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		<title>DWSIM/C2/Heat-Exchanger/English - Revision history</title>
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		<updated>2026-04-22T15:07:06Z</updated>
		<subtitle>Revision history for this page on the wiki</subtitle>
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	<entry>
		<id>https://script.spoken-tutorial.org/index.php?title=DWSIM/C2/Heat-Exchanger/English&amp;diff=38191&amp;oldid=prev</id>
		<title>Kaushik Datta at 05:58, 18 August 2017</title>
		<link rel="alternate" type="text/html" href="https://script.spoken-tutorial.org/index.php?title=DWSIM/C2/Heat-Exchanger/English&amp;diff=38191&amp;oldid=prev"/>
				<updated>2017-08-18T05:58:46Z</updated>
		
		<summary type="html">&lt;p&gt;&lt;/p&gt;
&lt;a href=&quot;https://script.spoken-tutorial.org/index.php?title=DWSIM/C2/Heat-Exchanger/English&amp;amp;diff=38191&amp;amp;oldid=38177&quot;&gt;Show changes&lt;/a&gt;</summary>
		<author><name>Kaushik Datta</name></author>	</entry>

	<entry>
		<id>https://script.spoken-tutorial.org/index.php?title=DWSIM/C2/Heat-Exchanger/English&amp;diff=38177&amp;oldid=prev</id>
		<title>Kaushik Datta at 08:39, 17 August 2017</title>
		<link rel="alternate" type="text/html" href="https://script.spoken-tutorial.org/index.php?title=DWSIM/C2/Heat-Exchanger/English&amp;diff=38177&amp;oldid=prev"/>
				<updated>2017-08-17T08:39:18Z</updated>
		
		<summary type="html">&lt;p&gt;&lt;/p&gt;
&lt;table class='diff diff-contentalign-left'&gt;
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				&lt;col class='diff-content' /&gt;
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				&lt;td colspan='2' style=&quot;background-color: white; color:black; text-align: center;&quot;&gt;← Older revision&lt;/td&gt;
				&lt;td colspan='2' style=&quot;background-color: white; color:black; text-align: center;&quot;&gt;Revision as of 08:39, 17 August 2017&lt;/td&gt;
				&lt;/tr&gt;&lt;tr&gt;&lt;td colspan=&quot;2&quot; class=&quot;diff-lineno&quot;&gt;Line 13:&lt;/td&gt;
&lt;td colspan=&quot;2&quot; class=&quot;diff-lineno&quot;&gt;Line 13:&lt;/td&gt;&lt;/tr&gt;
&lt;tr&gt;&lt;td class='diff-marker'&gt;&amp;#160;&lt;/td&gt;&lt;td style=&quot;background-color: #f9f9f9; color: #333333; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #e6e6e6; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;div&gt;'''Learning Objective'''&lt;/div&gt;&lt;/td&gt;&lt;td class='diff-marker'&gt;&amp;#160;&lt;/td&gt;&lt;td style=&quot;background-color: #f9f9f9; color: #333333; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #e6e6e6; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;div&gt;'''Learning Objective'''&lt;/div&gt;&lt;/td&gt;&lt;/tr&gt;
&lt;tr&gt;&lt;td class='diff-marker'&gt;&amp;#160;&lt;/td&gt;&lt;td style=&quot;background-color: #f9f9f9; color: #333333; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #e6e6e6; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;div&gt;|| In this tutorial, we will learn to:&lt;/div&gt;&lt;/td&gt;&lt;td class='diff-marker'&gt;&amp;#160;&lt;/td&gt;&lt;td style=&quot;background-color: #f9f9f9; color: #333333; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #e6e6e6; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;div&gt;|| In this tutorial, we will learn to:&lt;/div&gt;&lt;/td&gt;&lt;/tr&gt;
&lt;tr&gt;&lt;td class='diff-marker'&gt;−&lt;/td&gt;&lt;td style=&quot;color:black; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #ffe49c; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;div&gt;&lt;del style=&quot;font-weight: bold; text-decoration: none;&quot;&gt;&lt;/del&gt;&lt;/div&gt;&lt;/td&gt;&lt;td colspan=&quot;2&quot;&gt;&amp;#160;&lt;/td&gt;&lt;/tr&gt;
&lt;tr&gt;&lt;td class='diff-marker'&gt;&amp;#160;&lt;/td&gt;&lt;td style=&quot;background-color: #f9f9f9; color: #333333; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #e6e6e6; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;/td&gt;&lt;td class='diff-marker'&gt;&amp;#160;&lt;/td&gt;&lt;td style=&quot;background-color: #f9f9f9; color: #333333; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #e6e6e6; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;/td&gt;&lt;/tr&gt;
&lt;tr&gt;&lt;td class='diff-marker'&gt;&amp;#160;&lt;/td&gt;&lt;td style=&quot;background-color: #f9f9f9; color: #333333; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #e6e6e6; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;div&gt;* Simulate a''' Heat Exchanger'''&lt;/div&gt;&lt;/td&gt;&lt;td class='diff-marker'&gt;&amp;#160;&lt;/td&gt;&lt;td style=&quot;background-color: #f9f9f9; color: #333333; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #e6e6e6; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;div&gt;* Simulate a''' Heat Exchanger'''&lt;/div&gt;&lt;/td&gt;&lt;/tr&gt;
&lt;tr&gt;&lt;td colspan=&quot;2&quot; class=&quot;diff-lineno&quot;&gt;Line 296:&lt;/td&gt;
&lt;td colspan=&quot;2&quot; class=&quot;diff-lineno&quot;&gt;Line 295:&lt;/td&gt;&lt;/tr&gt;
&lt;tr&gt;&lt;td class='diff-marker'&gt;&amp;#160;&lt;/td&gt;&lt;td style=&quot;background-color: #f9f9f9; color: #333333; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #e6e6e6; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;/td&gt;&lt;td class='diff-marker'&gt;&amp;#160;&lt;/td&gt;&lt;td style=&quot;background-color: #f9f9f9; color: #333333; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #e6e6e6; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;/td&gt;&lt;/tr&gt;
&lt;tr&gt;&lt;td class='diff-marker'&gt;&amp;#160;&lt;/td&gt;&lt;td style=&quot;background-color: #f9f9f9; color: #333333; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #e6e6e6; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;/td&gt;&lt;td class='diff-marker'&gt;&amp;#160;&lt;/td&gt;&lt;td style=&quot;background-color: #f9f9f9; color: #333333; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #e6e6e6; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;/td&gt;&lt;/tr&gt;
&lt;tr&gt;&lt;td class='diff-marker'&gt;−&lt;/td&gt;&lt;td style=&quot;color:black; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #ffe49c; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;div&gt;'''&lt;del class=&quot;diffchange diffchange-inline&quot;&gt;S'''elect &lt;/del&gt;'''Flash Spec '''as '''Temperature and Pressure (TP).'''&lt;/div&gt;&lt;/td&gt;&lt;td class='diff-marker'&gt;+&lt;/td&gt;&lt;td style=&quot;color:black; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #a3d3ff; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;div&gt;'''&lt;ins class=&quot;diffchange diffchange-inline&quot;&gt;Select &lt;/ins&gt;'''Flash Spec '''as '''Temperature and Pressure (TP).'''&lt;/div&gt;&lt;/td&gt;&lt;/tr&gt;
&lt;tr&gt;&lt;td class='diff-marker'&gt;&amp;#160;&lt;/td&gt;&lt;td style=&quot;background-color: #f9f9f9; color: #333333; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #e6e6e6; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;/td&gt;&lt;td class='diff-marker'&gt;&amp;#160;&lt;/td&gt;&lt;td style=&quot;background-color: #f9f9f9; color: #333333; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #e6e6e6; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;/td&gt;&lt;/tr&gt;
&lt;tr&gt;&lt;td class='diff-marker'&gt;&amp;#160;&lt;/td&gt;&lt;td style=&quot;background-color: #f9f9f9; color: #333333; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #e6e6e6; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;/td&gt;&lt;td class='diff-marker'&gt;&amp;#160;&lt;/td&gt;&lt;td style=&quot;background-color: #f9f9f9; color: #333333; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #e6e6e6; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;/td&gt;&lt;/tr&gt;
&lt;tr&gt;&lt;td colspan=&quot;2&quot; class=&quot;diff-lineno&quot;&gt;Line 811:&lt;/td&gt;
&lt;td colspan=&quot;2&quot; class=&quot;diff-lineno&quot;&gt;Line 810:&lt;/td&gt;&lt;/tr&gt;
&lt;tr&gt;&lt;td class='diff-marker'&gt;&amp;#160;&lt;/td&gt;&lt;td style=&quot;background-color: #f9f9f9; color: #333333; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #e6e6e6; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;div&gt;|-&lt;/div&gt;&lt;/td&gt;&lt;td class='diff-marker'&gt;&amp;#160;&lt;/td&gt;&lt;td style=&quot;background-color: #f9f9f9; color: #333333; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #e6e6e6; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;div&gt;|-&lt;/div&gt;&lt;/td&gt;&lt;/tr&gt;
&lt;tr&gt;&lt;td class='diff-marker'&gt;&amp;#160;&lt;/td&gt;&lt;td style=&quot;background-color: #f9f9f9; color: #333333; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #e6e6e6; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;div&gt;|| '''Slide Number 13&lt;/div&gt;&lt;/td&gt;&lt;td class='diff-marker'&gt;&amp;#160;&lt;/td&gt;&lt;td style=&quot;background-color: #f9f9f9; color: #333333; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #e6e6e6; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;div&gt;|| '''Slide Number 13&lt;/div&gt;&lt;/td&gt;&lt;/tr&gt;
&lt;tr&gt;&lt;td class='diff-marker'&gt;−&lt;/td&gt;&lt;td style=&quot;color:black; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #ffe49c; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;div&gt;'''&lt;del class=&quot;diffchange diffchange-inline&quot;&gt;Lab Migration &lt;/del&gt;Project'''&lt;/div&gt;&lt;/td&gt;&lt;td class='diff-marker'&gt;+&lt;/td&gt;&lt;td style=&quot;color:black; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #a3d3ff; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;div&gt;'''&lt;ins class=&quot;diffchange diffchange-inline&quot;&gt;TextBook Companion &lt;/ins&gt;Project'''&lt;/div&gt;&lt;/td&gt;&lt;/tr&gt;
&lt;tr&gt;&lt;td class='diff-marker'&gt;−&lt;/td&gt;&lt;td style=&quot;color:black; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #ffe49c; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;div&gt;|| The '''FOSSEE '''team &lt;del class=&quot;diffchange diffchange-inline&quot;&gt;helps migrate commercial simulator labs to '''DWSIM&lt;/del&gt;.&lt;del class=&quot;diffchange diffchange-inline&quot;&gt;'''&lt;/del&gt;&lt;/div&gt;&lt;/td&gt;&lt;td class='diff-marker'&gt;+&lt;/td&gt;&lt;td style=&quot;color:black; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #a3d3ff; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;div&gt;|| The '''FOSSEE '''team &lt;ins class=&quot;diffchange diffchange-inline&quot;&gt;coordinates coding of solved examples of popular books&lt;/ins&gt;.&lt;/div&gt;&lt;/td&gt;&lt;/tr&gt;
&lt;tr&gt;&lt;td class='diff-marker'&gt;&amp;#160;&lt;/td&gt;&lt;td style=&quot;background-color: #f9f9f9; color: #333333; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #e6e6e6; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;/td&gt;&lt;td class='diff-marker'&gt;&amp;#160;&lt;/td&gt;&lt;td style=&quot;background-color: #f9f9f9; color: #333333; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #e6e6e6; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;/td&gt;&lt;/tr&gt;
&lt;tr&gt;&lt;td class='diff-marker'&gt;&amp;#160;&lt;/td&gt;&lt;td style=&quot;background-color: #f9f9f9; color: #333333; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #e6e6e6; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;/td&gt;&lt;td class='diff-marker'&gt;&amp;#160;&lt;/td&gt;&lt;td style=&quot;background-color: #f9f9f9; color: #333333; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #e6e6e6; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;/td&gt;&lt;/tr&gt;
&lt;tr&gt;&lt;td class='diff-marker'&gt;−&lt;/td&gt;&lt;td style=&quot;color:black; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #ffe49c; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;div&gt;We give honorarium and certificates.&lt;/div&gt;&lt;/td&gt;&lt;td class='diff-marker'&gt;+&lt;/td&gt;&lt;td style=&quot;color:black; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #a3d3ff; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;div&gt;We give honorarium and certificates .&lt;/div&gt;&lt;/td&gt;&lt;/tr&gt;
&lt;tr&gt;&lt;td class='diff-marker'&gt;&amp;#160;&lt;/td&gt;&lt;td style=&quot;background-color: #f9f9f9; color: #333333; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #e6e6e6; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;/td&gt;&lt;td class='diff-marker'&gt;&amp;#160;&lt;/td&gt;&lt;td style=&quot;background-color: #f9f9f9; color: #333333; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #e6e6e6; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;/td&gt;&lt;/tr&gt;
&lt;tr&gt;&lt;td class='diff-marker'&gt;&amp;#160;&lt;/td&gt;&lt;td style=&quot;background-color: #f9f9f9; color: #333333; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #e6e6e6; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;/td&gt;&lt;td class='diff-marker'&gt;&amp;#160;&lt;/td&gt;&lt;td style=&quot;background-color: #f9f9f9; color: #333333; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #e6e6e6; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;/td&gt;&lt;/tr&gt;
&lt;tr&gt;&lt;td class='diff-marker'&gt;−&lt;/td&gt;&lt;td style=&quot;color:black; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #ffe49c; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;div&gt;For more details, please visit this site&lt;/div&gt;&lt;/td&gt;&lt;td class='diff-marker'&gt;+&lt;/td&gt;&lt;td style=&quot;color:black; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #a3d3ff; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;div&gt;For more details, please visit this site&lt;ins class=&quot;diffchange diffchange-inline&quot;&gt;.&lt;/ins&gt;&lt;/div&gt;&lt;/td&gt;&lt;/tr&gt;
&lt;tr&gt;&lt;td class='diff-marker'&gt;&amp;#160;&lt;/td&gt;&lt;td style=&quot;background-color: #f9f9f9; color: #333333; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #e6e6e6; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;/td&gt;&lt;td class='diff-marker'&gt;&amp;#160;&lt;/td&gt;&lt;td style=&quot;background-color: #f9f9f9; color: #333333; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #e6e6e6; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;/td&gt;&lt;/tr&gt;
&lt;tr&gt;&lt;td class='diff-marker'&gt;&amp;#160;&lt;/td&gt;&lt;td style=&quot;background-color: #f9f9f9; color: #333333; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #e6e6e6; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;div&gt;|-&lt;/div&gt;&lt;/td&gt;&lt;td class='diff-marker'&gt;&amp;#160;&lt;/td&gt;&lt;td style=&quot;background-color: #f9f9f9; color: #333333; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #e6e6e6; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;div&gt;|-&lt;/div&gt;&lt;/td&gt;&lt;/tr&gt;
&lt;tr&gt;&lt;td class='diff-marker'&gt;&amp;#160;&lt;/td&gt;&lt;td style=&quot;background-color: #f9f9f9; color: #333333; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #e6e6e6; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;div&gt;|| '''Slide Number 14&lt;/div&gt;&lt;/td&gt;&lt;td class='diff-marker'&gt;&amp;#160;&lt;/td&gt;&lt;td style=&quot;background-color: #f9f9f9; color: #333333; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #e6e6e6; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;div&gt;|| '''Slide Number 14&lt;/div&gt;&lt;/td&gt;&lt;/tr&gt;
&lt;tr&gt;&lt;td class='diff-marker'&gt;−&lt;/td&gt;&lt;td style=&quot;color:black; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #ffe49c; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;div&gt;'''&lt;del class=&quot;diffchange diffchange-inline&quot;&gt;TextBook Companion &lt;/del&gt;Project'''&lt;/div&gt;&lt;/td&gt;&lt;td class='diff-marker'&gt;+&lt;/td&gt;&lt;td style=&quot;color:black; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #a3d3ff; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;div&gt;'''&lt;ins class=&quot;diffchange diffchange-inline&quot;&gt;Lab Migration &lt;/ins&gt;Project'''&lt;/div&gt;&lt;/td&gt;&lt;/tr&gt;
&lt;tr&gt;&lt;td class='diff-marker'&gt;−&lt;/td&gt;&lt;td style=&quot;color:black; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #ffe49c; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;div&gt;|| The '''FOSSEE '''team &lt;del class=&quot;diffchange diffchange-inline&quot;&gt;coordinates coding of solved examples of popular books&lt;/del&gt;.&lt;/div&gt;&lt;/td&gt;&lt;td class='diff-marker'&gt;+&lt;/td&gt;&lt;td style=&quot;color:black; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #a3d3ff; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;div&gt;|| The '''FOSSEE '''team &lt;ins class=&quot;diffchange diffchange-inline&quot;&gt;helps migrate commercial simulator labs to '''DWSIM&lt;/ins&gt;.&lt;ins class=&quot;diffchange diffchange-inline&quot;&gt;'''&lt;/ins&gt;&lt;/div&gt;&lt;/td&gt;&lt;/tr&gt;
&lt;tr&gt;&lt;td class='diff-marker'&gt;&amp;#160;&lt;/td&gt;&lt;td style=&quot;background-color: #f9f9f9; color: #333333; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #e6e6e6; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;/td&gt;&lt;td class='diff-marker'&gt;&amp;#160;&lt;/td&gt;&lt;td style=&quot;background-color: #f9f9f9; color: #333333; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #e6e6e6; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;/td&gt;&lt;/tr&gt;
&lt;tr&gt;&lt;td class='diff-marker'&gt;&amp;#160;&lt;/td&gt;&lt;td style=&quot;background-color: #f9f9f9; color: #333333; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #e6e6e6; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;/td&gt;&lt;td class='diff-marker'&gt;&amp;#160;&lt;/td&gt;&lt;td style=&quot;background-color: #f9f9f9; color: #333333; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #e6e6e6; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;/td&gt;&lt;/tr&gt;
&lt;tr&gt;&lt;td class='diff-marker'&gt;−&lt;/td&gt;&lt;td style=&quot;color:black; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #ffe49c; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;div&gt;We give honorarium and certificates .&lt;/div&gt;&lt;/td&gt;&lt;td class='diff-marker'&gt;+&lt;/td&gt;&lt;td style=&quot;color:black; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #a3d3ff; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;div&gt;We give honorarium and certificates.&lt;/div&gt;&lt;/td&gt;&lt;/tr&gt;
&lt;tr&gt;&lt;td class='diff-marker'&gt;&amp;#160;&lt;/td&gt;&lt;td style=&quot;background-color: #f9f9f9; color: #333333; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #e6e6e6; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;/td&gt;&lt;td class='diff-marker'&gt;&amp;#160;&lt;/td&gt;&lt;td style=&quot;background-color: #f9f9f9; color: #333333; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #e6e6e6; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;/td&gt;&lt;/tr&gt;
&lt;tr&gt;&lt;td class='diff-marker'&gt;&amp;#160;&lt;/td&gt;&lt;td style=&quot;background-color: #f9f9f9; color: #333333; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #e6e6e6; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;/td&gt;&lt;td class='diff-marker'&gt;&amp;#160;&lt;/td&gt;&lt;td style=&quot;background-color: #f9f9f9; color: #333333; font-size: 88%; border-style: solid; border-width: 1px 1px 1px 4px; border-radius: 0.33em; border-color: #e6e6e6; vertical-align: top; white-space: pre-wrap;&quot;&gt;&lt;/td&gt;&lt;/tr&gt;
&lt;/table&gt;</summary>
		<author><name>Kaushik Datta</name></author>	</entry>

	<entry>
		<id>https://script.spoken-tutorial.org/index.php?title=DWSIM/C2/Heat-Exchanger/English&amp;diff=38054&amp;oldid=prev</id>
		<title>Kaushik Datta: Created page with &quot; {| border=1 ||'''Visual Cue''' ||'''Narration'''  |- || '''Slide Number 1 '''Title Slide''' || Welcome to this tutorial on Simulating a '''Heat Exchanger '''in '''DWSIM'''....&quot;</title>
		<link rel="alternate" type="text/html" href="https://script.spoken-tutorial.org/index.php?title=DWSIM/C2/Heat-Exchanger/English&amp;diff=38054&amp;oldid=prev"/>
				<updated>2017-08-07T11:14:50Z</updated>
		
		<summary type="html">&lt;p&gt;Created page with &amp;quot; {| border=1 ||&amp;#039;&amp;#039;&amp;#039;Visual Cue&amp;#039;&amp;#039;&amp;#039; ||&amp;#039;&amp;#039;&amp;#039;Narration&amp;#039;&amp;#039;&amp;#039;  |- || &amp;#039;&amp;#039;&amp;#039;Slide Number 1 &amp;#039;&amp;#039;&amp;#039;Title Slide&amp;#039;&amp;#039;&amp;#039; || Welcome to this tutorial on Simulating a &amp;#039;&amp;#039;&amp;#039;Heat Exchanger &amp;#039;&amp;#039;&amp;#039;in &amp;#039;&amp;#039;&amp;#039;DWSIM&amp;#039;&amp;#039;&amp;#039;....&amp;quot;&lt;/p&gt;
&lt;p&gt;&lt;b&gt;New page&lt;/b&gt;&lt;/p&gt;&lt;div&gt;&lt;br /&gt;
{| border=1&lt;br /&gt;
||'''Visual Cue'''&lt;br /&gt;
||'''Narration'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| '''Slide Number 1&lt;br /&gt;
'''Title Slide'''&lt;br /&gt;
|| Welcome to this tutorial on Simulating a '''Heat Exchanger '''in '''DWSIM'''.&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| '''Slide Number 2&lt;br /&gt;
'''Learning Objective'''&lt;br /&gt;
|| In this tutorial, we will learn to:&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
* Simulate a''' Heat Exchanger'''&lt;br /&gt;
&lt;br /&gt;
* Calculate the '''Outlet stream temperatures'''&lt;br /&gt;
&lt;br /&gt;
* Calculate '''Thermal Efficiency '''and''' LMTD'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| '''Slide Number 3&lt;br /&gt;
'''System Requirements'''&lt;br /&gt;
|| To record this tutorial, I am using&lt;br /&gt;
&lt;br /&gt;
* '''DWSIM 4.3 '''and&lt;br /&gt;
&lt;br /&gt;
* '''Windows 7'''&lt;br /&gt;
&lt;br /&gt;
The process demonstrated in this tutorial is identical in other OS also, such as-&lt;br /&gt;
&lt;br /&gt;
*  '''Linux''', &lt;br /&gt;
&lt;br /&gt;
*  '''Mac OS X '''or &lt;br /&gt;
&lt;br /&gt;
*  '''FOSSEE OS '''on '''ARM'''.&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| '''Slide Number 4'''&lt;br /&gt;
&lt;br /&gt;
'''Pre-requisites '''&lt;br /&gt;
|| To practice this tutorial, you should know how to&lt;br /&gt;
&lt;br /&gt;
*  add components to a '''flowsheet'''&lt;br /&gt;
*  select '''thermodynamic '''packages and&lt;br /&gt;
*  add '''material '''stream''' '''and specify their properties.&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| '''Slide Number 5'''&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
'''Prerequisite Tutorials and Files'''&lt;br /&gt;
|| The prerequisite tutorials are mentioned on our website, '''spoken-tutorial.org'''&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
You can access these tutorials and all the associated files from this site.&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| '''Slide Number 6'''&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
'''Compounds '''and''' Inlet Condition'''&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
Cold Stream: Water&lt;br /&gt;
&lt;br /&gt;
Hot Stream: Methanol&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
'''Cold Inlet Stream:'''&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
Mass Flow: 15000 kg/h&lt;br /&gt;
&lt;br /&gt;
Mole Fraction(CH&amp;lt;sub&amp;gt;3&amp;lt;/sub&amp;gt;OH): 0&lt;br /&gt;
&lt;br /&gt;
Mole Fraction(H&amp;lt;sub&amp;gt;2&amp;lt;/sub&amp;gt;O): 1&lt;br /&gt;
&lt;br /&gt;
Temperature: 10 degree C &lt;br /&gt;
&lt;br /&gt;
Pressure: 1 bar&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
'''Hot Inlet Stream:'''&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
Mass Flow: 25000kg/h&lt;br /&gt;
&lt;br /&gt;
Mole Fraction(CH&amp;lt;sub&amp;gt;3&amp;lt;/sub&amp;gt;OH): 1&lt;br /&gt;
&lt;br /&gt;
Mole Fraction(H&amp;lt;sub&amp;gt;2&amp;lt;/sub&amp;gt;O): 0&lt;br /&gt;
&lt;br /&gt;
Temperature: 80 degree C &lt;br /&gt;
&lt;br /&gt;
Pressure: 5 bar&lt;br /&gt;
|| We will develop a '''flowsheet '''to determine the '''Outlet stream temperatures.'''&lt;br /&gt;
&lt;br /&gt;
Here we give '''Compounds '''and''' Inlet stream conditions.'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| '''Slide Number 6'''&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
'''Heat Exchanger Properties'''&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
Flow type: Counter-Current&lt;br /&gt;
&lt;br /&gt;
&amp;lt;nowiki&amp;gt;Overall Heat Transfer Coefficient: 450 W/[m&amp;lt;/nowiki&amp;gt;&amp;lt;sup&amp;gt;2&amp;lt;/sup&amp;gt;.K]&lt;br /&gt;
&lt;br /&gt;
Heat Exchanger Area: 250 m&amp;lt;sup&amp;gt;2&amp;lt;/sup&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Cold Fluid Pressure Drop: 0.002 bar&lt;br /&gt;
&lt;br /&gt;
Hot Fluid Pressure Drop: 0.025 bar&lt;br /&gt;
&lt;br /&gt;
Property Package: Raoult’s Law&lt;br /&gt;
|| Here we give '''Heat Exchanger''' properties and '''Property package'''.&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| &lt;br /&gt;
|| I have already opened '''DWSIM''' on my machine. &lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| File &amp;gt;&amp;gt;'''New Steady-state Simulation '''&lt;br /&gt;
|| Go to '''File '''menu and select '''New Steady-state Simulation.'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| Point to '''Simulation Configuration Wizard '''window&lt;br /&gt;
|| '''Simulation Configuration Wizard '''window appears.&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| Click on '''Next'''.&lt;br /&gt;
|| At the bottom, click on '''Next '''button.&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| Type '''Methanol '''in the '''Search '''tab&lt;br /&gt;
|| Now, in the '''Compounds Search '''tab, type '''Methanol.'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| '''ChemSep '''database &amp;gt;&amp;gt;'''Methanol'''&lt;br /&gt;
|| Select '''Methanol '''from '''ChemSep '''database.&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| '''Type Water '''in the '''Search '''tab&lt;br /&gt;
|| Similarly, add '''Water'''.&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| Click on '''Next.'''&lt;br /&gt;
|| At the bottom, click on '''Next '''button.&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| Point to''' Property Packages'''&lt;br /&gt;
|| Now comes '''Property Packages.'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| '''Property Packages'''&amp;gt;&amp;gt; '''Available Property Package'''&lt;br /&gt;
&lt;br /&gt;
Double click on '''Raoult’s Law'''&lt;br /&gt;
|| From '''Available Property Package '''list, double-click on '''Raoult’s Law.'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| Click on''' Next.'''&lt;br /&gt;
|| Then click on '''Next '''button'''.'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| Point to''' Flash Algorithm'''&lt;br /&gt;
|| We are moved to a new window named '''Flash Algorithm'''.&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| '''Default Flash Algorithm '''&amp;gt;&amp;gt;'''Nested Loops (VLE)'''&lt;br /&gt;
|| From '''Default Flash Algorithm '''select '''Nested Loops(VLE)'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| Click '''Next'''&lt;br /&gt;
|| Click on '''Next '''button'''.'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| Point to''' System of Units'''&lt;br /&gt;
|| Next option is '''System of Units.'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| '''System of Units &amp;gt;&amp;gt; C5'''&lt;br /&gt;
|| Under '''System of Units''', select '''C5'''.&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| Click on''' Finish'''&lt;br /&gt;
|| At the bottom, click on '''Finish '''button'''.'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| &lt;br /&gt;
|| Let us maximize the simulation window for better visibility.&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| &lt;br /&gt;
|| Now let’s insert two material streams that enter the '''Heat Exchanger'''.&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| Point to '''Flowsheet Objects.'''&lt;br /&gt;
|| On the right hand side of the main simulation window, go to '''Flowsheet Objects.'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| In the''' Filter List '''tab, type '''Material Stream'''&lt;br /&gt;
|| In the '''Filter List '''tab, type '''Material Stream.'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| Click and drag '''Material Stream '''to the flowsheet&lt;br /&gt;
|| From the displayed list, drag and drop a '''Material Stream '''to the '''Flowsheet'''.&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| Click on '''MSTR-000'''&lt;br /&gt;
|| Click on '''Material Stream '''“'''MSTR-000” '''to view its properties.&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| Type '''Water In'''&lt;br /&gt;
|| Let’s change the name of this '''stream '''to '''Water In.'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| &lt;br /&gt;
|| Now we will specify the '''Water In stream '''properties.&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| '''Input Data&amp;gt;&amp;gt;Flash Spec&amp;gt;&amp;gt;Temperature and Pressure(TP)'''&lt;br /&gt;
|| Go to '''Input Data.'''&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
Select '''Flash Spec '''as '''Temperature and Pressure (TP), '''if not already selected.&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
By default, '''Temperature and Pressure '''are already selected as '''Flash Spec.'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| '''Input Data &amp;gt;&amp;gt;Temperature &amp;gt;&amp;gt;10C'''&lt;br /&gt;
&lt;br /&gt;
Press '''Enter'''&lt;br /&gt;
|| Change '''Temperature '''to '''10 degC '''and press '''Enter.'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| '''Input Data &amp;gt;&amp;gt;Pressure &amp;gt;&amp;gt;1bar'''&lt;br /&gt;
&lt;br /&gt;
Press '''Enter'''&lt;br /&gt;
|| Change '''Pressure '''to '''1 bar '''and press '''Enter'''.&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| '''Input Data &amp;gt;&amp;gt;Mass Flow &amp;gt;&amp;gt;15000kg/h'''&lt;br /&gt;
&lt;br /&gt;
Press '''Enter'''&lt;br /&gt;
|| Change '''Mass Flow '''to '''15000 kg/h '''and press '''Enter'''.&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| &lt;br /&gt;
|| Now let us specify the '''feed stream compositions'''.&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| '''Composition &amp;gt;&amp;gt;Basis &amp;gt;&amp;gt;Mole Fractions'''&lt;br /&gt;
|| Under '''Composition''', choose the '''Basis '''as '''Mole Fractions, '''if not already selected'''.'''&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
By default, '''Mole Fractions '''is selected as '''Basis.'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| '''Methanol: 0'''&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
|| Now for '''Methanol''', enter the '''Amount '''as '''0 '''and press '''Enter.'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| '''Water: 1'''&lt;br /&gt;
|| Similarly, for '''Water''', enter it as '''1 '''and press '''Enter.'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| Click '''Accept Changes'''&lt;br /&gt;
|| On the right, click on this green tick to '''Accept Changes.'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| &lt;br /&gt;
|| Now drag and drop another '''Material Stream '''to the flowsheet.&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| Click on '''MSTR-000'''&lt;br /&gt;
|| Click on '''Material Stream '''“'''MSTR-001” '''to view its properties.&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| Type '''Methanol In'''&lt;br /&gt;
|| Let’s change the name of this '''stream '''to '''Methanol In.'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| &lt;br /&gt;
|| Now we will specify the '''Methanol In '''stream properties.&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| '''Input Data&amp;gt;&amp;gt;Flash Spec&amp;gt;&amp;gt;Temperature and Pressure(TP)'''&lt;br /&gt;
|| Go to '''Input Data.'''&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
'''S'''elect '''Flash Spec '''as '''Temperature and Pressure (TP).'''&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
By default, '''Temperature and Pressure '''are again already selected as '''Flash Spec.'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| '''Input Data &amp;gt;&amp;gt;Temperature &amp;gt;&amp;gt; 80 degC'''&lt;br /&gt;
&lt;br /&gt;
Press '''Enter'''&lt;br /&gt;
|| Change '''Temperature '''to '''80 degC '''and press '''Enter.'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| '''Input Data &amp;gt;&amp;gt;Pressure &amp;gt;&amp;gt;5 bar'''&lt;br /&gt;
&lt;br /&gt;
Press '''Enter'''&lt;br /&gt;
|| Change '''Pressure '''to '''5 bar '''and press '''Enter'''.&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| '''Input Data &amp;gt;&amp;gt;Mass Flow &amp;gt;&amp;gt;25000 kg/h'''&lt;br /&gt;
&lt;br /&gt;
Press '''Enter'''&lt;br /&gt;
|| Change '''Mass Flow '''to '''25000 kg/h '''and press '''Enter'''.&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| &lt;br /&gt;
|| Now let us specify the '''Methanol In stream compositions'''.&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| '''Composition &amp;gt;&amp;gt;Basis &amp;gt;&amp;gt;Mole Fractions'''&lt;br /&gt;
|| Under '''Composition''', choose the '''Basis '''as '''Mole Fractions, '''if not already selected'''.'''&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
By default, '''Mole Fractions '''is selected as '''Basis.'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| '''Methanol: 1'''&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
|| Now for '''Methanol''', enter the '''Amount '''as '''1 '''and press '''Enter.'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| '''Water: 0'''&lt;br /&gt;
|| Similarly, for '''Water''', enter it as '''0 '''and press '''Enter.'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| Click '''Accept Changes'''&lt;br /&gt;
|| On the right, click on this green tick to '''Accept Changes.'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| &lt;br /&gt;
|| Now let’s insert two more material streams that exit the '''Heat Exchanger'''.&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| Click and Drag '''Material Stream '''to the flowsheet&lt;br /&gt;
|| To do that, let us drag one '''Material Stream.'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| &lt;br /&gt;
|| Let us now arrange it.&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| &lt;br /&gt;
|| Leave that stream as unspecified.&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| Type '''Water Out'''&lt;br /&gt;
|| We will change the name of this '''stream '''to '''Water Out.'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| Click and drag''' Material Stream '''to the flowsheet&lt;br /&gt;
|| Next, we will insert another '''Material Stream.'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| &lt;br /&gt;
|| Let us once again arrange it.&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| &lt;br /&gt;
|| Leave that stream as unspecified.&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| Type''' Methanol Out'''&lt;br /&gt;
|| And name this '''stream '''as '''Methanol Out.'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| &lt;br /&gt;
|| Now let us insert a '''Heat Exchanger '''into the '''flowsheet'''.&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| Go to '''Flowsheet Objects'''&lt;br /&gt;
|| Go to '''Flowsheet Objects'''.&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| In the '''Filter list '''tab, type '''Heat Exchanger.'''&lt;br /&gt;
|| In the '''Filter list '''tab, type '''Heat Exchanger.'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| Click and drag '''Heat Exchanger '''to the flowsheet&lt;br /&gt;
|| Click on the '''Heat Exchanger '''displayed.&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
Drag and drop it to the '''flowsheet.'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| &lt;br /&gt;
|| Let us now arrange it as required for better visibility.&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| Click '''Heat Exchanger'''&lt;br /&gt;
|| We are now ready to specify the '''Heat Exchanger.'''&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
Let's click on it.&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| &lt;br /&gt;
|| On the left, we can see a tab called''' Property Editor Window.'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| Go to''' Connections'''&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
Click on drop down arrow against''' Inlet Stream 1'''&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
Select '''Methanol In.'''&lt;br /&gt;
|| Under '''Connections, '''click on the drop-down against '''Inlet Stream 1.'''&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
And select '''Methanol In.'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| Click on drop down arrow against''' Outlet Stream 1'''&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
Select '''Methanol Out.'''&lt;br /&gt;
|| Next, click on the drop-down against '''Outlet Stream 1.'''&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
And select '''Methanol Out.'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| Click on the drop down against''' Inlet Stream 2'''&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
Select '''Water In.'''&lt;br /&gt;
|| Then click on the drop-down against '''Inlet Stream 2. '''&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
And select '''Water In.'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| Click on the drop down against''' Outlet Stream 2'''&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
Select '''Water Out.'''&lt;br /&gt;
|| Then click on the drop-down against '''Outlet Stream 2. '''&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
And select '''Water Out.'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| Hover mouse at''' Calculation Parameters'''&lt;br /&gt;
|| Now go to the next section- '''Calculation Parameters.'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| &lt;br /&gt;
|| Here, the first option is '''Calculation Type.'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| Click drop down against '''Calculation Type'''&lt;br /&gt;
|| Click on the drop-down against '''Calculation Type.'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| Select '''Outlet Temperatures (UA) '''&lt;br /&gt;
|| Select '''Outlet Temperatures (UA) '''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| Click drop down against '''Flow Direction.'''&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
Select '''Counter Current'''&lt;br /&gt;
|| Next, click on the drop-down against '''Flow Direction'''&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
Select '''Counter Current.'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| '''Cold Fluid Pressure Drop'''&amp;gt;&amp;gt;'''0.002 bar'''&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
Press '''Enter'''&lt;br /&gt;
|| Then click on the field against '''Cold Fluid Pressure Drop '''and enter '''0.002 bar.'''&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
Then press '''Enter.'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| '''Hot Fluid Pressure Drop&amp;gt;&amp;gt;0.025bar'''&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
|| Click on the field against '''Hot Fluid Pressure Drop '''and enter it as '''0.025 bar.'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| '''Press Enter'''&lt;br /&gt;
|| Then press '''Enter.'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| '''&amp;lt;nowiki&amp;gt;Overall Heat Transfer Coefficient &amp;gt;&amp;gt;450W/[m&amp;lt;/nowiki&amp;gt;&amp;lt;sup&amp;gt;2&amp;lt;/sup&amp;gt;.K]'''&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
Press '''Enter'''&lt;br /&gt;
|| Click on the field against '''Overall Heat Transfer Coefficient '''and enter it as '''&amp;lt;nowiki&amp;gt;450W/[m&amp;lt;/nowiki&amp;gt;&amp;lt;sup&amp;gt;2&amp;lt;/sup&amp;gt;.K]'''&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
Then press '''Enter.'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| '''Heat Exchanged Area&amp;gt;&amp;gt;250 m&amp;lt;sup&amp;gt;2'''&amp;lt;/sup&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
Press '''Enter'''&lt;br /&gt;
|| Click on the field against '''Heat Exchanged Area '''and enter it as '''250 m&amp;lt;sup&amp;gt;2&amp;lt;/sup&amp;gt;.'''&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
Then press '''Enter.'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| &lt;br /&gt;
|| Now we will run the '''simulation.'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| Click '''Solve Flowsheet'''&lt;br /&gt;
|| So, from the toolbar, click on '''Solve Flowsheet '''button.&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| Click '''Heat Exchanger'''&lt;br /&gt;
|| When the calculations are completed, click on '''Heat Exchanger '''in the '''Flowsheet'''.&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| Hover mouse at''' Results'''&lt;br /&gt;
|| From the '''Property Editor Window '''of '''Heat Exchanger, '''locate '''Results '''section.&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| '''Results &amp;gt;&amp;gt;General'''&lt;br /&gt;
|| Under '''General''' tab, check '''Thermal efficiency;''' it is '''94.5%'''&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
Check '''Log Mean Temperature Difference;''' it is '''10.29 degree C.'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| &lt;br /&gt;
|| Now we will check the '''stream-'''wise temperature results and '''Material balance.'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| '''Insert &amp;gt;&amp;gt;Master Property Table'''&lt;br /&gt;
|| Go to '''Insert '''menu and select '''Master Property Table'''.&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| Double click on''' Master Property Table'''&lt;br /&gt;
|| Double-click on the '''Master Property Table '''to edit it.&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| Point to '''Configure Master Property Table'''&lt;br /&gt;
|| '''Configure Master Property Table '''window opens.&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| Type '''Heat Exchanger – Stream Wise Results'''&lt;br /&gt;
|| Enter '''Name '''as '''Heat Exchanger – Stream Wise Results'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| '''Object Type &amp;gt;&amp;gt;Material Stream'''&lt;br /&gt;
|| Enter '''Object Type '''as '''Material Stream'''.&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
By default, '''Material Stream '''is already selected.&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| &lt;br /&gt;
|| So we will not change it.&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| '''Object &amp;gt;&amp;gt;Methanol Out, Water Out, Methanol In and Water In.'''&lt;br /&gt;
|| Under '''Properties to display''', select '''Object '''as:&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
'''Methanol Out, Water Out, Methanol In '''and '''Water In'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| '''Configure Master Property Table&amp;gt;&amp;gt;Property'''&lt;br /&gt;
|| Under '''Property''', scroll down to see all the parameters.&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
Now select the properties as:&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
'''Temperature'''&lt;br /&gt;
&lt;br /&gt;
'''Pressure'''&lt;br /&gt;
&lt;br /&gt;
'''Mass Flow'''&lt;br /&gt;
&lt;br /&gt;
'''Molar Flow'''&lt;br /&gt;
&lt;br /&gt;
'''Molar Fraction(Mixture) / Methanol'''&lt;br /&gt;
&lt;br /&gt;
'''Molar Fraction(Mixture) / Water'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| Close this window.&lt;br /&gt;
|| Close this window.&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| &lt;br /&gt;
|| Move the '''Master Property Table '''for better visibility.&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
Here we can see the corresponding results for '''Inlet '''and '''Outlet streams.'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| &lt;br /&gt;
|| Now we will check the properties of '''Heat Exchanger.'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| '''Insert &amp;gt;&amp;gt;Master Property Table'''&lt;br /&gt;
|| Go to '''Insert '''menu and select '''Master Property Table'''.&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| Double click on''' Master Property Table'''&lt;br /&gt;
|| Double-click on the '''Master Property Table.'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| Point to '''Configure Master Property Table'''&lt;br /&gt;
|| '''Configure Master Property Table '''window opens.&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| Type '''Heat Exchanger – Results'''&lt;br /&gt;
|| Enter '''Name '''as '''Heat Exchanger – Results.'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| '''Object Type &amp;gt;&amp;gt;Material Stream'''&lt;br /&gt;
|| Enter '''Object Type '''as '''Heat Exchanger'''.&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| '''Object &amp;gt;&amp;gt;HE-004.'''&lt;br /&gt;
|| Under '''Properties to display''', select '''Object '''as '''HE-004'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| '''Configure Master Property Table&amp;gt;&amp;gt;Property'''&lt;br /&gt;
|| Under '''Property''', scroll down to see all the parameters.&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
Now select the properties as:&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
'''Global Heat Transfer Coefficient (U)'''&lt;br /&gt;
&lt;br /&gt;
'''Heat Exchange Area (A)'''&lt;br /&gt;
&lt;br /&gt;
'''Heat Load'''&lt;br /&gt;
&lt;br /&gt;
'''Cold fluid outlet temperature'''&lt;br /&gt;
&lt;br /&gt;
'''Hot fluid outlet temperature'''&lt;br /&gt;
&lt;br /&gt;
'''Logarithmic mean temperature difference LMTD'''&lt;br /&gt;
&lt;br /&gt;
'''Thermal Efficiency'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| Close this window.&lt;br /&gt;
|| Close this window.&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| &lt;br /&gt;
|| Move the '''Master Property Table '''for better visibility.&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
Here we can see the corresponding results for '''Heat Exchanger.'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| &lt;br /&gt;
|| Let's summarize.&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| '''Slide Number 7'''&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
'''Summary'''&lt;br /&gt;
|| In this tutorial, we have learnt to&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
Simulate a''' Heat Exchanger'''&lt;br /&gt;
Calculate the''' Outlet stream temperatures '''&lt;br /&gt;
Calculate''' Thermal Efficiency '''and''' LMTD'''&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| '''Slide Number 8'''&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
'''Assignment'''&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
'''Compounds and Inlet Condition'''&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
'''Cold Stream:''' Toluene&lt;br /&gt;
&lt;br /&gt;
'''Hot Stream:''' Acetone&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
'''Cold Inlet Stream:'''&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
Mass Flow: 30000 lb/hr&lt;br /&gt;
&lt;br /&gt;
Mole Fraction(C&amp;lt;sub&amp;gt;3&amp;lt;/sub&amp;gt;H&amp;lt;sub&amp;gt;6&amp;lt;/sub&amp;gt;O): 0&lt;br /&gt;
&lt;br /&gt;
Mole Fraction(C&amp;lt;sub&amp;gt;6&amp;lt;/sub&amp;gt;H&amp;lt;sub&amp;gt;5&amp;lt;/sub&amp;gt;-CH&amp;lt;sub&amp;gt;3&amp;lt;/sub&amp;gt;): 1&lt;br /&gt;
&lt;br /&gt;
Temperature: 100 degree F&lt;br /&gt;
&lt;br /&gt;
Pressure: 1 bar&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
'''Hot Inlet Stream:'''&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
Mass Flow: 15000 lb/hr&lt;br /&gt;
&lt;br /&gt;
Mole Fraction(C&amp;lt;sub&amp;gt;3&amp;lt;/sub&amp;gt;H&amp;lt;sub&amp;gt;6&amp;lt;/sub&amp;gt;O): 1&lt;br /&gt;
&lt;br /&gt;
Mole Fraction(C&amp;lt;sub&amp;gt;6&amp;lt;/sub&amp;gt;H&amp;lt;sub&amp;gt;5&amp;lt;/sub&amp;gt;-CH&amp;lt;sub&amp;gt;3&amp;lt;/sub&amp;gt;): 0&lt;br /&gt;
&lt;br /&gt;
Temperature: 200 degree F &lt;br /&gt;
&lt;br /&gt;
Pressure: 5 bar&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
'''Heat Exchanger Properties'''&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
Flow type: Counter-Current&lt;br /&gt;
&lt;br /&gt;
&amp;lt;nowiki&amp;gt;Overall Heat Transfer Coefficient: 270 W/[m&amp;lt;/nowiki&amp;gt;&amp;lt;sup&amp;gt;2&amp;lt;/sup&amp;gt;.K]&lt;br /&gt;
&lt;br /&gt;
Heat Exchanger Area: 75 m&amp;lt;sup&amp;gt;2&amp;lt;/sup&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Cold Fluid Pressure Drop: 0.0035 bar&lt;br /&gt;
&lt;br /&gt;
Hot Fluid Pressure Drop: 0.0025 bar&lt;br /&gt;
&lt;br /&gt;
Property Package: Raoult’s Law&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
|| As an assignment,&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
Repeat this simulation with different '''Compounds, feed conditions '''and '''Thermodynamics'''.&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| '''Slide Number 9'''&lt;br /&gt;
&lt;br /&gt;
'''About the Spoken Tutorial Project'''&lt;br /&gt;
|| Watch the video available at following link.&lt;br /&gt;
&lt;br /&gt;
'''http://spoken-tutorial.org/ '''&lt;br /&gt;
&lt;br /&gt;
It summarizes the Spoken Tutorial project.&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| '''Slide Number 10'''&lt;br /&gt;
&lt;br /&gt;
'''Spoken Tutorial Workshops'''&lt;br /&gt;
| style=&amp;quot;background-color:#ffffff;border:0.5pt solid #000001;padding-top:0in;padding-bottom:0in;padding-left:0.0736in;padding-right:0.0736in;&amp;quot;| The Spoken Tutorial Project Team&lt;br /&gt;
&lt;br /&gt;
Conducts workshops and&lt;br /&gt;
Gives certificates&lt;br /&gt;
For more details, please write to contact@spoken-tutorial.org&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| '''Slide Number 11'''&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
'''Forum Slide'''&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
Do you have questions in this '''Spoken Tutorial?'''&lt;br /&gt;
&lt;br /&gt;
Please visit this site &lt;br /&gt;
&lt;br /&gt;
Choose the minute and second where you have the question. &lt;br /&gt;
&lt;br /&gt;
Explain your question briefly. &lt;br /&gt;
&lt;br /&gt;
Someone from the FOSSEE team will answer them. &lt;br /&gt;
|| Please post your times queries in this forum. &lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| '''Slide Number 12&lt;br /&gt;
'''DWSIM Flowsheeting Project'''&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
|| The '''FOSSEE '''team coordinates conversion of existing flow sheets into '''DWSIM'''.&lt;br /&gt;
&lt;br /&gt;
We give honorarium and certificates.&lt;br /&gt;
&lt;br /&gt;
For more details, please visit this site.&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| '''Slide Number 13&lt;br /&gt;
'''Lab Migration Project'''&lt;br /&gt;
|| The '''FOSSEE '''team helps migrate commercial simulator labs to '''DWSIM.'''&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
We give honorarium and certificates.&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
For more details, please visit this site&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| '''Slide Number 14&lt;br /&gt;
'''TextBook Companion Project'''&lt;br /&gt;
|| The '''FOSSEE '''team coordinates coding of solved examples of popular books.&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
We give honorarium and certificates .&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
For more details, please visit this site.&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| '''Slide Number 15&lt;br /&gt;
'''Acknowledgements'''&lt;br /&gt;
|| '''Spoken Tutorial '''and '''FOSSEE '''projects are funded by '''NMEICT, MHRD''', Government of India.&lt;br /&gt;
&lt;br /&gt;
|-&lt;br /&gt;
|| '''Slide Number 16&lt;br /&gt;
'''Thanks'''&lt;br /&gt;
|| This tutorial is contributed by Kaushik Datta and Priyam Nayak.&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
Thanks for joining.&lt;br /&gt;
&lt;br /&gt;
|}&lt;/div&gt;</summary>
		<author><name>Kaushik Datta</name></author>	</entry>

	</feed>