15 | Densiti... |
| csound,fluid | 1207.02 | m/s | 313.15 | Thermod... |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [341.82; 466.94] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.64361e+01 | |||
| Coefficient B | -4.47407e+03 | |||
| Coefficient C | -6.47630e+01 | |||
| Temperature range, min. | 341.82 | |||
| Temperature range, max. | 466.94 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 450 | ||||
| Pvap | 1.33 | kPa | 341.82 | Calculated Property |
| Pvap | 2.88 | kPa | 355.72 | Calculated Property |
| Pvap | 5.81 | kPa | 369.62 | Calculated Property |
| Pvap | 11.03 | kPa | 383.53 | Calculated Property |
| Pvap | 19.83 | kPa | 397.43 | Calculated Property |
| Pvap | 34.00 | kPa | 411.33 | Calculated Property |
| Pvap | 55.95 | kPa | 425.23 | Calculated Property |
| Pvap | 88.70 | kPa | 439.14 | Calculated Property |
| Pvap | 136.07 | kPa | 453.04 | Calculated Property |
| Pvap | 202.66 | kPa | 466.94 | Calculated Property |
Similar Compounds
![Ethanol, 2-[2-(2-butoxyethoxy)ethoxy]-.](data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAAPoAAAD6CAIAAAAHjs1qAAAM4klEQVR4nO3be2xTdR/H8V/XjbGx4TacwGRTEHDqwsXJIoNxk4TbCFNT9uAsStCpJFQiwfKHpCbDpYGEzGBM5gJYEAP7x6SAEIGJ4oXLJgKDyTIEd3lwd5BdXLf18/zx61PHbddWjN/P66/RlfNte97n9HcOagCgiGQIuN8vgOjvw9xJEOZOgjB3EoS5kyDMnQRh7iQIcydBmDsJwtxJEOZOgjB3EoS5kyDMnQRh7iQIcydBmDsJwtxJEOZOgjB3EoS5kyDMnQRh7iQIcydBmDsJwtxJEOZOgjB3EoS5kyDMnQRh7iQIcydBmDsJwtxJEOZOgjB3EoS5kyDMnQRh7iQIcydBmDsJwtxJEOZOgjB3EoS5kyDMnQRh7iQIcydBmDsJwtxJEOZOgjB3EoS5kyDMnQRh7iQIcydBmDsJwtxJEOZOgjB3EoS5kyDMnQRh7iQIcydBmDsJwtxJEOZOgjB3EoS5kyDMnQRh7iQIcydBmDsJwtxJEOZOgjB3EoS5kyDMnQRh7iQIcydBmDsJwtxJEOZOgjB3EoS5kyDMnQRh7iQIcydBmDsJwtxJEOZOgjB3EoS5kyDMnQRh7iQIcydBmDsJwtxJEOZOgjB3EoS5kyDMnQRh7iQIcydBmDsJwtxJEOZOgjB3EoS5kyDMnQRh7iQIcydBmDsJwtxJEOZOgjB3EiTwfr8A2WprldWqOjtVS4tav14lJt7vF/Qv5+Oze3FxcUxMTFhY2JIlS5qbm327ca+qqqq0tLSMjIzy8nI/jVBKud3uzz///ODBg/4bodavV5mZyuFQeXlq9Wrldvtx1r9AZ6datUq98opKT1fZ2UoplZ6url9XSqnKSrVyZc9bgI9UV1e/8cYbRqPRu+VRo0bt2bPHV9vX2tvbc3Nzo6OjlVKDBg0KCQmx2WwtLS2+nQKgoKBg0qRJQ4cOVUrNnz//t99+8/kIAEhO/utnkwkVFf4Y0tLSsmDBgsTExLy8PLfb7Y8R2vbt2zdt2lRfX++vATt3YvNmz88rVuDUKaSloaEBAMrL8fLLPW7AB7m7XK6cnJwHHnhAKRUYGLhy5cq8vLypU6fq6GfOnHn27NmBTwGwf//++Ph4vdkJEyakpKQYDAal1OjRo7/44gufjABw6dKlJUuW6Cnh4eFBQUFKqbCwMLvd3tbW5qspuHkTbjemT4e3v8WLUVcHl8tnIwC3252fnz969GillH4jSUlJJ0+e9OEIraioaNasWXp3REdHOxwOn48AAIsFp097ft65Ex9/jLQ0vPQSXn0VS5f+Hbk7nc7HHntMxzF37tzz58/rx91ut8PheOihh5RSAQEBZrO5tra231NKSkoWLVqkp4wbNy4/P18//s0330ycOFE/PmfOnOLi4oG8l4aGBqvVGhwcrJQaMmSI/t6oqKgwm816xNixY/fv3z+QEQDQ2QmHAyNGYNcubNiAbdsA4Px5zJuHykqMGgW7Hb44rk6dOjVt2jTv2SEjI2P48OHe3VFTUzPwEQCqqqpWrFgREBCglIqIiIiIiPDGcPHiRZ+MAIC2Nvz+O957D0eOeB7ZuhW7d3vO7m6338/uhYWFM2bM0O8tPj7+rh00NjZardZBgwYppaKionJycjo6Ovo0pa6uzmKxBAYGKqUiIyPtdvuff/7Z9QkdHR1bt26NjIzUJ7ArH3yAGzf6/GZcrmPbtg0bNkwpZTQaX3vttWvXrnX9fUFBQUJCgndHlpSU9HmEdvQoJk6EUlAKJhPa27F5M5YvxzvvoLYWmzZ5fpWQgIKCfo4A9CGqz7UjR47Mzc3VH3vX3REZGdmP3dFVS0uL3W7X672goCCLxdLY2NjZ2elwOPRqMzAw0GKxXL9+vd8jPJxOjB2LBQtw7hwWLUJdHa5cQUoKGhr+jsVMZWVlZmamPqCHDRuWk5PT3t7ezfNLSkrmzZunW5k8efJ3333XmyltbW1d10iZmZndnJDq6+stFstbEyfCYMCIEcjNRWdnb9/P4cNISGiIiBgWFTV79uwzZ87c9Vld12x67/7xxx+9HQGgtBQmk6fmUaPgcOCuy+jDhxEf73laaiquXOnDCKCpqclms4WEhCilQkJCrFbrjTsO/uLi4jlz5ujdsXfZMvRud9zC7W7csyc2NlZv5IUXXigrK+v6+4aGBovFoi/kdCGdvd8dXRUWYsYMz6fx1FNoaMCJE1izBlYr9MTt26Gv3BobsXt3j9vrW+7Nzc12uz08PFxfKfbp2HU6nY888ohSymAwmEym8vLy7p88ZsyYO9dI3WsvKkJysufTSU5GUVEPf+HcOcyd63n++PFXDh7sccS1a9e8h3pMTIzD4ejx4q++vr5t3ToEBUEphIcjOxutrd39hdZWbNyIIUOgFEJDkZXV3v3zAQD6tDpixAjvJ3yl20PF6XTOnDChMyoKBgNMJnS7O25x8iSmTYNS6VOnPv3008eOHbvXE8+cOTN9+nS9E5955pkff/yxtyMAVFUhMxNGI5RCVBRyctDtKbWXepu7vujRvSqlUlNTL1++3Ndhzc3NNptt8ODB3sXxbSsTAIWFhSkpKXrKE088ceDAgb7NcLuRn4/YWCiFgACYzaiuvsvT6upgsXg+zchI2O2445V04/Tp088++2yP1+Iul0vfR/pq1izPi7l1jdSdqiqYzTAYjk+YEBcX1/3F39GjR73XMElJSb38/kRzMzZswODBnuNw06Yerhl+/RVLl8JggFJ4+OEbu3b1eM7W2cTFxemD0Gw2V991d9zyoport2zxHO3BwVi3DgNfDv1fr3I/ceKE905LYmLit99+O5CRZWVlJpNJb238+PFffvmlfvzONVL/V5Y3bmDtWs8JNToa16/j+HGsXo1330VZGX76CUOHQikEBcFiQb9unHW9FtdrrduuxZ1O5+OPP+75ul+40N2/21Nff/2fBQv0RubPn//LL7/c9vtLly55P8zY2NjefNvcrqICZrPnK27cONz1/NLUBJvNc2CEhsJqRV8WcnqJpe8BRERE3Gv1q4+NRx99dHZcHIKDkZqKW9dIA9dD7i6X68UXX/R+mrt27fLVjdsjR448+eSTesspKSnp6elhYWH9WCN1p7QUCxdi1SqcPInnn0djIy5fxrRpqK1FQgLmzsXA7uQAaGxs9F5Je6/FL168uHDhQu/x7L2P1D96lfLggw96rxn0cvzO+0itvVjz3NOhQ39dM+zbhwsXkJmJ5cvx6adwuTBmDJSCwQCzud//OFBaWuq9vRYfH3/o0KGuvz1+/PiUKVO8K5///vBD/9/LvfV8djeZTKGhoVar9ebNm76drS/+9KX9QNZIPWhrw9q1+P57zx+3bMHevT78fgRw9uzZmTNn6rcQEhKiL9GioqI+/PBDl4/uo9fU1Lz++uv6q2/kyJHJycn6ZpTRaMzMzOxxhdArLhdycpCcjIYGpKSgpgZuN9aswd69eP99JCX99RkOQNerstTU1KtXr5aXl3vvI8XExHjvI/lDz7lXVlZWVVX5aTyA0tLSKVOmTJ48eXcvrqz76c034V1LfPIJduzwxxCn0xkZGWkwGHq8j9RvRUVF+la67v655577+eeffTzD7cbhw7DZPH+8fBkZGT65TPRqbW3NysoKDQ3Vh6v+96/Q0FCbzdbU1OTDQXfy2X9E8I+2Ywdycjw/L1uGCxf8NKe6utrhcPT2SrFf3G53dnZ2WlpaVlaWv2YcOICNGz0/V1QgPd0fQyorKxcvXqyUCgsLM5lMV69e9ceU2xgAqH+9jg61erVqbVXNzWr6dPX22/f7Bf2z1dSojAx18KAKDFQffaSMRvXWW34aVVRUZDQaJ02a5Kft30ZG7tRX+/apzz5TwcFq+HCVna2Cgu73C/IN5k6C8P9mIkGYOwnC3EkQ5k6CMHcShLmTIMydBGHuJAhzJ0GYOwnC3EkQ5k6CMHcShLmTIMydBGHuJAhzJ0GYOwnC3EkQ5k6CMHcShLmTIMydBGHuJAhzJ0GYOwnC3EkQ5k6CMHcShLmTIMydBGHuJAhzJ0GYOwnC3EkQ5k6CMHcShLmTIMydBGHuJAhzJ0GYOwnC3EkQ5k6CMHcShLmTIMydBGHuJAhzJ0GYOwnC3EkQ5k6CMHcShLmTIMydBGHuJAhzJ0GYOwnC3EkQ5k6CMHcShLmTIMydBGHuJAhzJ0GYOwnC3EkQ5k6CMHcShLmTIMydBGHuJAhzJ0GYOwnC3EkQ5k6CMHcShLmTIMydBGHuJAhzJ0GYOwnC3EkQ5k6CMHcShLmTIMydBGHuJAhzJ0GYOwnC3EkQ5k6CMHcShLmTIMydBGHuJAhzJ0GYOwnC3EkQ5k6CMHcShLmTIMydBGHuJAhzJ0GYOwnC3EkQ5k6CMHcShLmTIMydBGHuJAhzJ0GYOwnC3EkQ5k6C/A/lGjO0VAsPZgAAAABJRU5ErkJggg==)
Find more compounds similar to 2-Propanol, 1-butoxy-.
Mixtures
- 1-Propanol + 2-Propanol, 1-butoxy-
- Isopropyl Alcohol + 2-Propanol, 1-butoxy-
- 1-Butanol + 2-Propanol, 1-butoxy-
- 2-Propanol, 1-butoxy- + 1-Hexanol
- 1-Octanol + 2-Propanol, 1-butoxy-
- 2-Propanol, 1-butoxy- + 1-Decanol
- 2-Propanol, 1-butoxy- + Acetic acid, methyl ester
- Ethyl Acetate + 2-Propanol, 1-butoxy-
- Acetic acid, butyl ester + 2-Propanol, 1-butoxy-
- 2-Propanol, 1-butoxy- + Water
Sources
- Crippen Method
- Crippen Method
- Heat capacity of dowanols within a temperature range of (275.15 to 339.15) K. Measurements and prediction.
- Molecular interactions in binary mixtures of 1-butoxy-2-propanol with alcohols at different temperatures: A thermophysical and spectroscopic approach
- Thermodynamic and spectral studies of molecular interactions in binary liquid mixtures of 1-butoxy-2- propanol with 1-alcohols
- Mutual Solubility and Lower Critical Solution Temperature for Water + Glycol Ether Systems
- Densities and Speeds of Sound of Binary Liquid Mixtures of Some n-Alkoxypropanols with Methyl Acetate, Ethyl Acetate, and n-Butyl Acetate at T = (288.15, 293.15, 298.15, 303.15, and 308.15) K
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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.
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