- InChI
- InChI=1S/C9H10/c1-3-9-7-5-4-6-8(9)2/h3-7H,1H2,2H3
- InChI Key
- NVZWEEGUWXZOKI-UHFFFAOYSA-N
- Formula
- C9H10
- SMILES
- C=Cc1ccccc1C
- Molecular Weight1
- 118.18
- CAS
- 611-15-4
- Other Names
-
- 1-Ethenyl-2-methylbenzene
- 1-METHYL-2-ETHENYLBENZENE
- 1-Methyl-2-vinylbenzene
- 2-Ethenylmethylbenzene
- 2-Methyl-1-vinylbenzene
- 2-Methylstyrene
- 2-Vinyltoluene
- Styrene, o-methyl-
- o-Methylstyrene
- o-Vinyltoluene
- ω : Acentric Factor.
- PAff : Proton affinity (kJ/mol).
- BasG : Gas basicity (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- η : Dynamic viscosity (Pa×s).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- Δc,grossH : Heat of Combustion, Gross form (kJ/mol).
- Δc,netH : Heat of Combustion, Net Form (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).
- 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).
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- Inp : Non-polar retention indices.
- Ip : Polar retention indices.
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.3250 | KDB | |
| PAff | 855.20 | kJ/mol | NIST |
| BasG | 826.30 | kJ/mol | NIST |
| ΔfG° | 215.52 | kJ/mol | Joback Calculated Property |
| Δc,grossH | 5044.65 | kJ/mol | KDB |
| Δc,netH | 4824.989 | kJ/mol | KDB |
| ΔfH°gas | 142.31 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 11.44 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 48.55 | kJ/mol | Relay (1.0) Calculated Property |
| IE | [8.20; 8.53] | eV |
|
| IE | 8.20 ± 0.02 | eV | NIST |
| IE | 8.53 | eV | NIST |
| log10WS | -2.79 | Relay (1.0) Calculated Property | |
| logPoct/wat | 2.638 | Crippen Calculated Property | |
| McVol | 109.610 | ml/mol | McGowan Calculated Property |
| Pc | 3370.00 | kPa | KDB |
| Inp | [147.84; 1016.00] |
|
|
| Inp | 955.00 | NIST | |
| Inp | 978.00 | NIST | |
| Inp | 975.00 | NIST | |
| Inp | 977.50 | NIST | |
| Inp | 1000.00 | NIST | |
| Inp | 982.00 | NIST | |
| Inp | 972.10 | NIST | |
| Inp | 974.20 | NIST | |
| Inp | 987.50 | NIST | |
| Inp | 993.20 | NIST | |
| Inp | 1000.40 | NIST | |
| Inp | 981.00 | NIST | |
| Inp | 990.60 | NIST | |
| Inp | 981.00 | NIST | |
| Inp | 976.00 | NIST | |
| Inp | 1016.00 | NIST | |
| Inp | 978.00 | NIST | |
| Inp | 985.00 | NIST | |
| Inp | 982.00 | NIST | |
| Inp | Outlier 161.30 | NIST | |
| Inp | Outlier 155.50 | NIST | |
| Inp | Outlier 163.20 | NIST | |
| Inp | Outlier 147.84 | NIST | |
| Inp | 955.00 | NIST | |
| Inp | 982.00 | NIST | |
| Inp | 1000.40 | NIST | |
| Inp | Outlier 161.30 | NIST | |
| Ip | [1327.00; 1342.20] |
|
|
| Ip | 1342.20 | NIST | |
| Ip | 1327.00 | NIST | |
| Ip | 1342.00 | NIST | |
| Ip | 1342.00 | NIST | |
| Ip | 1327.00 | NIST | |
| Tboil | [433.15; 444.20] | K |
|
| Tboil | 444.20 | K | KDB |
| Tboil | 433.15 ± 6.00 | K | NIST |
| Tc | 662.70 | K | KDB |
| Tfus | [204.58; 205.00] | K |
|
| Tfus | 205.00 | K | KDB |
| Tfus | 204.76 ± 0.50 | K | NIST |
| Tfus | 204.58 ± 0.10 | K | NIST |
| Vc | 0.412 | m3/kmol | KDB |
| Zc | 0.2522900 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [36.82; 47.90] | kJ/mol | [345.00; 444.20] |
|
| ΔvapH | 47.90 | kJ/mol | 345.00 | NIST |
| ΔvapH | 36.82 | kJ/mol | 444.20 | KDB |
| n0 | 1.54130 | 298.15 | KDB |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [131.89; 333.57] | J/mol×K | [273.00; 1000.00] |
Joback Predicted correlation
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | -2.78900e+01 | |||
| Coefficient B | 7.00420e-01 | |||
| Coefficient C | -4.52860e-04 | |||
| Coefficient D | 1.13900e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 131.89 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 168.27 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 200.31 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 228.38 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 252.84 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 274.05 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 292.37 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 308.15 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 321.77 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 333.57 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0034657; 0.0001847] | Pa×s | [204.78; 463.89] |
Joback Predicted correlation
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -1.09138e+01 | |||
| Coefficient B | 1.07488e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | Liquid phase. Joback/Reid (1987), valid from Tf to 0.7·Tc. | |||
| Temperature range, min. | 204.78 | |||
| Temperature range, max. | 463.89 | |||
| η | 0.0034657 | Pa×s | 204.78 | Calculated Property |
| η | 0.0018147 | Pa×s | 233.57 | Calculated Property |
| η | 0.0010952 | Pa×s | 262.36 | Calculated Property |
| η | 0.0007304 | Pa×s | 291.15 | Calculated Property |
| η | 0.0005239 | Pa×s | 319.94 | Calculated Property |
| η | 0.0003970 | Pa×s | 348.73 | Calculated Property |
| η | 0.0003139 | Pa×s | 377.52 | Calculated Property |
| η | 0.0002565 | Pa×s | 406.31 | Calculated Property |
| η | 0.0002153 | Pa×s | 435.10 | Calculated Property |
| η | 0.0001847 | Pa×s | 463.89 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.67] | kPa | [324.64; 459.17] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.53995e+01 | |||
| Coefficient B | -4.08230e+03 | |||
| Coefficient C | -5.44980e+01 | |||
| Temperature range, min. | 324.64 | |||
| Temperature range, max. | 459.17 | |||
| Pvap | 1.33 | kPa | 324.64 | Calculated Property |
| Pvap | 2.95 | kPa | 339.59 | Calculated Property |
| Pvap | 6.01 | kPa | 354.54 | Calculated Property |
| Pvap | 11.46 | kPa | 369.48 | Calculated Property |
| Pvap | 20.62 | kPa | 384.43 | Calculated Property |
| Pvap | 35.26 | kPa | 399.38 | Calculated Property |
| Pvap | 57.65 | kPa | 414.33 | Calculated Property |
| Pvap | 90.64 | kPa | 429.27 | Calculated Property |
| Pvap | 137.64 | kPa | 444.22 | Calculated Property |
| Pvap | 202.67 | kPa | 459.17 | Calculated Property |
| Pvap | [1.53e-05; 3470.16] | kPa | [204.58; 659.00] |
KDB Vapor Pressure Data
|
| Equation | ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K | |||
| Coefficient A | 8.28813e+01 | |||
| Coefficient B | -8.58406e+03 | |||
| Coefficient C | -9.80992e+00 | |||
| Coefficient D | 4.53627e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 204.58 | |||
| Temperature range, max. | 659.00 | |||
| Pvap | 1.53e-05 | kPa | 204.58 | Calculated Property |
| Pvap | 7.91e-03 | kPa | 255.07 | Calculated Property |
| Pvap | 0.40 | kPa | 305.56 | Calculated Property |
| Pvap | 5.55 | kPa | 356.05 | Calculated Property |
| Pvap | 35.92 | kPa | 406.54 | Calculated Property |
| Pvap | 143.08 | kPa | 457.04 | Calculated Property |
| Pvap | 413.59 | kPa | 507.53 | Calculated Property |
| Pvap | 961.92 | kPa | 558.02 | Calculated Property |
| Pvap | 1925.21 | kPa | 608.51 | Calculated Property |
| Pvap | 3470.16 | kPa | 659.00 | Calculated Property |
| Pvap | [0.39; 17.68] | kPa | [305.16; 385.50] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.44545e+01 | |||
| Coefficient B | -3.74939e+03 | |||
| Coefficient C | -6.17700e+01 | |||
| Reference | Clements, Wise, et al., 1953, 2 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 305.16 | |||
| Temperature range, max. | 385.50 | |||
| Pvap | 0.39 | kPa | 305.16 | Calculated Property |
| Pvap | 0.67 | kPa | 314.09 | Calculated Property |
| Pvap | 1.11 | kPa | 323.01 | Calculated Property |
| Pvap | 1.78 | kPa | 331.94 | Calculated Property |
| Pvap | 2.77 | kPa | 340.87 | Calculated Property |
| Pvap | 4.21 | kPa | 349.79 | Calculated Property |
| Pvap | 6.22 | kPa | 358.72 | Calculated Property |
| Pvap | 8.99 | kPa | 367.65 | Calculated Property |
| Pvap | 12.73 | kPa | 376.57 | Calculated Property |
| Pvap | 17.68 | kPa | 385.50 | Calculated Property |
| Pvap | [0.39; 17.68] | kPa | [305.16; 385.50] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.44545e+01 | |||
| Coefficient B | -3.74939e+03 | |||
| Coefficient C | -6.17700e+01 | |||
| Reference | Clements, Wise, et al., 1953 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 305.16 | |||
| Temperature range, max. | 385.50 | |||
| Pvap | 0.39 | kPa | 305.16 | Calculated Property |
| Pvap | 0.67 | kPa | 314.09 | Calculated Property |
| Pvap | 1.11 | kPa | 323.01 | Calculated Property |
| Pvap | 1.78 | kPa | 331.94 | Calculated Property |
| Pvap | 2.77 | kPa | 340.87 | Calculated Property |
| Pvap | 4.21 | kPa | 349.79 | Calculated Property |
| Pvap | 6.22 | kPa | 358.72 | Calculated Property |
| Pvap | 8.99 | kPa | 367.65 | Calculated Property |
| Pvap | 12.73 | kPa | 376.57 | Calculated Property |
| Pvap | 17.68 | kPa | 385.50 | Calculated Property |
Similar Compounds
![Dibenzo[a,e]cyclooctene.](data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAAPoAAAD6CAIAAAAHjs1qAAARu0lEQVR4nO3dXUxTZxzH8YcXu6HggIkbTlRkE9nAoajIxnw3ouILySTRjAtJVrIQidOL7o4LltjdzMaYuO6ChZuZNCTGThGGOqdRXhSHilamTgSVKQhTVoEi7S6e7OTkAKU9PT2n7f/3uVgyPT19aL99evqcyglzuVwMgIZwrQcAoB7kDoQgdyAEuQMhyB0IQe5ACHIHQpA7EILcgRDkDoQgdyAEuQMhyB0IQe5ACHIHQpA7EILcgRDkDoQgdyAEuQMhyB0IQe5ACHIHQpA7EILcgRDkDoQgdyAEuQMhyB0IQe5ACHIHQpA7EILcgRDkDoQgdyAEuQMhyB0IQe5ACHIHQpA7EILcgRDkDoQgdyAEuQMhyB0IQe5ACHIHQpA7EILcgRDkDoQgdyAEuQMhyB0IQe5ACHIHQpA7EILcgRDkDoQgdyAEuQMhyB0IQe5ACHIHQpA7EILcgRDkDoQgdyAEuQMhyB0IQe5ACHIHQpA7EILcgRDkDoQgdyAEuQMhkVoPIIi1t7c3NzdHRUXNmzdPhbvr6OgYHBxcvnx5amqqCncXmlwgS0VFRUREhPrPV0REREVFhdY/fbAKc7lc6j9nwe7EiRMFBQUul0un08XExKg2uw8MDDgcjrCwsOPHj2/fvl2FOw01Wr/egk9tbe2bb77JGFu8ePHo6Kiadz06Orp06VLGmE6ns1qtat51aEDu3hFaLykpcTqd6g/A6XSWlZWheHmQuxc0b51D8bLh2N1TdXV1O3bsGBoaKikpOXr0aFhYmPBXx44d6+rq8uu9JyUl7dq1S/hfl8u1b9++w4cP63S66urqrVu3+vXeQ4fWr7fg4H5ez83N9ffTlJubK7lTzPEyBMS6u9PprK2tzcnJiYuL03os43Azr3O7d+/Oycnx6xiSk5MlfxIWFmYymRhjhw8f/vzzzwN2ju/v729oaMjLywsPD4Bzmlq/3lzV1dXTp09njEVERJSUlKi81jGpADlen0ggz/FOp3P//v387ER0dPTPP/+s9Yg0/aja3d1dXFwsedFnZ2c3NjZqOCqxAG+dC8ziGxsbs7Ozxc9seHh4cXFxd3e3hqPSJneHw2Eymd566y3G2JQpU7Zt29bR0XHgwIE5c+YwxsLCwnbu3Pnw4UNNxiYIita5gCr+yZMner2ez2KJiYklJSVdXV27d+9+4403GGPTpk0rLy8fHBzUZGwa5F5fX//hhx/yV/z69etv3bol/JXdbi8vL+eRTZ06VcPHJYha5wKh+OHhYZPJxA9NdTpdWVnZixcvhL+9e/fuzp07+fP+/vvvWywW9Ueoau537tzZvHkz/4FTU1NPnTo17madnZ1FRUV8s6SkpKqqKjUH6QrC1jlti7darfPnz+fPWn5+/v3798fd7OzZsxkZGXyztWvX3rhxQ81BqpR7X1+fwWDQ6XSMsbi4OKPRODw87P4mv/3228cff8wfl9WrV7e2tqoz1CBtndOkeJvNlpeXx5+phQsXnj592v32IyMjZrM5ISGBMRYZGanX6589e6bOUP2e++joaFVVFf/ZwsPDi4qKnj59OnYzh8NRU1Mz7m1nzpzp/rYKCurWOTWLf/78eVlZWWRkJGMsPj7eZDKNjIxItqmpqXE4HGNv29fXJ9w2Li5u3Nsqzr+5nzt3btGiRfx1v2bNmuvXr0+05ffffz/RNv39/cI7Q2xsrCfvDPKEQOucCsXzGXrGjBnCDN3T0yPZxmazbdq0iTF26NChifYjbMOPb8dOecryV+7eHn9XVlbGx8fzx660tLS3t1eyQXt7+5YtW/gOFyxYcPLkSWUHHDKtc34t/syZM+np6fy5WLdu3c2bNyUb9Pb2lpaWCrN+ZWWl+x1ardaUlBThuP/evXvKDligfO7//vuvsLri1aqTJ8f39fX1H330kbCq09bWpsiYQ6x1zh/F//nnn8LqygcffDB2dUX2cTlfm+arOlOmTJGs6ihFydydTqfFYklKShLWzjs7O73dyaSrN5I1+7Kysn/++ceXYYdk65yCxQ8MDJSXl4vXzoeGhiTb+L7qwtfs+YnYxMREs9n8+vVrX4YtoVjuzc3NwvdGli1bdunSJV/2Vl9fn5aWNu7aPNfb21tWVsYfl7fffttkMsl7XEK4dc734vmCwTvvvCMsGPz999+SbZRdU7969arwrbslS5ZcvHjRl72JKZD748ePi4qK+BenZs2aZTabFfneiyez+LVr11auXMkfl8WLF//+++9e3UXIt875UnxjY+OKFSv4I7x8+fKGhgbJBrKPXScds8VimTt3rnBA39HR4ftufcr91atXRqMxJiaG/X8W7eXLl76PScyTWdxqtQpfGMzPz//rr7882TOR1jkZxXd1dQmz2HvvvVdVVSV5lJxOZ1VV1bvvvsuPXYuKihT/Pgw/yx4VFcUYmzp1qsFgGBgY8GWH8nOXF5k8LS0tn332mfDuduHCBckG4hdeVFSUwWBw/8Ij1TrnefF2u91oNEZHR7uJrKmpSXzsevnyZf+NXPzCmz179tgXnufk5C4+hMjMzDx//ry8+/aW1WoV/s1/fn7+gwcPJBs8evTI/YTEEWyd86R4pR5kxYm/Yin7a7Pe5S4+tOBn0ZT94Dwp8cTDZ/GxE4/kQ7Nk4iHbOuem+JaWFvEHxIneQsUPvuLHru558qHZPU9zH/vBsb+/3+vxKmTSCWaiw0rirXNji+/p6fHkA5J41vfrsat74iXR6OjocZdEJ+JR7t9+++20adOEZUGlTu74qKmpyatFgy+++AKtc+Liv/zyS/HJnXGXv4QPTjKWv/xEfMJr6tSp33zzjSe3mjz3gwcP8p0mJCT88ssvPo9TSeJ3t4kWB4QlYT4f7N27l3jrnNPp3Lt3L2OMTwHr16+/ffu2ZBulTm74T319fWJiIu/z4MGDk24/ee6rVq1ijCUmJtrtdiVGqDw+i7s/4XfkyBHGWEpKCloXOJ1O/k2VI0eOSP5K8VPX/mO323nxq1atmnTjyXPPz8/nh2sKDM2f3J/Yu3LlCmMsKytLq+EFpqysLMbYlStXxH/o5p+bBSbPE538dyHwR4T/N5DxxGtra9PS0u7du1dYWGixWLQeVPCxWCwbNmy4fft2WlpabW2tOP2A5Xmicn71x549ezIyMlpaWmTc1t82btx448YNs9mck5OzY8cOrYcTfAoKClasWGE0GltbWzdu3Kj1cMbR0tKSkZGxZ88eGbeV82uV7t+/39bWZrfbZdxWBfx7p3q9XuuBBKUpU6Y0NDRoPQp37HZ7W1ubvN/AFQC/2AlALcgdCEHuQAhyB0KQOxCC3IEQ5A6EIHcgBLkDIcgdCEHuQAhyB0KQOxCC3IEQ5A6EIHcgBLkDIcgdCEHuQAhyB0KQOxCC3IEQ5A6EIHcgBLkDIcgdCEHuQAhyB0KQOxAiJ/eUlJT09HThak2B5vXr1z/++GNOTs7w8LDWYwk+IyMjK1as+O677xwOh9ZjGd+0adPS09P5dUe8JecXXv/0008ybqWOurq6r7/+2mazMcZOnDhRWFio9YiCzPHjx5uampqamqqqqg4dOhSAv+I9Kyvr5s2b8m47+ezOL1sQmBcvELt7925hYWFeXp7NZuNX8kDrMhQWFvIrdthstry8vA0bNty6dUvrQU3Ci0QnvZxN4F+KTHyhTVyKzHO4FNk4guVCkxNdRhkXmhzX2AtNjr3kWFBcaJJfLJopdaFJV8hdRliv1xMvXnIZYfez+LVr11auXMkf59C/jDDH391iY2P546LX63t6enwYrU+6urrkXSS+rq4OxY+9SLwns7jVak1OTuZ5aXuR+P7+foPB4MeLxAueP38uPC7x8fHqv7vZ7Xaj0RgdHc1f0waDYWBgQLJNc3NzTk4Of2KWLVt2+fJl8d8SL35s64KWlhbhYvBLliy5cOGC5LavXr0yGo0xMTGMsaioKIPB8PLlSxXH7tGxq3ve5c798ccf/PMrY4xffVPGTmSwWq3z5s0TJpgHDx5INnj06JH7WZ8jW7yb1gVKPciKO3/+fGZmJh9YdnZ2Y2OjjJ3IyZ1T893Nw4mHz/qeTDwEi/ekdU78FsofTG/fQpUlPnadPXu2Ly8w+bm7XK7h4WGTycTf3XQ6XVlZmeLvbj09PZ4cVoonJA9feKSK97x1waSz+EQfkBRkt9vLy8ujoqL4sWt5efmrV6982aFPuXOPHz/W6/Xh4eGMsVmzZpnN5tHRUd93yz8cT58+3X+LBkSKl9G6wNvlr/Ly8sHBQUXGbLFY5s6dy19LO3fu7Ojo8H23CuTONTc3f/LJJ/xxWbp06aVLl3zZW319fVpamrD0efv2bckGSi0Jh3zxvrTOiT8gTjSLCyc3GGMpKSkWi8WXMV+9evXTTz/le8vKyrp48aIvexNTLHfX/6/IpKQk4RX58OFDb3dy586dzZs38x81NTX11KlTkg0UP+EXwsX73rqAz+LuT12fPXs2IyODP3dr1669fv26t/fy5MkT4UghMTHRbDYru/SnZO6c7He3vr4+g8Gg0+kYY3FxcUajcXh4WLIN/zqHMOsrdcIrJItXsHWB+OQO/2KSZIORkRGz2ZyQkMAYi4yM1Ov1z54982TPY49dX7x4ociYxZTPnevs7CwqKuKPS1JSUlVVlfvtKysr4+Pj+WNUWlra29sr2aC9vX3Lli18hwsWLDh58qSyAw6x4v3RuuDMmTPp6en8uVi3bt2NGzckG/T29paWlkZGRjLG4uPjKysr3e/QarUKX+jNz8+/d++esgMW+Ct37ty5c4sWLeI/xpo1a9y8ux06dGiibfhZND7rx8bGjjvrKyJkivdr6xyfxWfMmCHM4mPPst+5c2fTpk2MMZPJNNF+bDYb34YxtnDhwpqaGn+MVuDf3F3/f9CZOXMm+/9M2NOnT8du5nA4xv6oHt5WQSFQvAqtC/hZdmEWN5lMIyMjkm1qamocDof728bFxY17W8X5PXfOk+NyCfE7w+rVq1tbW9UZalAXr2brAv7NeGGGPn36tPvtZR/f+06l3LlJV104b4/7FRekxWvSusBqtc6fP184/r5///64m0lWb8Ye9/uVqrlzktUV8desxas6/CyaIucsZAi64rVtneNn2fnqCj/LLl5dEa/Nj7uqowINcneNWTvftm1bR0fHgQMH5syZ48uavbKCqPhAaF0gWTsvKSnp6uravXu3+zV7dWiTO9fd3V1cXMwfF4HsL7v5Q1AUH1CtCxobG7Ozs8XPbHh4eHFxseLfq/GKlrlz1dXV/O0vIiKipKREke/bKCjAiw/M1jmn07l//37+RY/o6Ohjx45pPSJXmMvlYlpzOp21tbU5OTlxcXFaj2Ucv/766/bt24eGhvR6/Q8//MC/JCh29OjRBw8e+HUMycnJX331leQPXS7Xvn37Dh8+rNPpqqurt27d6tcxyNPf39/Q0JCXlyd5G9eG1q+34OB+js/NzfX305Sbmyu500Ce1wNWQMzuQcHNHH/s2LGuri6/3ntSUtKuXbuE/3UFw7weiLR+vQWTADmOx7wuG3L3jubFo3VfIHevCcVnZmaqvI40Ojq6dOlStC4bjt3lOHHiREFBgcvl0ul0MTExwr+U9auOjo6BgQGHwxEWFnb8+PHt27ercKehRuvXW7CqqKjgK8oqi4iIqKio0PqnD1aY3eVrb29vbm6OiopSbXYfHBxcvnx5amqqCncXkpA7EBIAJ7oA1ILcgRDkDoQgdyAEuQMhyB0IQe5ACHIHQpA7EILcgRDkDoQgdyAEuQMhyB0IQe5ACHIHQpA7EILcgRDkDoQgdyAEuQMhyB0IQe5ACHIHQpA7EILcgRDkDoQgdyAEuQMhyB0IQe5ACHIHQpA7EILcgRDkDoQgdyAEuQMhyB0IQe5ACHIHQpA7EILcgRDkDoQgdyAEuQMhyB0IQe5ACHIHQpA7EILcgRDkDoQgdyAEuQMhyB0IQe5ACHIHQpA7EILcgRDkDoQgdyAEuQMhyB0IQe5ACHIHQpA7EILcgRDkDoQgdyAEuQMhyB0IQe5ACHIHQpA7EILcgRDkDoQgdyDkP75s+TMr+GBiAAAAAElFTkSuQmCC)
Find more compounds similar to Benzene, 1-ethenyl-2-methyl-.
Sources
- KDB Vapor Pressure Data
- Cheméo Relay (1.0)
- Crippen Method
- Crippen Method
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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