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		<title>Pressure Drop In Pipe Lines And Fittings &#124; Part 2</title>
		<link>https://engineeringness.com/pressure-drop-in-pipe-lines-and-fittings-part-2/</link>
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		<dc:creator><![CDATA[Hassan Ahmed]]></dc:creator>
		<pubDate>Thu, 22 Apr 2021 20:25:56 +0000</pubDate>
				<category><![CDATA[Fluid Mechanics]]></category>
		<category><![CDATA[Equivalent Length Method]]></category>
		<category><![CDATA[Pipeline Tutorial]]></category>
		<category><![CDATA[Head Loss]]></category>
		<category><![CDATA[Pressure Drop]]></category>
		<category><![CDATA[Darcy&#039;s Friction Factor]]></category>
		<category><![CDATA[K Values]]></category>
		<category><![CDATA[Head Loss Coefficient]]></category>
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					<description><![CDATA[<p>Pressure Drop Caused By Valves and Fittings In part 1 the tutorial goes over pressure drop in pipelines. Just to recap pressure drop arises due to skin friction and forms friction. Non-separated boundary layers causes skin friction (the roughness of the pipe causing shear within the boundary layer of the fluid) whereas separated boundary layers cause form friction (geometrical characteristics of the piping system are piled up causing localised losses). Simply put, pipe pressure drop is due to skin friction. But in a pipeline with valves and fittings pressure drop is mainly due to form friction. The pipelines may be</p>
<p>The post <a href="https://engineeringness.com/pressure-drop-in-pipe-lines-and-fittings-part-2/" data-wpel-link="internal">Pressure Drop In Pipe Lines And Fittings | Part 2</a> appeared first on <a href="https://engineeringness.com" data-wpel-link="internal">Engineeringness</a>.</p>
]]></description>
										<content:encoded><![CDATA[<h2><u>Pressure Drop Caused By Valves and Fittings</u></h2>
<p>In part 1 the tutorial goes over pressure drop in pipelines. Just to recap pressure drop arises due to skin friction and forms friction. Non-separated boundary layers causes skin friction (the roughness of the pipe causing shear within the boundary layer of the fluid) whereas separated boundary layers cause form friction (geometrical characteristics of the piping system are piled up causing localised losses).</p>
<p>Simply put, pipe pressure drop is due to skin friction. But in a pipeline with valves and fittings pressure drop is mainly due to form friction. The pipelines may be connected to equipment and again pressure drop occur due to the specific piece of equipment. This tutorial is focused on pressure drop in valves and fittings only.</p>
<p>In order to account for pressure drop due to valves and fittings, various methods are used The most common among them is:</p>
<ol>
<li>K values or Head Loss Coefficient.</li>
<li>Equivalent length method.</li>
</ol>
<h2>1. K values or Head Loss Coefficient Method</h2>
<div>
<div class="separator"><a href="http://3.bp.blogspot.com/--TO3mPEDrzo/VVIOAzryo6I/AAAAAAAAA1M/E9choMkq_SY/s1600/K%2Bvalue.jpg" data-wpel-link="external" rel="nofollow external noopener noreferrer"><img decoding="async" class="aligncenter" title="Pressure drop formula by Chemineering" src="https://3.bp.blogspot.com/--TO3mPEDrzo/VVIOAzryo6I/AAAAAAAAA1M/E9choMkq_SY/s200/K%2Bvalue.jpg" alt="Pressure drop formula by Chemineering" width="200" height="126" border="0" /></a></div>
</div>
<div>
<p class="FXNormalChar">Where:</p>
<p class="FXEqnDefinition">Hf = Head Loss</p>
<p class="FXEqnDefinition">K = Head Loss Coefficient</p>
<p class="FXEqnDefinition">V = Average Velocity of fluid</p>
<p class="FXEqnDefinition">g = Acceleration due to gravity</p>
<p><img decoding="async" src="https://latex.codecogs.com/gif.latex?rho" alt="rho" align="absmiddle" /> = Density of fluid</p>
</div>
<div>Earlier K values were static constants but in recent applications (Industrial applications) they are seen to be dynamic and change with pipe diameter.</div>
<div>
<p>Depending upon the type of valves and fittings, various K values are available, which can be seen in the table below:</p>
<div class="separator"><a href="http://4.bp.blogspot.com/-VWVIqgmTnvQ/VVIP4zxu3AI/AAAAAAAAA1Y/KAxmkxX6IlQ/s1600/New%2BDoc_1.jpg" data-wpel-link="external" rel="nofollow external noopener noreferrer"><img fetchpriority="high" decoding="async" class="aligncenter" title="K Values by Chemineering" src="https://4.bp.blogspot.com/-VWVIqgmTnvQ/VVIP4zxu3AI/AAAAAAAAA1Y/KAxmkxX6IlQ/s400/New%2BDoc_1.jpg" alt="K Values by Chemineering" width="400" height="345" border="0" /></a></div>
</div>
<div>
<p>K values that are subject to change, then the pipe diameter can be calculated as follows:</p>
<div class="separator"><a href="http://2.bp.blogspot.com/-zwdzgeQxzmw/VVIRvenSHSI/AAAAAAAAA1k/AVfWOS63Rhw/s1600/P_20150512_185742-001.jpg" data-wpel-link="external" rel="nofollow external noopener noreferrer"><img decoding="async" class="aligncenter" title="3-K formula by Chemineering" src="https://2.bp.blogspot.com/-zwdzgeQxzmw/VVIRvenSHSI/AAAAAAAAA1k/AVfWOS63Rhw/s200/P_20150512_185742-001.jpg" alt="3-K formula by Chemineering" width="200" height="81" border="0" /></a></div>
<div class="separator"></div>
<div class="separator">The Km, Ki, and Kd values corresponding to the type of fittings and valves that are given in the table below.</div>
<div class="separator"></div>
<div class="separator"><a href="http://4.bp.blogspot.com/-Ilzdx2c4EhE/VVISWziXNxI/AAAAAAAAA1s/KiZ2wJoYolU/s1600/New%2BDoc_2.jpg" data-wpel-link="external" rel="nofollow external noopener noreferrer"><img loading="lazy" decoding="async" class="aligncenter" title="3-K constant for loss coefficients by Chemineering" src="https://4.bp.blogspot.com/-Ilzdx2c4EhE/VVISWziXNxI/AAAAAAAAA1s/KiZ2wJoYolU/s640/New%2BDoc_2.jpg" alt="3-K constant for loss coefficients by Chemineering" width="524" height="640" border="0" /></a></div>
<p>Once determining the appropriate K value for your pipe, it can be substituted back into the first equation to determine the pressure drop or headloss</p>
<h2>2. Equivalent Length Method.</h2>
<div class="separator"><a href="http://4.bp.blogspot.com/-ur86cvgzKDU/VVIY3YQI9VI/AAAAAAAAA18/eInFWlzEjrI/s1600/K%2BValue%2B-%2BCopy.jpg" data-wpel-link="external" rel="nofollow external noopener noreferrer"><img loading="lazy" decoding="async" class="aligncenter" src="https://4.bp.blogspot.com/-ur86cvgzKDU/VVIY3YQI9VI/AAAAAAAAA18/eInFWlzEjrI/s200/K%2BValue%2B-%2BCopy.jpg" width="230" height="146" border="0" /></a></div>
<p>Where:</p>
<p>f = Darcy&#8217;s Friction Factor</p>
<p>D = Internal Diameter of the pipe</p>
<p>Another method that is widely used in calculating pressure drop is the equivalent length method. For every valve and fitting particular L/D, equivalent length value is available in the previous table. To find the equivalent length, multiply the L/D value with the diameter and insert this value in the given formula, in place of Leq.</p>
<p>Similarly, for contraction and expansion losses you need to consider the k value as per the following formula.</p>
<div class="separator"><a href="http://3.bp.blogspot.com/-BvuetNDts6A/VVImszc0LyI/AAAAAAAAA2M/gTojuvxZD60/s1600/New%2BDoc_3.jpg" data-wpel-link="external" rel="nofollow external noopener noreferrer"><img loading="lazy" decoding="async" class="aligncenter" title="Contraction and expansion loss coefficient by Chemineering" src="https://3.bp.blogspot.com/-BvuetNDts6A/VVImszc0LyI/AAAAAAAAA2M/gTojuvxZD60/s400/New%2BDoc_3.jpg" alt="Contraction and expansion loss coefficient by Chemineering" width="365" height="400" border="0" /></a></div>
</div>
<div class="saboxplugin-wrap" itemtype="http://schema.org/Person" itemscope itemprop="author"><div class="saboxplugin-tab"><div class="saboxplugin-gravatar"><img loading="lazy" decoding="async" src="https://engineeringness.com/wp-content/uploads/2025/02/1649882991639.jpeg" width="100"  height="100" alt="" itemprop="image"></div><div class="saboxplugin-authorname"><a href="https://engineeringness.com/author/hassan-ahmed/" class="vcard author" rel="author" data-wpel-link="internal"><span class="fn">Hassan Ahmed</span></a></div><div class="saboxplugin-desc"><div itemprop="description"><p>Hassan graduated with a Master’s degree in Chemical Engineering from the University of Chester (UK). He currently works as a design engineering consultant for one of the largest engineering firms in the world along with being an associate member of the Institute of Chemical Engineers (IChemE).</p>
</div></div><div class="clearfix"></div><div class="saboxplugin-socials "><a title="Linkedin" target="_self" href="https://www.linkedin.com/in/hassan-ahmed-961781237/" rel="noopener nofollow external noreferrer" class="saboxplugin-icon-grey" data-wpel-link="external"><svg aria-hidden="true" class="sab-linkedin" role="img" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 448 512"><path fill="currentColor" d="M100.3 480H7.4V180.9h92.9V480zM53.8 140.1C24.1 140.1 0 115.5 0 85.8 0 56.1 24.1 32 53.8 32c29.7 0 53.8 24.1 53.8 53.8 0 29.7-24.1 54.3-53.8 54.3zM448 480h-92.7V334.4c0-34.7-.7-79.2-48.3-79.2-48.3 0-55.7 37.7-55.7 76.7V480h-92.8V180.9h89.1v40.8h1.3c12.4-23.5 42.7-48.3 87.9-48.3 94 0 111.3 61.9 111.3 142.3V480z"></path></svg></span></a></div></div></div><p>The post <a href="https://engineeringness.com/pressure-drop-in-pipe-lines-and-fittings-part-2/" data-wpel-link="internal">Pressure Drop In Pipe Lines And Fittings | Part 2</a> appeared first on <a href="https://engineeringness.com" data-wpel-link="internal">Engineeringness</a>.</p>
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			</item>
		<item>
		<title>Pressure Drop In Pipe Lines And Fittings &#124; Part 1</title>
		<link>https://engineeringness.com/pressure-drop-in-pipe-lines-and-fittings-part-1/</link>
					<comments>https://engineeringness.com/pressure-drop-in-pipe-lines-and-fittings-part-1/#respond</comments>
		
		<dc:creator><![CDATA[Hassan Ahmed]]></dc:creator>
		<pubDate>Wed, 21 Apr 2021 21:46:38 +0000</pubDate>
				<category><![CDATA[Fluid Mechanics]]></category>
		<category><![CDATA[Fanning Friction Factor]]></category>
		<category><![CDATA[Friction Factor]]></category>
		<category><![CDATA[Reynolds Number]]></category>
		<category><![CDATA[Colebrook Equation]]></category>
		<category><![CDATA[Swamee and Jain Equation]]></category>
		<category><![CDATA[Pressure Drop]]></category>
		<category><![CDATA[Haaland Equation]]></category>
		<category><![CDATA[Pipe Flow]]></category>
		<category><![CDATA[Roughness Factor]]></category>
		<category><![CDATA[Skin Friction]]></category>
		<category><![CDATA[Unseparated boundary layers]]></category>
		<category><![CDATA[Boundary layers]]></category>
		<category><![CDATA[Darcy&#039;s Friction Factor]]></category>
		<guid isPermaLink="false">http://52.205.3.27/?p=83777</guid>

					<description><![CDATA[<p>Pressure plays a prominent role in driving and arresting the fluid flow from one place to another. What Pressure Is Involved In Driving Fluid Through Pipes And Fittings? One classical definition is Pressure is force acted per unit area Pressure in a pipeline may be due to pumping, vaporization, compression, etc. The fluid should travel the entire pipeline without losing its pressure otherwise we need to spend extra for pumping the fluid to compromise for the loss in pressure. Why Is Pressure Lost Through Pipes? The reason is due to friction, wake formation, separation of the boundary layer by fittings, pipe</p>
<p>The post <a href="https://engineeringness.com/pressure-drop-in-pipe-lines-and-fittings-part-1/" data-wpel-link="internal">Pressure Drop In Pipe Lines And Fittings | Part 1</a> appeared first on <a href="https://engineeringness.com" data-wpel-link="internal">Engineeringness</a>.</p>
]]></description>
										<content:encoded><![CDATA[<div>Pressure plays a prominent role in driving and arresting the fluid flow from one place to another.</div>
<h2><u>What Pressure Is Involved In Driving Fluid Through Pipes And Fittings?</u></h2>
<div>One classical definition is</div>
<div dir="ltr">
<blockquote class="tr_bq"><p>Pressure is force acted per unit area</p></blockquote>
<div class="separator"></div>
<p>Pressure in a pipeline may be due to pumping, vaporization, compression, etc. The fluid should travel the entire pipeline without losing its pressure otherwise we need to spend extra for pumping the fluid to compromise for the loss in pressure.</p>
<h2><u>Why Is Pressure Lost Through Pipes?</u></h2>
<p>The reason is due to friction, wake formation, separation of the boundary layer by fittings, pipe roughness, etc. In order for the pump to work efficiently, the pump will be designed to accommodate any extra pressure that is required.</p>
<p>Pressure drop due to unseparated boundary layers (Skin friction) can be calculated by the following classical formula,</p>
<div class="separator"></div>
<div class="separator"></div>
<div class="separator"><a href="http://4.bp.blogspot.com/-5tR7NcV_fhc/VQBRsnrVX9I/AAAAAAAAAyM/gEgJM9JB2qA/s1600/Hfs.JPG" data-wpel-link="external" rel="nofollow external noopener noreferrer"><img loading="lazy" decoding="async" class="aligncenter" title="Pressure drop by Cheminnering.blogspot.com" src="https://4.bp.blogspot.com/-5tR7NcV_fhc/VQBRsnrVX9I/AAAAAAAAAyM/gEgJM9JB2qA/s1600/Hfs.JPG" alt="Pressure drop by Cheminnering.blogspot.com" width="320" height="225" border="0" /></a></div>
<div class="separator"></div>
<div class="separator"></div>
<div class="separator">Pressure drop varies with length and diameter of the pipe, velocity, and density of the fluid, and Fanning friction factor. <a href="http://en.wikipedia.org/wiki/Darcy%E2%80%93Weisbach_equation" target="_blank" rel="noopener noreferrer nofollow external" data-wpel-link="external">Don&#8217;t confuse this fanning friction factor with Darcy&#8217;s friction factor</a>.</div>
<div></div>
<div class="separator">The Fanning friction factor varies with the nature of the flow. So if we know the nature of flow i.e., laminar or turbulent we can calculate the &#8216;f &#8216; value accordingly.</div>
<div class="separator"></div>
<div class="separator"><a href="http://4.bp.blogspot.com/-encLxThvXRs/VQBVRV03E8I/AAAAAAAAAyY/Zjm2Y8GEsTY/s1600/Nre.JPG" data-wpel-link="external" rel="nofollow external noopener noreferrer"><img loading="lazy" decoding="async" class="aligncenter" title="Reynolds number by Cheminnering.blogspot.com" src="https://4.bp.blogspot.com/-encLxThvXRs/VQBVRV03E8I/AAAAAAAAAyY/Zjm2Y8GEsTY/s1600/Nre.JPG" alt="Reynolds number by Cheminnering.blogspot.com" width="320" height="255" border="0" /></a></div>
<div class="separator"></div>
<div class="separator">If the flow is laminar the fanning friction varies with Reynolds number as follows,</div>
<div class="separator"></div>
<div class="separator"></div>
<div class="separator"><a href="http://4.bp.blogspot.com/-g1A54hwSrnk/VQBXG1ljwFI/AAAAAAAAAys/u_KWTuu9LlU/s1600/fr.JPG" data-wpel-link="external" rel="nofollow external noopener noreferrer"><img loading="lazy" decoding="async" class="aligncenter" title="Friction factor by Cheminnering.blogspot.com" src="https://4.bp.blogspot.com/-g1A54hwSrnk/VQBXG1ljwFI/AAAAAAAAAys/u_KWTuu9LlU/s1600/fr.JPG" alt="Friction factor by Cheminnering.blogspot.com" width="320" height="101" border="0" /></a></div>
<div class="separator"></div>
<div class="separator">If the flow is turbulent a lot of equations are in practice and you can use any of those equations at the expense of accuracy. the equations are mentioned as follows.</div>
<div class="separator"></div>
<ul>
<li>Colebrook equation (1938)</li>
</ul>
<div class="separator"><a href="http://1.bp.blogspot.com/-Y1mnZSx45sI/VQBaobs9liI/AAAAAAAAAy8/6xYmBLeO7c8/s1600/col.JPG" data-wpel-link="external" rel="nofollow external noopener noreferrer"><img decoding="async" class="aligncenter" title="Colebrook equation from Chemineering.blogspot.com" src="https://1.bp.blogspot.com/-Y1mnZSx45sI/VQBaobs9liI/AAAAAAAAAy8/6xYmBLeO7c8/s1600/col.JPG" alt="Colebrook equation from Chemineering.blogspot.com" border="0" /></a></div>
<div></div>
<ul>
<li>Swamee and Jain equation (1976)</li>
</ul>
<div class="separator"><a href="http://2.bp.blogspot.com/-XTGsddpqs7U/VQBaoQyMJCI/AAAAAAAAAy4/c5lugCbG_iw/s1600/hal.JPG" data-wpel-link="external" rel="nofollow external noopener noreferrer"><img loading="lazy" decoding="async" class="aligncenter" title="Swamee and jain equation from Chemineering.blogspot.com" src="https://2.bp.blogspot.com/-XTGsddpqs7U/VQBaoQyMJCI/AAAAAAAAAy4/c5lugCbG_iw/s1600/hal.JPG" alt="Swamee and jain equation from Chemineering.blogspot.com" width="320" height="71" border="0" /></a></div>
<div></div>
<ul>
<li>Haaland equation. (1983)</li>
</ul>
<div class="separator"><a href="http://4.bp.blogspot.com/-joPeK3LgLXc/VQBaoYw0M1I/AAAAAAAAAzI/WwDTqsHHtNg/s1600/swa.JPG" data-wpel-link="external" rel="nofollow external noopener noreferrer"><img loading="lazy" decoding="async" class="aligncenter" title="Haaland equation from Chemineering.blogspot.com" src="https://4.bp.blogspot.com/-joPeK3LgLXc/VQBaoYw0M1I/AAAAAAAAAzI/WwDTqsHHtNg/s1600/swa.JPG" alt="Haaland equation from Chemineering.blogspot.com" width="320" height="64" border="0" /></a></div>
<div class="separator"></div>
<div class="separator">The &#8216; ε &#8216; symbol corresponds to the roughness factor which depends on the material of the construction of the pipe, whereas D and Re have their usual meaning.</div>
<div></div>
<div class="separator">After calculating the friction factor, we can find the pressure drop due to skin friction in a pipeline by substituting the &#8216; f &#8216; value into the pressure drop formula stated earlier.</div>
<div class="separator"></div>
<div class="separator">In the Second Part pressure drop due to fittings will be covered.</div>
</div>
<div class="saboxplugin-wrap" itemtype="http://schema.org/Person" itemscope itemprop="author"><div class="saboxplugin-tab"><div class="saboxplugin-gravatar"><img loading="lazy" decoding="async" src="https://engineeringness.com/wp-content/uploads/2025/02/1649882991639.jpeg" width="100"  height="100" alt="" itemprop="image"></div><div class="saboxplugin-authorname"><a href="https://engineeringness.com/author/hassan-ahmed/" class="vcard author" rel="author" data-wpel-link="internal"><span class="fn">Hassan Ahmed</span></a></div><div class="saboxplugin-desc"><div itemprop="description"><p>Hassan graduated with a Master’s degree in Chemical Engineering from the University of Chester (UK). He currently works as a design engineering consultant for one of the largest engineering firms in the world along with being an associate member of the Institute of Chemical Engineers (IChemE).</p>
</div></div><div class="clearfix"></div><div class="saboxplugin-socials "><a title="Linkedin" target="_self" href="https://www.linkedin.com/in/hassan-ahmed-961781237/" rel="noopener nofollow external noreferrer" class="saboxplugin-icon-grey" data-wpel-link="external"><svg aria-hidden="true" class="sab-linkedin" role="img" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 448 512"><path fill="currentColor" d="M100.3 480H7.4V180.9h92.9V480zM53.8 140.1C24.1 140.1 0 115.5 0 85.8 0 56.1 24.1 32 53.8 32c29.7 0 53.8 24.1 53.8 53.8 0 29.7-24.1 54.3-53.8 54.3zM448 480h-92.7V334.4c0-34.7-.7-79.2-48.3-79.2-48.3 0-55.7 37.7-55.7 76.7V480h-92.8V180.9h89.1v40.8h1.3c12.4-23.5 42.7-48.3 87.9-48.3 94 0 111.3 61.9 111.3 142.3V480z"></path></svg></span></a></div></div></div><p>The post <a href="https://engineeringness.com/pressure-drop-in-pipe-lines-and-fittings-part-1/" data-wpel-link="internal">Pressure Drop In Pipe Lines And Fittings | Part 1</a> appeared first on <a href="https://engineeringness.com" data-wpel-link="internal">Engineeringness</a>.</p>
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