<!-- Exported from Cranium Knowledge Base: MKS Core Knowledge Base - Internal.mkskbd -->
<!-- Exported on Apr 07, 2020 at 16:29:51 -->

<comp>
  <!-- Ethyl acetate -->
    <id number="20000031" formula="C4H8O2" name="Ethyl acetate" casNum="141-78-6">
    COMP0001
  </id>

  <!-- Structural Groups -->
    <structure>
    0700(1) 0900(1) 0901(1)
  </structure>

  <!-- Critical Properties -->
    <property name="ZC" value="0.252"></property>
    <property name="TC" value="523.2" uom="k"></property>
    <property name="PC" value="3830" uom="kpa"></property>
    <property name="VC" value="0.286" uom="m3/kg-mole"></property>

  <!-- Thermodynamic Properties -->
    <property name="GFORMATION" value="-3.1316e+08" uom="j/kg-mole"></property>
    <property name="HFORMATION" value="-4.441e+08" uom="j/kg-mole"></property>
    <property name="HFUSIONNMP" value="1.0485e+07" uom="j/kg-mole"></property>

  <!-- Safety Properties -->
    <property name="HIFLAMM" value="11.5" uom="pct"></property>
    <property name="LOFLAMM" value="2" uom="pct"></property>
    <property name="HCOMBUST" value="-2.2375e+09" uom="j/kg-mole"></property>
    <property name="AUTOIGNITION" value="699.817" uom="k"></property>

  <!-- Basic Properties -->
    <property name="SOLUPARA" value="8.89765"></property>
    <property name="DIPOLE" value="1.78"></property>
    <property name="RADIUS" value="3.468" uom="ang"></property>
    <property name="MW" value="88.1051"></property>
    <property name="ACENTRIC" value="0.362"></property>
    <property name="NBP" value="350.3" uom="k"></property>
    <property name="NMP" value="189.6" uom="k"></property>

  <!-- Thermal Conductivities -->
    <correlation tempUnit="k" propUnit="w/mk" tMin="189.6" tMax="481.344" name="LiquidThermal" equation="1">
    0.174049 7.61498e-05 -1.05162e-07 -2.79635e-09 3.62402e-12
  </correlation>
    <correlation tempUnit="k" propUnit="w/mk" tMin="350.3" tMax="723.2" name="VaporThermal" equation="19">
    128.188 0.447211 3.84774e+07 2.1497e+09
  </correlation>

  <!-- Viscosities -->
    <correlation logBasis="ln" tempUnit="k" propUnit="pas" tMin="189.6" tMax="481.344" name="LiquidViscosity" equation="20">
    -42.9828 1896.22 5.24657 -1.18028e-05
  </correlation>
    <correlation tempUnit="k" propUnit="pas" tMin="350.3" tMax="723.2" name="VaporViscosity" equation="19">
    4.96275e-06 0.272563 425.211 73189.3
  </correlation>

  <!-- Enthalpies -->
    <correlation moleWtBasis="m" tempUnit="k" propUnit="j/kg-mole" tMin="189.6" tMax="481.344" name="LiquidEnthalpy" equation="1">
    -6.71069e+07 288227 -608.016 1.16 -0.000605179
  </correlation>
    <correlation moleWtBasis="m" tempUnit="k" propUnit="j/kg-mole" tMin="350.3" tMax="723.2" name="IdealEnthalpy" equation="17">
    -5.11256e+07 109398 113682 1030.12 72716.6 1010.9
  </correlation>

  <!-- Densities -->
    <correlation moleWtBasis="m" tempUnit="k" propUnit="kg/m3-mole" tMin="189.6" tMax="481.344" name="LiquidDensity" equation="1">
    -137.161 1.97148 -0.00975509 2.12938e-05 -1.74235e-08
  </correlation>

  <!-- Liquid Properties -->
    <correlation tempUnit="k" propUnit="n/m" tMin="189.6" tMax="481.344" name="SurfaceTension" equation="1">
    0.0554796 -2.02376e-06 -7.51203e-07 1.72011e-09 -1.29894e-12
  </correlation>
    <correlation moleWtBasis="m" tempUnit="k" propUnit="j/kg-mole" tMin="189.6" tMax="481.344" name="LatentHeat" equation="15">
    4.933e+07 0.3847 -3.43188e-07
  </correlation>
    <correlation logBasis="ln" tempUnit="k" propUnit="pa" tMin="189.6" tMax="481.344" name="VaporPressure" equation="20">
    94.5607 -7106.79 -10.8907 8.65252e-06
  </correlation>
</comp>