This page provides supplementary chemical data on o-Xylene.
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 SIRI, and follow its directions. MSDS is available from Safety Information Resources, inc.
Structure and properties
Thermodynamic properties
Phase behavior
|
Triple point
| 247.8 K (–25.3 °C), ? Pa
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Critical point
| 631 K (358 °C), 3700 Pa
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Std enthalpy change of fusion, ΔfusHo
| 13.6 kJ/mol
|
Std entropy change of fusion, ΔfusSo
| 54.87 J/(mol·K) at –25.3
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Std enthalpy change of vaporization, ΔvapHo
| 36.24 kJ/mol at 144.5°C
|
Std entropy change of vaporization, ΔvapSo
| ? J/(mol·K)
|
Solid properties
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Std enthalpy change of formation, ΔfHosolid
| ? kJ/mol
|
Standard molar entropy, Sosolid
| ? J/(mol K)
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Heat capacity, cp
| ? J/(mol K)
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Liquid properties
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Std enthalpy change of formation, ΔfHoliquid
| –24.4 kJ/mol
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Standard molar entropy, Soliquid
| 247 J/(mol K)
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Enthalpy of combustion, ΔcHo
| –4552 kJ/mol
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Heat capacity, cp
| 187.0 J/(mol K) at 25°C
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Gas properties
|
Std enthalpy change of formation, ΔfHogas
| 19.0 kJ/mol
|
Standard molar entropy, Sogas
| 353.6 J/(mol K)
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Heat capacity, cp
| 132.5 J/(mol K) at 25°C
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van der Waals' constants[5]
| a = 3038 L2 kPa/mol2 b = 0.1755 liter per mole
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Vapor pressure of liquid
P in mm Hg | 1 | 10 | 40 | 100 | 400 | 760
|
T in °C | –3.8 | 32.1 | 59.5 | 81.3 | 121.7 | 144.4
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Table data obtained from CRC Handbook of Chemistry and Physics 44th ed.
Distillation data
See also:
Vapor-liquid Equilibrium for o-Xylene/m-Xylene[7] P = 26.66 kPa
|
BP Temp. °C
| % by mole m-xylene
|
liquid | vapor
|
100.1 | 0.0 | 0.0
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99.8 | 4.7 | 5.6
|
99.6 | 9.7 | 11.4
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99.2 | 17.8 | 20.6
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98.8 | 25.9 | 29.3
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98.4 | 34.1 | 38.1
|
97.9 | 42.5 | 46.8
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97.6 | 49.6 | 53.9
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97.2 | 57.4 | 61.5
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96.8 | 65.5 | 69.2
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96.5 | 73.5 | 76.5
|
96.1 | 80.8 | 83.2
|
95.8 | 88.6 | 90.2
|
95.6 | 93.7 | 94.6
|
95.3 | 100.0 | 100.0
|
|
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Vapor-liquid Equilibrium for o-Xylene/Carbon tetrachloride[7] P = 760 mm Hg
|
BP Temp. °C
| % by mole carbon tetrachloride
|
liquid | vapor
|
142.0 | 1.8 | 6.5
|
136.0 | 6.4 | 22.9
|
130.4 | 11.2 | 36.9
|
125.0 | 16.1 | 49.4
|
120.7 | 20.4 | 57.3
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116.1 | 25.3 | 64.6
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111.8 | 30.2 | 70.9
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107.9 | 35.2 | 75.9
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104.2 | 40.4 | 80.3
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104.1 | 40.5 | 80.5
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99.4 | 47.8 | 85.2
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95.1 | 55.4 | 88.9
|
91.6 | 62.4 | 91.6
|
88.2 | 70.0 | 94.0
|
85.3 | 77.1 | 95.8
|
82.6 | 84.1 | 97.2
|
80.0 | 91.0 | 98.5
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77.7 | 97.6 | 99.6
|
|
|
Vapor-liquid Equilibrium for o-Xylene/Ethanol[7] P = 101.3 kPa
|
BP Temp. °C
| % by mole ethanol
|
liquid | vapor
|
78.3 | 99.52 | 99.66
|
78.7 | 98.59 | 99.03
|
78.7 | 97.73 | 98.52
|
79.0 | 95.78 | 97.40
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79.3 | 90.59 | 95.09
|
79.7 | 86.79 | 94.16
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80.0 | 85.01 | 93.70
|
80.2 | 80.91 | 92.91
|
80.3 | 76.77 | 92.36
|
82.0 | 67.69 | 91.21
|
83.8 | 48.66 | 89.25
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88.1 | 25.11 | 87.32
|
97.3 | 10.94 | 81.49
|
112.8 | 5.22 | 65.91
|
137.3 | 0.65 | 22.90
|
|
|
Vapor-liquid Equilibrium for o-Xylene/Methanol[7] P = 101.3 kPa
|
BP Temp. °C
| % by mole Methanol
|
liquid | vapor
|
64.7 | 98.78 | 99.10
|
64.8 | 98.33 | 98.81
|
64.8 | 97.67 | 98.45
|
64.9 | 96.70 | 97.96
|
65.3 | 93.34 | 96.82
|
65.7 | 86.84 | 95.68
|
66.3 | 84.24 | 95.31
|
66.7 | 83.30 | 95.65
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67.3 | 76.74 | 94.97
|
68.4 | 49.33 | 94.52
|
71.5 | 21.76 | 93.84
|
102.1 | 2.49 | 80.00
|
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Spectral data
References
- ^ Merck Index of Chemicals and Drugs, 9th ed. monograph 9743
- ^ CRC Handbook of Chemistry and Physics, 44th ed. pp 2611-2620
- ^ CRC Handbook of Chemistry and Physics, 44th ed. pp 2244-2248
- ^ Lange's Handbook of Chemistry, 10th ed. pp 1669-1674
- ^ Lange's Handbook of Chemistry, 10th ed, pp 1522-1524
- ^ Pure Component Properties (Queriable Database). Chemical Engineering Research Information Center. Retrieved on 27 May 2007.
- ^ a b c d Binary Vapor-Liquid Equilibrium Data (Queriable database). Chemical Engineering Research Information Center. Retrieved on 27 May 2007.
- NIST Standard Reference Database.
Except where noted otherwise, data relate to standard ambient temperature and pressure.
Disclaimer applies.
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