<?xml version="1.0" encoding="UTF-8"?>
<rss version="2.0" xmlns:content="http://purl.org/rss/1.0/modules/content/" xmlns:dc="http://purl.org/dc/elements/1.1/">
	<channel>
		<title><![CDATA[ForumTotal.com - Engineering Principles & Technology Science]]></title>
		<link>https://forumtotal.com/</link>
		<description><![CDATA[ForumTotal.com - https://forumtotal.com]]></description>
		<pubDate>Mon, 31 Aug 2026 09:01:25 +0000</pubDate>
		<generator>MyBB</generator>
		<item>
			<title><![CDATA[Testing engineering principles on three different solar panel designs]]></title>
			<link>https://forumtotal.com/thread/testing-engineering-principles-on-three-different-solar-panel-designs</link>
			<pubDate>Sat, 27 Jun 2026 01:56:56 +0000</pubDate>
			<dc:creator><![CDATA[<a href="https://forumtotal.com/member.php?action=profile&uid=1977">Chloe.M</a>]]></dc:creator>
			<guid isPermaLink="false">https://forumtotal.com/thread/testing-engineering-principles-on-three-different-solar-panel-designs</guid>
			<description><![CDATA[I thought I understood the basic principles of thermodynamics, but my latest experiment has proven otherwise in a fairly spectacular way. I built a small Stirling engine from plans I found online, trying to demonstrate a simple heat-to-work conversion for a classroom project.<br />
<br />
The design looked straightforward: a displacer piston, a power piston, a temperature differential between a hot plate and a cold sink. I followed every dimension to the millimeter, used brass for the cylinders and Teflon for the seals, checked for leaks with soapy water. The hot end sits at about 200°C, the cold end at roughly 25°C with a water jacket. That should give me a decent temperature gradient, right? I calculated the theoretical efficiency using Carnot’s formula, and for a 175 K difference I expected something sensible, even with real-world losses.<br />
<br />
I fired it up, and nothing. The power piston twitched once, then stopped. I adjusted the flywheel, added a bit of lubrication, checked the seal clearances, even tried a different heat source to ensure steady temperature. Still no sustained motion. I read that regenerators can improve performance, so I stuffed some copper wool into the displacer path, thinking it might store and release heat more effectively. That just made the whole thing sluggish. I am now wondering if my fundamental understanding of the cycle timing is off, or if I am missing something about the relationship between pressure volume changes and the displacer movement. I know the displacer should shift the air between hot and cold zones, but maybe the phase angle between the two pistons is wrong, or my swept volume ratio is out of whack for the temperature delta I have.<br />
<br />
What I really need is someone to look at my numbers and tell me whether the engine should theoretically run with a 175 K difference and a given bore and stroke, or if I am asking for an impossible pressure change. I am looking for a clear explanation of why it fails, not just another tweak to try, because I have already tried tweaks. I want to know specifically how to calculate whether my configuration yields a net positive work loop.]]></description>
			<content:encoded><![CDATA[I thought I understood the basic principles of thermodynamics, but my latest experiment has proven otherwise in a fairly spectacular way. I built a small Stirling engine from plans I found online, trying to demonstrate a simple heat-to-work conversion for a classroom project.<br />
<br />
The design looked straightforward: a displacer piston, a power piston, a temperature differential between a hot plate and a cold sink. I followed every dimension to the millimeter, used brass for the cylinders and Teflon for the seals, checked for leaks with soapy water. The hot end sits at about 200°C, the cold end at roughly 25°C with a water jacket. That should give me a decent temperature gradient, right? I calculated the theoretical efficiency using Carnot’s formula, and for a 175 K difference I expected something sensible, even with real-world losses.<br />
<br />
I fired it up, and nothing. The power piston twitched once, then stopped. I adjusted the flywheel, added a bit of lubrication, checked the seal clearances, even tried a different heat source to ensure steady temperature. Still no sustained motion. I read that regenerators can improve performance, so I stuffed some copper wool into the displacer path, thinking it might store and release heat more effectively. That just made the whole thing sluggish. I am now wondering if my fundamental understanding of the cycle timing is off, or if I am missing something about the relationship between pressure volume changes and the displacer movement. I know the displacer should shift the air between hot and cold zones, but maybe the phase angle between the two pistons is wrong, or my swept volume ratio is out of whack for the temperature delta I have.<br />
<br />
What I really need is someone to look at my numbers and tell me whether the engine should theoretically run with a 175 K difference and a given bore and stroke, or if I am asking for an impossible pressure change. I am looking for a clear explanation of why it fails, not just another tweak to try, because I have already tried tweaks. I want to know specifically how to calculate whether my configuration yields a net positive work loop.]]></content:encoded>
		</item>
		<item>
			<title><![CDATA[How do I find the neutral axis for an unsymmetrical beam section?]]></title>
			<link>https://forumtotal.com/thread/how-do-i-find-the-neutral-axis-for-an-unsymmetrical-beam-section</link>
			<pubDate>Fri, 17 Apr 2026 15:30:11 +0000</pubDate>
			<dc:creator><![CDATA[<a href="https://forumtotal.com/member.php?action=profile&uid=1098">Addison91</a>]]></dc:creator>
			<guid isPermaLink="false">https://forumtotal.com/thread/how-do-i-find-the-neutral-axis-for-an-unsymmetrical-beam-section</guid>
			<description><![CDATA[I’m trying to design a simple beam support and I keep running into confusion about where the true neutral axis lies when the cross-section isn’t symmetrical. My textbook’s explanation about the centroid and moment of area isn’t clicking when I try to apply it to an uneven I-beam.]]></description>
			<content:encoded><![CDATA[I’m trying to design a simple beam support and I keep running into confusion about where the true neutral axis lies when the cross-section isn’t symmetrical. My textbook’s explanation about the centroid and moment of area isn’t clicking when I try to apply it to an uneven I-beam.]]></content:encoded>
		</item>
		<item>
			<title><![CDATA[How do I size a centrifugal pump for a cooling system when system curve has zero hea]]></title>
			<link>https://forumtotal.com/thread/how-do-i-size-a-centrifugal-pump-for-a-cooling-system-when-system-curve-has-zero-hea</link>
			<pubDate>Fri, 17 Apr 2026 11:02:37 +0000</pubDate>
			<dc:creator><![CDATA[<a href="https://forumtotal.com/member.php?action=profile&uid=1850">EleanorT</a>]]></dc:creator>
			<guid isPermaLink="false">https://forumtotal.com/thread/how-do-i-size-a-centrifugal-pump-for-a-cooling-system-when-system-curve-has-zero-hea</guid>
			<description><![CDATA[I’m trying to size a centrifugal pump for a closed-loop cooling system, but I’m getting stuck on the system curve because my static head is essentially zero. My calculations for friction losses seem solid, yet the required pump head feels off when I look at the manufacturer’s charts.]]></description>
			<content:encoded><![CDATA[I’m trying to size a centrifugal pump for a closed-loop cooling system, but I’m getting stuck on the system curve because my static head is essentially zero. My calculations for friction losses seem solid, yet the required pump head feels off when I look at the manufacturer’s charts.]]></content:encoded>
		</item>
		<item>
			<title><![CDATA[How do i calculate total dynamic head for a centrifugal pump with minor losses?]]></title>
			<link>https://forumtotal.com/thread/how-do-i-calculate-total-dynamic-head-for-a-centrifugal-pump-with-minor-losses</link>
			<pubDate>Fri, 10 Apr 2026 15:53:07 +0000</pubDate>
			<dc:creator><![CDATA[<a href="https://forumtotal.com/member.php?action=profile&uid=707">NatalieS</a>]]></dc:creator>
			<guid isPermaLink="false">https://forumtotal.com/thread/how-do-i-calculate-total-dynamic-head-for-a-centrifugal-pump-with-minor-losses</guid>
			<description><![CDATA[I’m trying to size a centrifugal pump for a closed-loop cooling system and I’m stuck on calculating the total dynamic head accurately. My main issue is accounting for the minor losses from the valves and fittings—every time I sum the equivalent lengths, I get a different result, and it’s throwing off my pump selection.]]></description>
			<content:encoded><![CDATA[I’m trying to size a centrifugal pump for a closed-loop cooling system and I’m stuck on calculating the total dynamic head accurately. My main issue is accounting for the minor losses from the valves and fittings—every time I sum the equivalent lengths, I get a different result, and it’s throwing off my pump selection.]]></content:encoded>
		</item>
		<item>
			<title><![CDATA[How do I size a centrifugal pump for a closed-loop cooling system?]]></title>
			<link>https://forumtotal.com/thread/how-do-i-size-a-centrifugal-pump-for-a-closed-loop-cooling-system--4383</link>
			<pubDate>Fri, 10 Apr 2026 12:56:12 +0000</pubDate>
			<dc:creator><![CDATA[<a href="https://forumtotal.com/member.php?action=profile&uid=923">Jeffrey23</a>]]></dc:creator>
			<guid isPermaLink="false">https://forumtotal.com/thread/how-do-i-size-a-centrifugal-pump-for-a-closed-loop-cooling-system--4383</guid>
			<description><![CDATA[I’m trying to size a centrifugal pump for a closed-loop cooling system, but I keep getting stuck on the system curve calculation. My theoretical head requirement seems way too high compared to the actual pressure drop I measured in my test loop, even after accounting for all the fittings and pipe length. I’m wondering if my assumption about the fluid’s specific gravity is throwing things off, or if I’m misapplying the Darcy-Weisbach equation somewhere.]]></description>
			<content:encoded><![CDATA[I’m trying to size a centrifugal pump for a closed-loop cooling system, but I keep getting stuck on the system curve calculation. My theoretical head requirement seems way too high compared to the actual pressure drop I measured in my test loop, even after accounting for all the fittings and pipe length. I’m wondering if my assumption about the fluid’s specific gravity is throwing things off, or if I’m misapplying the Darcy-Weisbach equation somewhere.]]></content:encoded>
		</item>
		<item>
			<title><![CDATA[How do i account for minor losses in TDH for a centrifugal pump?]]></title>
			<link>https://forumtotal.com/thread/how-do-i-account-for-minor-losses-in-tdh-for-a-centrifugal-pump</link>
			<pubDate>Wed, 08 Apr 2026 21:03:13 +0000</pubDate>
			<dc:creator><![CDATA[<a href="https://forumtotal.com/member.php?action=profile&uid=1235">Brian81</a>]]></dc:creator>
			<guid isPermaLink="false">https://forumtotal.com/thread/how-do-i-account-for-minor-losses-in-tdh-for-a-centrifugal-pump</guid>
			<description><![CDATA[I’m trying to size a centrifugal pump for a closed-loop cooling system and I’m stuck on calculating the total dynamic head accurately. My main issue is accounting for all the minor losses from the valves and fittings in my piping layout—I think I might be underestimating their combined effect on the system curve.]]></description>
			<content:encoded><![CDATA[I’m trying to size a centrifugal pump for a closed-loop cooling system and I’m stuck on calculating the total dynamic head accurately. My main issue is accounting for all the minor losses from the valves and fittings in my piping layout—I think I might be underestimating their combined effect on the system curve.]]></content:encoded>
		</item>
		<item>
			<title><![CDATA[How do i size a centrifugal pump for a closed-loop cooling system?]]></title>
			<link>https://forumtotal.com/thread/how-do-i-size-a-centrifugal-pump-for-a-closed-loop-cooling-system--3358</link>
			<pubDate>Wed, 08 Apr 2026 18:07:19 +0000</pubDate>
			<dc:creator><![CDATA[<a href="https://forumtotal.com/member.php?action=profile&uid=2399">Zoey90</a>]]></dc:creator>
			<guid isPermaLink="false">https://forumtotal.com/thread/how-do-i-size-a-centrifugal-pump-for-a-closed-loop-cooling-system--3358</guid>
			<description><![CDATA[I'm trying to size a centrifugal pump for a closed-loop cooling system, but I keep getting stuck on the system curve calculation. My static head is negligible, so it's all about the friction losses, and I'm second-guessing my equivalent length of pipe fittings.]]></description>
			<content:encoded><![CDATA[I'm trying to size a centrifugal pump for a closed-loop cooling system, but I keep getting stuck on the system curve calculation. My static head is negligible, so it's all about the friction losses, and I'm second-guessing my equivalent length of pipe fittings.]]></content:encoded>
		</item>
		<item>
			<title><![CDATA[What should i check when using a single-phase induction motor on a conveyor?]]></title>
			<link>https://forumtotal.com/thread/what-should-i-check-when-using-a-single-phase-induction-motor-on-a-conveyor</link>
			<pubDate>Wed, 08 Apr 2026 16:42:21 +0000</pubDate>
			<dc:creator><![CDATA[<a href="https://forumtotal.com/member.php?action=profile&uid=1538">Gary.H</a>]]></dc:creator>
			<guid isPermaLink="false">https://forumtotal.com/thread/what-should-i-check-when-using-a-single-phase-induction-motor-on-a-conveyor</guid>
			<description><![CDATA[I’m trying to understand the practical limits of using a single-phase induction motor for a small conveyor system I’m prototyping. The motor starts fine under no load, but it seems to struggle and overheat when I try to move even a modest weight, and I’m not sure if the issue is the starting torque or if I’ve simply chosen the wrong type of motor for this constant load application.]]></description>
			<content:encoded><![CDATA[I’m trying to understand the practical limits of using a single-phase induction motor for a small conveyor system I’m prototyping. The motor starts fine under no load, but it seems to struggle and overheat when I try to move even a modest weight, and I’m not sure if the issue is the starting torque or if I’ve simply chosen the wrong type of motor for this constant load application.]]></content:encoded>
		</item>
		<item>
			<title><![CDATA[How do I size a centrifugal pump for a closed-loop cooling system?]]></title>
			<link>https://forumtotal.com/thread/how-do-i-size-a-centrifugal-pump-for-a-closed-loop-cooling-system--2565</link>
			<pubDate>Mon, 06 Apr 2026 17:18:22 +0000</pubDate>
			<dc:creator><![CDATA[<a href="https://forumtotal.com/member.php?action=profile&uid=676">Addison40</a>]]></dc:creator>
			<guid isPermaLink="false">https://forumtotal.com/thread/how-do-i-size-a-centrifugal-pump-for-a-closed-loop-cooling-system--2565</guid>
			<description><![CDATA[I'm trying to size a centrifugal pump for a closed-loop cooling system, and I keep getting stuck on the system curve calculation. My theoretical head requirement seems way higher than what feels practical for the pipe length and fittings I've laid out, which makes me question if I'm properly accounting for all the minor losses.]]></description>
			<content:encoded><![CDATA[I'm trying to size a centrifugal pump for a closed-loop cooling system, and I keep getting stuck on the system curve calculation. My theoretical head requirement seems way higher than what feels practical for the pipe length and fittings I've laid out, which makes me question if I'm properly accounting for all the minor losses.]]></content:encoded>
		</item>
		<item>
			<title><![CDATA[How do I include minor losses in the system curve for a centrifugal pump?]]></title>
			<link>https://forumtotal.com/thread/how-do-i-include-minor-losses-in-the-system-curve-for-a-centrifugal-pump</link>
			<pubDate>Mon, 06 Apr 2026 15:52:43 +0000</pubDate>
			<dc:creator><![CDATA[<a href="https://forumtotal.com/member.php?action=profile&uid=855">Scott27</a>]]></dc:creator>
			<guid isPermaLink="false">https://forumtotal.com/thread/how-do-i-include-minor-losses-in-the-system-curve-for-a-centrifugal-pump</guid>
			<description><![CDATA[I'm trying to size a centrifugal pump for a closed-loop cooling system, but I'm getting stuck on the system curve calculation. My friction loss estimates from the Darcy-Weisbach equation seem okay, but I'm unsure how to properly account for the minor losses from all the elbows and the control valve in a way that feels practical for the final operating point.]]></description>
			<content:encoded><![CDATA[I'm trying to size a centrifugal pump for a closed-loop cooling system, but I'm getting stuck on the system curve calculation. My friction loss estimates from the Darcy-Weisbach equation seem okay, but I'm unsure how to properly account for the minor losses from all the elbows and the control valve in a way that feels practical for the final operating point.]]></content:encoded>
		</item>
		<item>
			<title><![CDATA[What’s the right way to include minor piping losses in pump head?]]></title>
			<link>https://forumtotal.com/thread/what%E2%80%99s-the-right-way-to-include-minor-piping-losses-in-pump-head</link>
			<pubDate>Mon, 06 Apr 2026 14:21:38 +0000</pubDate>
			<dc:creator><![CDATA[<a href="https://forumtotal.com/member.php?action=profile&uid=702">Logan38</a>]]></dc:creator>
			<guid isPermaLink="false">https://forumtotal.com/thread/what%E2%80%99s-the-right-way-to-include-minor-piping-losses-in-pump-head</guid>
			<description><![CDATA[I’m trying to size a centrifugal pump for a closed-loop cooling system, and I keep getting tripped up on how to accurately account for the minor losses from all the elbows and valves in my piping layout. My calculated system curve feels off because I might be underestimating these losses, but the pump selection charts don’t make it clear how much they really affect the required pump head.]]></description>
			<content:encoded><![CDATA[I’m trying to size a centrifugal pump for a closed-loop cooling system, and I keep getting tripped up on how to accurately account for the minor losses from all the elbows and valves in my piping layout. My calculated system curve feels off because I might be underestimating these losses, but the pump selection charts don’t make it clear how much they really affect the required pump head.]]></content:encoded>
		</item>
		<item>
			<title><![CDATA[How do I size a centrifugal pump for a closed-loop cooling system with losses?]]></title>
			<link>https://forumtotal.com/thread/how-do-i-size-a-centrifugal-pump-for-a-closed-loop-cooling-system-with-losses</link>
			<pubDate>Mon, 06 Apr 2026 12:59:35 +0000</pubDate>
			<dc:creator><![CDATA[<a href="https://forumtotal.com/member.php?action=profile&uid=783">MarkM</a>]]></dc:creator>
			<guid isPermaLink="false">https://forumtotal.com/thread/how-do-i-size-a-centrifugal-pump-for-a-closed-loop-cooling-system-with-losses</guid>
			<description><![CDATA[I’m trying to size a centrifugal pump for a closed-loop cooling system, and I keep getting tripped up on how to accurately account for the minor losses from all the elbows and valves in my piping layout. My calculated system curve feels off because I might be underestimating the equivalent length of pipe for these fittings.]]></description>
			<content:encoded><![CDATA[I’m trying to size a centrifugal pump for a closed-loop cooling system, and I keep getting tripped up on how to accurately account for the minor losses from all the elbows and valves in my piping layout. My calculated system curve feels off because I might be underestimating the equivalent length of pipe for these fittings.]]></content:encoded>
		</item>
		<item>
			<title><![CDATA[How do I size a centrifugal pump for a closed-loop system with minor losses?]]></title>
			<link>https://forumtotal.com/thread/how-do-i-size-a-centrifugal-pump-for-a-closed-loop-system-with-minor-losses</link>
			<pubDate>Mon, 06 Apr 2026 11:23:00 +0000</pubDate>
			<dc:creator><![CDATA[<a href="https://forumtotal.com/member.php?action=profile&uid=792">JonathanIT</a>]]></dc:creator>
			<guid isPermaLink="false">https://forumtotal.com/thread/how-do-i-size-a-centrifugal-pump-for-a-closed-loop-system-with-minor-losses</guid>
			<description><![CDATA[I’m trying to size a centrifugal pump for a closed-loop cooling system and I’m stuck on how to accurately account for the minor losses from all the elbows and valves. The textbook system curve examples seem oversimplified compared to my actual piping layout. I’m not sure if my calculated total dynamic head is way off because I’m overcomplicating these friction losses or if I’m still missing something.]]></description>
			<content:encoded><![CDATA[I’m trying to size a centrifugal pump for a closed-loop cooling system and I’m stuck on how to accurately account for the minor losses from all the elbows and valves. The textbook system curve examples seem oversimplified compared to my actual piping layout. I’m not sure if my calculated total dynamic head is way off because I’m overcomplicating these friction losses or if I’m still missing something.]]></content:encoded>
		</item>
		<item>
			<title><![CDATA[How do I reconcile NPSH with a vendor curve for a centrifugal pump?]]></title>
			<link>https://forumtotal.com/thread/how-do-i-reconcile-npsh-with-a-vendor-curve-for-a-centrifugal-pump</link>
			<pubDate>Mon, 06 Apr 2026 10:03:08 +0000</pubDate>
			<dc:creator><![CDATA[<a href="https://forumtotal.com/member.php?action=profile&uid=2245">RileyA</a>]]></dc:creator>
			<guid isPermaLink="false">https://forumtotal.com/thread/how-do-i-reconcile-npsh-with-a-vendor-curve-for-a-centrifugal-pump</guid>
			<description><![CDATA[I'm trying to size a centrifugal pump for a closed-loop cooling system, but I'm getting conflicting results for the required net positive suction head. My calculations seem right based on the pipe friction losses and static head, yet the vendor's curve suggests my available NPSH is too low. I'm worried I'm missing something about the vapor pressure relationship with the system's temperature swing.]]></description>
			<content:encoded><![CDATA[I'm trying to size a centrifugal pump for a closed-loop cooling system, but I'm getting conflicting results for the required net positive suction head. My calculations seem right based on the pipe friction losses and static head, yet the vendor's curve suggests my available NPSH is too low. I'm worried I'm missing something about the vapor pressure relationship with the system's temperature swing.]]></content:encoded>
		</item>
		<item>
			<title><![CDATA[What about minor losses in centrifugal pump sizing and system curve?]]></title>
			<link>https://forumtotal.com/thread/what-about-minor-losses-in-centrifugal-pump-sizing-and-system-curve</link>
			<pubDate>Mon, 06 Apr 2026 08:27:42 +0000</pubDate>
			<dc:creator><![CDATA[<a href="https://forumtotal.com/member.php?action=profile&uid=1609">Stephen.W</a>]]></dc:creator>
			<guid isPermaLink="false">https://forumtotal.com/thread/what-about-minor-losses-in-centrifugal-pump-sizing-and-system-curve</guid>
			<description><![CDATA[I’m trying to size a centrifugal pump for a closed-loop cooling system, and I keep hitting a wall when it comes to the system curve. My calculated friction losses seem okay, but I’m genuinely unsure how to properly account for the minor losses from all the elbows and valves without overcomplicating the model.]]></description>
			<content:encoded><![CDATA[I’m trying to size a centrifugal pump for a closed-loop cooling system, and I keep hitting a wall when it comes to the system curve. My calculated friction losses seem okay, but I’m genuinely unsure how to properly account for the minor losses from all the elbows and valves without overcomplicating the model.]]></content:encoded>
		</item>
	</channel>
</rss>