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	<title>One-way analysis of variance - Revision history</title>
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		<title>69.131.49.231: /* Assumptions */</title>
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		<updated>2013-12-27T08:33:03Z</updated>

		<summary type="html">&lt;p&gt;&lt;span class=&quot;autocomment&quot;&gt;Assumptions&lt;/span&gt;&lt;/p&gt;
&lt;p&gt;&lt;b&gt;New page&lt;/b&gt;&lt;/p&gt;&lt;div&gt;The &amp;#039;&amp;#039;&amp;#039;Hatta number&amp;#039;&amp;#039;&amp;#039; (&amp;#039;&amp;#039;&amp;#039;Ha&amp;#039;&amp;#039;&amp;#039;) was developed by Shirôji Hatta, who taught at [[Tohoku University]].&amp;lt;ref&amp;gt;S. Hatta, Technological Reports of Tôhoku University, 10, 613-622 (1932).&amp;lt;/ref&amp;gt; It is a dimensionless parameter that compares the rate of reaction in a liquid film to the rate of diffusion through the film.&amp;lt;ref&amp;gt;[[Robert Byron Bird|R.B. Bird]], W.E. Stewart, [[Edwin N. Lightfoot|E.N. Lightfoot]], Transport Phenomena, 2nd ed. John Wiley &amp;amp; Sons, 2002&amp;lt;/ref&amp;gt; For a second order reaction (&amp;#039;&amp;#039;r&amp;#039;&amp;#039;&amp;lt;sub&amp;gt;A&amp;lt;/sub&amp;gt; = &amp;#039;&amp;#039;k&amp;#039;&amp;#039;&amp;lt;sub&amp;gt;2&amp;lt;/sub&amp;gt;&amp;#039;&amp;#039;C&amp;#039;&amp;#039;&amp;lt;sub&amp;gt;B&amp;lt;/sub&amp;gt;&amp;#039;&amp;#039;C&amp;#039;&amp;#039;&amp;lt;sub&amp;gt;A&amp;lt;/sub&amp;gt;), the maximum rate of reaction assumes that the liquid film is saturated with gas at the interfacial concentration (&amp;#039;&amp;#039;C&amp;#039;&amp;#039;&amp;lt;sub&amp;gt;A,i&amp;lt;/sub&amp;gt;); thus, the maximum rate of reaction is &amp;#039;&amp;#039;k&amp;#039;&amp;#039;&amp;lt;sub&amp;gt;2&amp;lt;/sub&amp;gt;&amp;#039;&amp;#039;C&amp;#039;&amp;#039;&amp;lt;sub&amp;gt;B,bulk&amp;lt;/sub&amp;gt;&amp;#039;&amp;#039;C&amp;#039;&amp;#039;&amp;lt;sub&amp;gt;A,i&amp;lt;/sub&amp;gt;&amp;#039;&amp;#039;δ&amp;#039;&amp;#039;&amp;lt;sub&amp;gt;L&amp;lt;/sub&amp;gt;. &lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
&amp;lt;math&amp;gt;Ha^2 = {{k_{2} C_{A,i} C_{B,bulk} \delta_L} \over {\frac{D_A}{\delta_L}\ C_{A,i}}} = {{k_2 C_{B,bulk} D_A} \over ({\frac{D_A}{\delta_L}}) ^2} = {{k_2 C_{B,bulk} D_A} \over {{k_L} ^2}}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
For a reaction m&amp;lt;sup&amp;gt;th&amp;lt;/sup&amp;gt; order in A and n&amp;lt;sup&amp;gt;th&amp;lt;/sup&amp;gt; order in B:&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
&amp;lt;math&amp;gt;Ha = {{ \sqrt{{\frac{2}{{m} + 1}}k_{m,n} {C_{A,i}}^{m - 1} C_{B,bulk}^n {D}_A}} \over {{k}_L}}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
It is an important parameter used in Chemical Reaction Engineering&lt;br /&gt;
&lt;br /&gt;
==References==&lt;br /&gt;
{{reflist}}&lt;br /&gt;
&lt;br /&gt;
== See also ==&lt;br /&gt;
*[[Dimensionless quantity]]&lt;br /&gt;
*[[Dimensional analysis]]&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
[[Category:Catalysis]]&lt;br /&gt;
[[Category:Dimensionless numbers of chemistry]]&lt;br /&gt;
[[Category:Transport phenomena]]&lt;br /&gt;
{{chemistry-stub}}&lt;/div&gt;</summary>
		<author><name>69.131.49.231</name></author>
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