释义 |
- Vapor pressure of liquid
- Distillation data
- References
This page provides supplementary chemical data on isopropanol. == Material Safety Data Sheet == The handling of this chemical may incur notable safety precautions. It is highly recommend that you seek the Material Safety Datasheet (MSDS) for this chemical from a reliable source such as MSDS Search Engine, and follow its directions. == Structure and properties == Structure and properties | Index of refraction, nD | 1.3776 at 20°C | Abbe number | ? | Dielectric constant, εr | 18.23 ε0 at 25 °C | Bond strength | ? | Bond length | ? | Bond angle | ? | Magnetic susceptibility | ? | Surface tension | 21.7 dyn/cm at 20°C | Viscosity[1] | 4.5646 mPa·s at 0°C 2.3703 mPa·s at 20°C 1.3311 mPa·s at 40°C | |
== Thermodynamic properties == Phase behavior | Triple point | 184.9 K (–88.2 °C), ? Pa | Critical point | 508.7 K (235.6 °C), 5370 kPa | Std enthalpy change of fusion, ΔfusHo | 5.28 kJ/mol | Std entropy change of fusion, ΔfusSo | 28.6 J/(mol·K) | Std enthalpy change of vaporization, ΔvapHo | 44.0 kJ/mol | Std entropy change of vaporization, ΔvapSo | 124 J/(mol·K) | Solid properties |
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Std enthalpy change of formation, ΔfHosolid | ? kJ/mol | Standard molar entropy, Sosolid | ? J/(mol K) | Heat capacity, cp | 0.212 J/(mol K) at –200°C | Liquid properties |
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Std enthalpy change of formation, ΔfHoliquid | –318.2 kJ/mol | Standard molar entropy, Soliquid | 180 J/(mol K) | Heat capacity, cp | 2.68 J/(gK) at 20°C-25°C | Gas properties |
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Std enthalpy change of formation, ΔfHogas | –261.1 kJ/mol | Standard molar entropy, Sogas | 333 J/(mol K) | Heat capacity, cp | 1.54 J/(gK) at 25°C | |
Vapor pressure of liquidP in mm Hg | 1 | 10 | 40 | 100 | 400 | 760 | 1520 | 3800 | 7600 | 15200 | 30400 | 45600 | T in °C | −26.1 | 2.4 | 23.8 | 39.5 | 67.8 | 82.5 | 101.3 | 130.2 | 155.7 | 186.0 | 220.2 | — |
Table data obtained from CRC Handbook of Chemistry and Physics 44th ed. {{Clear}}Distillation dataVapor-liquid equilibrium for isopropanol/water[4] P = 760 mm Hg | BP temp. °C | % by mole isopropanol |
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liquid | vapor |
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82.2 | 100.00 | 100.00 | 81.48 | 95.35 | 93.25 | 80.70 | 87.25 | 83.40 | 80.37 | 80.90 | 77.45 | 80.23 | 76.50 | 73.70 | 80.11 | 69.55 | 69.15 | 80.16 | 66.05 | 67.15 | 80.15 | 64.60 | 66.45 | 80.31 | 55.90 | 62.55 | 80.38 | 51.45 | 60.75 | 80.67 | 44.60 | 59.20 | 80.90 | 38.35 | 57.00 | 81.28 | 29.80 | 55.10 | 81.29 | 29.75 | 55.40 | 81.23 | 28.35 | 55.30 | 81.62 | 24.50 | 53.90 | 81.75 | 19.35 | 53.20 | 81.58 | 18.95 | 53.75 | 81.99 | 16.65 | 52.15 | 82.32 | 12.15 | 51.20 | 82.70 | 10.00 | 50.15 | 84.57 | 5.70 | 45.65 | 88.05 | 3.65 | 36.55 | 93.40 | 1.60 | 21.15 | 95.17 | 1.15 | 16.30 | 100.0 | 0.00 | 0.00 | |
Vapor-liquid equilibrium for isopropanol/methanol[4] P = 101.325 kPa | BP temp. °C | % by mole methanol |
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liquid | vapor |
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64.37 | 100.0 | 100.0 | 67.34 | 81.26 | 90.32 | 67.64 | 79.45 | 89.10 | 69.54 | 68.64 | 81.73 | 70.77 | 61.72 | 76.52 | 71.88 | 55.96 | 71.76 | 72.78 | 51.03 | 67.78 | 73.80 | 46.34 | 63.08 | 74.85 | 39.75 | 56.21 | 75.65 | 35.50 | 51.62 | 76.36 | 31.71 | 46.91 | 77.93 | 23.79 | 35.98 | 78.67 | 19.49 | 30.22 | 79.45 | 15.45 | 24.40 | 80.04 | 12.30 | 19.56 | 80.57 | 9.30 | 14.66 | 80.82 | 8.43 | 12.43 | 82.20 | 0.0 | 0.0 | |
| Vapor-liquid equilibrium for isopropanol/acetone[4] P = 101.325 kPa | BP temp. °C | % by mole acetone |
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liquid | vapor |
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77.92 | 6.12 | 19.90 | 76.71 | 8.28 | 25.52 | 71.50 | 19.59 | 47.03 | 70.99 | 20.91 | 48.90 | 69.20 | 26.01 | 55.29 | 68.85 | 27.10 | 56.50 | 65.91 | 37.55 | 66.12 | 63.55 | 48.12 | 73.37 | 63.42 | 48.74 | 73.75 | 62.46 | 53.77 | 76.63 | 62.37 | 54.27 | 76.91 | 61.85 | 57.22 | 78.49 | 61.86 | 57.12 | 78.43 | |
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See also - Tetrachloroethylene (data page)
{{Clear}}== Spectral data == UV-Vis | λmax | 205 nm | Extinction coefficient, ε | 100.2 m2/mol | IR |
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Major absorption bands | 3334, 2970, 1466, 1378, 1160, 1128, 951, 817, 639 cm−1 | NMR |
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Proton NMR | | Carbon-13 NMR | | Other NMR data | | MS |
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Masses of main fragments | m/z (% of relative intensity): 45 (100), 43 (19.1), 27 (16.8), 29 (12.5), 19 (9.9), 15 (9.5), 41 (8.2), 31 (6.8), 39 (6.6), 42 (4.4) | |
References1. ^Lange's Handbook of Chemistry, 10th ed. pp 1669-1674 2. ^{{cite journal|last=Parks|first=J. S.|author2=B. Barton|journal=Journal of the American Chemical Society|year=1928|volume=50|pages=24–26|doi=10.1021/ja01388a004 |title=Vapor pressure data for isopropyl alcohol and tertiary butyl alcohol }} 3. ^{{cite journal|last=Barr-David|first=F|author2=B. F. Dodge|journal=Journal of Chemical and Engineering Data|year=1959|volume=4|pages=107–121 |doi=10.1021/je60002a003 |title= Vapor-Liquid Equilibrium at High Pressures. The Systems Ethanol-Water and 2-Propanol-Water}} 4. ^1 2 {{Cite web|url=http://www.cheric.org/research/kdb/hcvle/hcvle.php|title=Binary Vapor-Liquid Equilibrium Data|publisher=Chemical Engineering Research Information Center|format=Queriable database|accessdate=2007-05-05}}
Except where noted otherwise, data relate to standard ambient temperature and pressure. {{Use dmy dates|date=September 2010}}{{DEFAULTSORT:Isopropyl Alcohol (Data Page)}} 1 : Chemical data pages |