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	<title>Three cups problem - Revision history</title>
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		<title>en&gt;Wahrmund: /* Proof of impossibility */ Missing word.</title>
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		<summary type="html">&lt;p&gt;&lt;span class=&quot;autocomment&quot;&gt;Proof of impossibility: &lt;/span&gt; Missing word.&lt;/p&gt;
&lt;p&gt;&lt;b&gt;New page&lt;/b&gt;&lt;/p&gt;&lt;div&gt;In [[fluid dynamics]], the &amp;#039;&amp;#039;&amp;#039;Buckley–Leverett equation&amp;#039;&amp;#039;&amp;#039; is a [[Generic scalar transport equation|transport equation]] used to model [[two-phase flow]] in [[porous media]].&amp;lt;ref&amp;gt;{{cite journal|author=S.E. Buckley and M.C. Leverett|title=Mechanism of fluid displacements in sands|url=http://www.aimehq.org/library/books/Petroleum%20Technology,%201941,%20Vol.%20IV/T.P.%201337.pdf|journal=Transactions of the AIME|issue=146|pages=107–116|year=1942}}&amp;lt;/ref&amp;gt; The Buckley–Leverett equation or the Buckley–Leverett &amp;#039;&amp;#039;displacement&amp;#039;&amp;#039; can be interpreted as a way of incorporating the microscopic effects due to [[capillary pressure]] in [[two-phase flow]] into [[Darcy&amp;#039;s law]].&lt;br /&gt;
&lt;br /&gt;
In a 1D sample ([[control volume]]), let &amp;lt;math&amp;gt;S(x,t)&amp;lt;/math&amp;gt; be the [[water saturation]], then the Buckley–Leverett equation is&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;\frac{\partial S}{\partial t} = U(S)\frac{\partial S}{\partial x}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
where &lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;U(S) = \frac{Q}{\phi A} \frac{\mathrm{d} f}{\mathrm{d} S}.&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;math&amp;gt;f&amp;lt;/math&amp;gt; is the fractional flow rate, &amp;lt;math&amp;gt;Q&amp;lt;/math&amp;gt; is the total flow, &amp;lt;math&amp;gt;\phi&amp;lt;/math&amp;gt; is [[porosity]] and &amp;lt;math&amp;gt;A&amp;lt;/math&amp;gt; is area of the cross-section in the sample volume.&lt;br /&gt;
&lt;br /&gt;
==Assumptions for validity==&lt;br /&gt;
The Buckley–Leverett equation is derived for a 1D sample given&lt;br /&gt;
* [[Conservation of mass|mass conservation]]&lt;br /&gt;
* [[capillary pressure]] &amp;lt;math&amp;gt;p_c(S)&amp;lt;/math&amp;gt; is a function of [[water saturation]] &amp;lt;math&amp;gt;S&amp;lt;/math&amp;gt; only&lt;br /&gt;
* &amp;lt;math&amp;gt;\mathrm{d}p_c/\mathrm{d}S = 0&amp;lt;/math&amp;gt; causing the [[pressure gradients]] of the two phases to be equal.&lt;br /&gt;
* Flow is Linear&lt;br /&gt;
* Flow is Steady-State&lt;br /&gt;
* Formation is one Layer&lt;br /&gt;
&lt;br /&gt;
==General solution==&lt;br /&gt;
&lt;br /&gt;
The solution of the Buckley&amp;amp;ndash;Leverett equation has the form &amp;lt;math&amp;gt;S(x,t) = S(x+U(S)t)&amp;lt;/math&amp;gt; which means that &amp;lt;math&amp;gt;U(S)&amp;lt;/math&amp;gt; is the [[front velocity]] of the fluids at saturation &amp;lt;math&amp;gt;S&amp;lt;/math&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
==See also==&lt;br /&gt;
* [[Capillary pressure]]&lt;br /&gt;
* [[Permeability (fluid)]]&lt;br /&gt;
* [[Relative permeability]]&lt;br /&gt;
* [[Darcy&amp;#039;s law]]&lt;br /&gt;
&lt;br /&gt;
==References==&lt;br /&gt;
{{reflist}}&lt;br /&gt;
&lt;br /&gt;
{{DEFAULTSORT:Buckley-Leverett equation}}&lt;br /&gt;
[[Category:Hyperbolic partial differential equations]]&lt;br /&gt;
[[Category:Equations of fluid dynamics]]&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
{{fluiddynamics-stub}}&lt;/div&gt;</summary>
		<author><name>en&gt;Wahrmund</name></author>
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