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		<id>https://en.formulasearchengine.com/w/index.php?title=Projected_area&amp;diff=23236</id>
		<title>Projected area</title>
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		<updated>2013-10-04T17:58:51Z</updated>

		<summary type="html">&lt;p&gt;216.49.150.43: it wanted curlies that it didn&amp;#039;t care for in the preview. Weird.&lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;The &#039;&#039;&#039;Lee-Kesler method&#039;&#039;&#039; &lt;br /&gt;
&amp;lt;ref&amp;gt;Lee B.I., Kesler M.G., &amp;quot;A Generalized Thermodynamic Correlation Based on Three-Parameter Corresponding States&amp;quot;, AIChE J., 21(3), 510-527, 1975&lt;br /&gt;
&amp;lt;/ref&amp;gt;&lt;br /&gt;
allows the estimation of the [[saturated vapor pressure]] at a given temperature for all components for which the [[critical pressure]] P&amp;lt;sub&amp;gt;c&amp;lt;/sub&amp;gt;, the [[critical temperature]] T&amp;lt;sub&amp;gt;c&amp;lt;/sub&amp;gt;, and the [[acentric factor]] ω are known.&lt;br /&gt;
&lt;br /&gt;
== Equations ==&lt;br /&gt;
&amp;lt;math&amp;gt; \ln P_r = f^{(0)} + \omega \cdot f^{(1)} &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;math&amp;gt; f^{(0)}=5.92714 - \frac{6.09648}{T_r} - 1.28862 \cdot \ln T_r + 0.169347 \cdot T_r^6 &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;math&amp;gt; f^{(1)}=15.2518 - \frac{15.6875}{T_r}-13.4721 \cdot \ln T_r + 0.43577 \cdot T_r^6 &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
with&lt;br /&gt;
&lt;br /&gt;
&amp;lt;math&amp;gt;P_r=\frac{P}{P_c}&amp;lt;/math&amp;gt; ([[reduced pressure]]) und &amp;lt;math&amp;gt;T_r=\frac{T}{T_c}&amp;lt;/math&amp;gt; ([[reduced temperature]]).&lt;br /&gt;
&lt;br /&gt;
== Typical errors ==&lt;br /&gt;
The prediction error can be up to 10% for polar components and small pressures and the calculated pressure is typically too low. For pressures above 1&amp;amp;nbsp;bar, that means, above the normal boiling point, the typical errors are below 2%.&lt;br /&gt;
&amp;lt;ref&amp;gt;Reid R.C., Prausnitz J.M., Poling B.E., &amp;quot;The Properties of Gases &amp;amp; Liquids&amp;quot;, 4. Auflage, McGraw-Hill, 1988&lt;br /&gt;
&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
== Example calculation ==&lt;br /&gt;
For [[benzene]] with&lt;br /&gt;
* T&amp;lt;sub&amp;gt;c&amp;lt;/sub&amp;gt; = 562.12 K&amp;lt;ref name=&amp;quot;Brunner&amp;quot;&amp;gt;Brunner E., Thies M.C., Schneider G.M., J.Supercrit.Fluids, 39(2), 160-173, 2006&amp;lt;/ref&amp;gt;&lt;br /&gt;
* P&amp;lt;sub&amp;gt;c&amp;lt;/sub&amp;gt; = 4898 kPa&amp;lt;ref name=&amp;quot;Brunner&amp;quot; /&amp;gt;&lt;br /&gt;
* T&amp;lt;sub&amp;gt;b&amp;lt;/sub&amp;gt; = 353.15 K&amp;lt;ref&amp;gt;Silva L.M.C., Mattedi S., Gonzalez-Olmos R., Iglesias M., J.Chem.Thermodyn., 38(12), 1725-1736, 2006&amp;lt;/ref&amp;gt;&lt;br /&gt;
* ω = 0.2120&amp;lt;ref&amp;gt;[[Dortmund Data Bank]]&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
the following calculation for T=T&amp;lt;sub&amp;gt;b&amp;lt;/sub&amp;gt; results:&lt;br /&gt;
&lt;br /&gt;
* T&amp;lt;sub&amp;gt;r&amp;lt;/sub&amp;gt; = 353.15 / 562.12 = 0.628247&lt;br /&gt;
* f&amp;lt;sup&amp;gt;(0)&amp;lt;/sup&amp;gt; = -3.167428&lt;br /&gt;
* f&amp;lt;sup&amp;gt;(1)&amp;lt;/sup&amp;gt; = -3.429560&lt;br /&gt;
* P&amp;lt;sub&amp;gt;r&amp;lt;/sub&amp;gt; = exp( f&amp;lt;sup&amp;gt;(0)&amp;lt;/sup&amp;gt; + ω f&amp;lt;sup&amp;gt;(1)&amp;lt;/sup&amp;gt; ) = 0.020354&lt;br /&gt;
* P = P&amp;lt;sub&amp;gt;r&amp;lt;/sub&amp;gt; * P&amp;lt;sub&amp;gt;c&amp;lt;/sub&amp;gt; = 99.69 kPa&lt;br /&gt;
&lt;br /&gt;
The correct result would be P = 101.325 kPa, the normal (atmospheric) pressure. The deviation is -1.63 kPa or -1.61 %.&lt;br /&gt;
&lt;br /&gt;
It is important to use the same absolute units for T and T&amp;lt;sub&amp;gt;c&amp;lt;/sub&amp;gt; as well as for P and P&amp;lt;sub&amp;gt;c&amp;lt;/sub&amp;gt;. The unit system used (K or R for T) is irrelevant because of the usage of the reduced values T&amp;lt;sub&amp;gt;r&amp;lt;/sub&amp;gt; and P&amp;lt;sub&amp;gt;r&amp;lt;/sub&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&amp;lt;references/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
{{DEFAULTSORT:Lee-Kesler Method}}&lt;br /&gt;
[[Category:Thermodynamic models]]&lt;/div&gt;</summary>
		<author><name>216.49.150.43</name></author>
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