<?xml version="1.0" encoding="ISO-8859-1"?>

<rss version="2.0" xmlns:dc="http://purl.org/dc/elements/1.1/" xmlns:content="http://purl.org/rss/1.0/modules/content/">
	<channel>
		<title>CFD Online Discussion Forums - Blogs - OpenFOAM On Road by nimasam</title>
		<link>http://www.cfd-online.com/Forums/blogs/nimasam/</link>
		<description>Discussion forums related to Computational Fluid Dynamics. This is the largest meeting place on the web for people working with CFD.</description>
		<language>en</language>
		<lastBuildDate>Wed, 19 Jun 2013 09:40:30 GMT</lastBuildDate>
		<generator>vBulletin</generator>
		<ttl>60</ttl>
		<image>
			<url>http://www.cfd-online.com/Forums/images/misc/rss.jpg</url>
			<title>CFD Online Discussion Forums - Blogs - OpenFOAM On Road by nimasam</title>
			<link>http://www.cfd-online.com/Forums/blogs/nimasam/</link>
		</image>
		<item>
			<title>boiling in openFOAM</title>
			<link>http://www.cfd-online.com/Forums/blogs/nimasam/906-boiling-openfoam.html</link>
			<pubDate>Fri, 12 Aug 2011 20:06:00 GMT</pubDate>
			<description><![CDATA[i would like to review some works i have seen in openFOAM which involved boiling. 
maybe the main work is related to professor Peter Stephan's group...]]></description>
			<content:encoded><![CDATA[<div><font size="2">i would like to review some works i have seen in openFOAM which involved boiling.<br />
maybe the main work is related to professor <i>Peter Stephan</i>'s group from darmstadt university.<br />
they used the OpenFOAM solver (<b>interfoam</b>) as the basic solver and made new solver, first <i>Bitan shu</i> (<a href="http://www.cfd-online.com/Forums/openfoam-solving/57849-phase-change-vof.html" target="_blank">Phase change with VOF</a>) in paper &quot;</font><font size="2">PHASE CHANGE MODEL FOR TWO-PHASE FLUID FLOW BASED ON THE VOLUME OF FLUID METHOD&quot; implemented <i>welch</i>   method in &quot;A Volume of Fluid Based Method for Fluid Flows with Phase   Change&quot; , i tried to repeat bitan work again! but i could not resolve   interface diffusivity, because VOF in interFoam is not sharp! and it's a   transition region among two or 3 cells! and for boiling </font><font size="2">a sharp interface is needed</font><font size="2">, so i had an over estimation! it seems he has used an special treatment for interface diffusivity! <br />
second! <i>Christian Kunkelmann</i> developed the code! he made great progress, he implemented <i>hardt</i>   model in &quot;Evaporation model for interfacial flows based on a   continuum-field representation of the source terms&quot;, then he resolved   interface problem with combination of levelset method and VOF method in   &quot;Evaporation model for interfacial flows based on acontinuum-field   representation of the source terms &quot;.<br />
i followed their instruction, so i implement hardt model and i tried to resolve interface diffusivity , with dynamic mesh! (<a href="http://www.cfd-online.com/Forums/openfoam-solving/87665-evapphasechangefoam.html" target="_blank">evapPhaseChangeFOAM</a>) <br />
however it works well! but the mesh number increase so fast! and its   time- consuming so implementation of leveL set method is necessary!<br />
</font></div>

]]></content:encoded>
			<dc:creator>nimasam</dc:creator>
			<guid isPermaLink="true">http://www.cfd-online.com/Forums/blogs/nimasam/906-boiling-openfoam.html</guid>
		</item>
	</channel>
</rss>
