<?xml version="1.0"?>
<feed xmlns="http://www.w3.org/2005/Atom" xml:lang="en">
		<id>http://wiki.newmars.com/index.php?action=history&amp;feed=atom&amp;title=Overall_heat_transfer_coefficient</id>
		<title>Overall heat transfer coefficient - Revision history</title>
		<link rel="self" type="application/atom+xml" href="http://wiki.newmars.com/index.php?action=history&amp;feed=atom&amp;title=Overall_heat_transfer_coefficient"/>
		<link rel="alternate" type="text/html" href="http://wiki.newmars.com/index.php?title=Overall_heat_transfer_coefficient&amp;action=history"/>
		<updated>2026-05-25T00:00:46Z</updated>
		<subtitle>Revision history for this page on the wiki</subtitle>
		<generator>MediaWiki 1.29.1</generator>

	<entry>
		<id>http://wiki.newmars.com/index.php?title=Overall_heat_transfer_coefficient&amp;diff=405&amp;oldid=prev</id>
		<title>Josh Cryer: 1 revision</title>
		<link rel="alternate" type="text/html" href="http://wiki.newmars.com/index.php?title=Overall_heat_transfer_coefficient&amp;diff=405&amp;oldid=prev"/>
				<updated>2009-01-21T11:02:34Z</updated>
		
		<summary type="html">&lt;p&gt;1 revision&lt;/p&gt;
&lt;table class=&quot;diff diff-contentalign-left&quot; data-mw=&quot;interface&quot;&gt;
				&lt;tr style=&#039;vertical-align: top;&#039; lang=&#039;en&#039;&gt;
				&lt;td colspan=&#039;1&#039; style=&quot;background-color: white; color:black; text-align: center;&quot;&gt;← Older revision&lt;/td&gt;
				&lt;td colspan=&#039;1&#039; style=&quot;background-color: white; color:black; text-align: center;&quot;&gt;Revision as of 11:02, 21 January 2009&lt;/td&gt;
				&lt;/tr&gt;&lt;tr&gt;&lt;td colspan=&#039;2&#039; style=&#039;text-align: center;&#039; lang=&#039;en&#039;&gt;&lt;div class=&quot;mw-diff-empty&quot;&gt;(No difference)&lt;/div&gt;
&lt;/td&gt;&lt;/tr&gt;&lt;/table&gt;</summary>
		<author><name>Josh Cryer</name></author>	</entry>

	<entry>
		<id>http://wiki.newmars.com/index.php?title=Overall_heat_transfer_coefficient&amp;diff=404&amp;oldid=prev</id>
		<title>Josh Cryer: Reverted edit of MonchIcotr, changed back to last version by C M Edwards</title>
		<link rel="alternate" type="text/html" href="http://wiki.newmars.com/index.php?title=Overall_heat_transfer_coefficient&amp;diff=404&amp;oldid=prev"/>
				<updated>2009-01-20T13:25:30Z</updated>
		
		<summary type="html">&lt;p&gt;Reverted edit of MonchIcotr, changed back to last version by C M Edwards&lt;/p&gt;
&lt;p&gt;&lt;b&gt;New page&lt;/b&gt;&lt;/p&gt;&lt;div&gt;An overall heat transfer coefficient h&amp;lt;sub&amp;gt;overall&amp;lt;/sub&amp;gt; can be calculated for a given system, given its heat transfer behavior, so that it can be described by Newton’s Law of Cooling:&lt;br /&gt;
&lt;br /&gt;
&amp;lt;math&amp;gt;q = h_{overall} \cdot A \cdot \Delta T&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
where q is the heat transfer rate, h is the heat transfer coefficient for the system, A is the area of heat transfer, and delta-T is the temperature difference between the zones of heat transfer.  This description of heat transfer can be applied to the combined effects of conduction, cooling, and radiation.&lt;br /&gt;
&lt;br /&gt;
Generally, for a body at some temperature T&amp;lt;sub&amp;gt;body&amp;lt;/sub&amp;gt; in a reservoir of fluid T&amp;lt;sub&amp;gt;fluid&amp;lt;/sub&amp;gt;:&lt;br /&gt;
&lt;br /&gt;
&amp;lt;math&amp;gt; \Delta T = T_{body} - T_{fluid} &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
==Deriving the Overall Heat Transfer Coefficient==&lt;br /&gt;
&lt;br /&gt;
If the heat transfer rate is known, then h&amp;lt;sub&amp;gt;overall&amp;lt;/sub&amp;gt; can be derived directly from Newton’s Law of Cooling.  However, if the other thermal characteristics of the system are known ([[heat transfer coefficient|heat transfer coefficients]], [[thermal conductivity|thermal conductivities]], and [[emissivity]]), the overall heat transfer coefficient can be calculated from the thermal resistance for simple systems.&lt;br /&gt;
&lt;br /&gt;
&amp;lt;math&amp;gt;h_{overall} = \frac{{1}}{{R_{total}}} &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
where A is the area of the heat transfer surface and R&amp;lt;sub&amp;gt;total&amp;lt;/sub&amp;gt; is the total thermal resistance of the transfer surface.&lt;br /&gt;
&lt;br /&gt;
Thermal resistances in series, like electrical resistances in series, are additive.  So, for heat passing into a wall by convection, through the wall by conduction, then out by a combination of convection and radiation, the total resistance is equal to the sum of the resistances at each step.  &lt;br /&gt;
&lt;br /&gt;
&amp;lt;math&amp;gt;R_{total} = R_{in} + R_{through} + R_{out} &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
h is analogous to thermal conductivity, and R can be defined relative to thermal conductivity just like it can relative to h.  So,&lt;br /&gt;
&lt;br /&gt;
&amp;lt;math&amp;gt;R_{total} = A \cdot ( \frac{{1}}{{A_{in} \cdot h_{in}}} + \frac{{t}}{{A_{mean} \cdot k}} + \frac{{1}}{{A_{out} \cdot h_{out}}} )&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
which can be inverted to obtain the overall heat transfer coefficient.&lt;br /&gt;
&lt;br /&gt;
*see also: [[Thermodynamics of the greenhouse]]&lt;br /&gt;
&lt;br /&gt;
{{MainArticle|[[Heat transfer|Heat Transfer]]}}&lt;/div&gt;</summary>
		<author><name>Josh Cryer</name></author>	</entry>

	</feed>