{"id":6559,"date":"2026-08-30T12:40:28","date_gmt":"2026-08-30T12:40:28","guid":{"rendered":"https:\/\/bbpmfg.com\/?p=6559"},"modified":"2026-08-30T12:40:28","modified_gmt":"2026-08-30T12:40:28","slug":"friction-loss-formula","status":"publish","type":"post","link":"https:\/\/bbpmfg.com\/ar\/blog\/friction-loss-formula\/","title":{"rendered":"\u0635\u064a\u063a\u0629 \u0641\u0642\u062f\u0627\u0646 \u0627\u0644\u0627\u062d\u062a\u0643\u0627\u0643 \u0644\u0623\u0646\u0638\u0645\u0629 \u0627\u0644\u0645\u0636\u062e\u0627\u062a: \u0623\u0645\u062b\u0644\u0629 \u0639\u0645\u0644 \u062f\u0627\u0631\u0633\u064a-\u0648\u0627\u064a\u0633\u0628\u0627\u062e \u0648\u0647\u0627\u0632\u0646-\u0648\u0644\u064a\u0627\u0645\u0632"},"content":{"rendered":"<div class=\"seo-blog-content\" style=\"padding:1px 0;\">\n<p style=\"color:#6b7280; margin:0 0 24px;\">Updated August 2026<\/p>\n<p>A friction loss formula is a calculation that converts resistance inside a pipe into head loss or pressure drop. For ordinary water service, the two formulas you will see most often are Darcy-Weisbach and Hazen-Williams. Darcy-Weisbach starts from velocity, pipe geometry, viscosity, and roughness. Hazen-Williams replaces those fluid and surface terms with an empirical C-factor. Both can produce a useful design estimate, but only when the inputs, unit form, and operating range are stated.<\/p>\n<p>This guide works through both methods line by line. It also shows what neither straight-pipe equation includes: valves, fittings, elevation, required discharge pressure, and the pump&#8217;s full operating curve. If you already know your inputs and only need a quick numerical result, use BBP&#8217;s <a href=\"https:\/\/bbpmfg.com\/blog\/pipe-friction-loss-calculator\/\" style=\"text-decoration:underline; text-underline-offset:3px;\">friction loss calculator<\/a>. This article owns the method-choice and audit trail; the calculator owns interactive calculation.<\/p>\n<p><strong>Scope:<\/strong> the examples below cover ordinary water service at a declared duty point. They do not establish a shortcut for slurry, pulp stock, non-Newtonian liquids, or an old pipe whose internal condition is unknown. A calculation can be perfectly repeatable and still miss field resistance if the flow, inside diameter, viscosity, roughness, C-factor, or fitting data do not describe the installed line.<\/p>\n<p>This is also not the fire hose coefficient formula that dominates the current search results. A hose friction shortcut is built around different coefficients, units, and operating practice; do not insert its C value into either pipe method below. If you are comparing a friction loss formula in pipe design, a friction loss coefficient, or a friction loss formula Hazen-Williams reference, keep the method&#8217;s own coefficient definition and units attached to the calculation.<\/p>\n<div class=\"ecc-stat-strip\" style=\"margin:24px 0; padding:18px 20px; background:#f5f5f5; border:1px solid #e0e0e0; display:grid; grid-template-columns:repeat(auto-fit,minmax(150px,1fr)); gap:16px;\">\n<div><strong style=\"display:block; font-size:1.45em; color:#2d2d2d;\">Re &lt; 2,000<\/strong><span style=\"color:#6b7280;\">Laminar tendency<\/span><\/div>\n<div><strong style=\"display:block; font-size:1.45em; color:#2d2d2d;\">Re 2,000-4,000<\/strong><span style=\"color:#6b7280;\">Transition zone<\/span><\/div>\n<div><strong style=\"display:block; font-size:1.45em; color:#2d2d2d;\">Re &gt; 4,000<\/strong><span style=\"color:#6b7280;\">Turbulent tendency<\/span><\/div>\n<div><strong style=\"display:block; font-size:1.45em; color:#2d2d2d;\">D = inside diameter<\/strong><span style=\"color:#6b7280;\">Not nominal size<\/span><\/div>\n<\/div>\n<h2 style=\"margin:48px 0 16px; padding-bottom:10px; border-bottom:2px solid #2d2d2d;\">Which Friction Loss Formula Should You Use?<\/h2>\n<figure style=\"margin:28px 0; text-align:center;\"><img decoding=\"async\" src=\"https:\/\/bbpmfg.com\/wp-content\/uploads\/2026\/08\/friction-loss-formula-h2_01.png\" alt=\"Which Friction Loss Formula Should You Use? \u2014 BBP\" class=\"wp-image-6550\" width=\"1200\" height=\"800\" loading=\"lazy\" style=\"max-width:100%; height:auto; border-radius:8px;\" srcset=\"https:\/\/bbpmfg.com\/wp-content\/uploads\/2026\/08\/friction-loss-formula-h2_01.png 1200w, https:\/\/bbpmfg.com\/wp-content\/uploads\/2026\/08\/friction-loss-formula-h2_01-300x200.png 300w, https:\/\/bbpmfg.com\/wp-content\/uploads\/2026\/08\/friction-loss-formula-h2_01-1024x683.png 1024w, https:\/\/bbpmfg.com\/wp-content\/uploads\/2026\/08\/friction-loss-formula-h2_01-768x512.png 768w, https:\/\/bbpmfg.com\/wp-content\/uploads\/2026\/08\/friction-loss-formula-h2_01-18x12.png 18w\" sizes=\"auto, (max-width: 1200px) 100vw, 1200px\" \/><\/figure>\n<p>Use Darcy-Weisbach when the fluid properties, temperature, or pipe condition matter, when the liquid is not plain water, or when you need a method that exposes the flow regime. Use Hazen-Williams for turbulent water service when a defensible C-factor and the correct unit-specific equation are already part of the design basis. Do not choose a formula simply because one calculator asks for fewer inputs.<\/p>\n<p>The <a href=\"https:\/\/www.epa.gov\/water-research\/epanet\" style=\"text-decoration:underline; text-underline-offset:3px;\" target=\"_blank\" rel=\"noopener\">U.S. Environmental Protection Agency&#8217;s EPANET page<\/a> lists both Darcy-Weisbach and Hazen-Williams as available friction head-loss methods for water-distribution modeling. That is evidence that both methods have legitimate uses. It is not evidence that the methods share the same assumptions or can be swapped after a calculation has started.<\/p>\n<div class=\"ecc-versus\" style=\"margin:24px 0; display:grid; grid-template-columns:repeat(auto-fit,minmax(260px,1fr)); gap:16px;\">\n<section style=\"padding:20px; border:1px solid #d1d5db; border-top:4px solid #2d2d2d; background:#ffffff;\">\n<h3 style=\"margin:0 0 10px;\">Choose Darcy-Weisbach when&#8230;<\/h3>\n<ul style=\"margin:0; padding-left:20px;\">\n<li>The liquid is not ordinary water.<\/li>\n<li>Temperature or viscosity changes.<\/li>\n<li>Reynolds number may cross flow regimes.<\/li>\n<li>Roughness and pipe age need an explicit assumption.<\/li>\n<li>You need the calculation to connect to a Moody chart or Colebrook method.<\/li>\n<\/ul>\n<\/section>\n<section style=\"padding:20px; border:1px solid #d1d5db; border-top:4px solid #6b7280; background:#f9fafb;\">\n<h3 style=\"margin:0 0 10px;\">Choose Hazen-Williams when&#8230;<\/h3>\n<ul style=\"margin:0; padding-left:20px;\">\n<li>The service is turbulent water flow.<\/li>\n<li>The project specification already calls for it.<\/li>\n<li>A defensible C-factor is documented.<\/li>\n<li>The unit form and coefficient constant are fixed.<\/li>\n<li>You need a quick water-pipe estimate with known limits.<\/li>\n<\/ul>\n<\/section>\n<\/div>\n<p>A useful selection rule is simple: if you can&#8217;t explain where the C-factor came from, use Darcy-Weisbach and document roughness, viscosity, and the friction-factor method instead. If you can&#8217;t classify the Reynolds-number regime, neither method should be treated as a push-button answer.<\/p>\n<h2 style=\"margin:48px 0 16px; padding-bottom:10px; border-bottom:2px solid #2d2d2d;\">Darcy-Weisbach Equation: Inputs, Friction Factor, and Units<\/h2>\n<figure style=\"margin:28px 0; text-align:center;\"><img decoding=\"async\" src=\"https:\/\/bbpmfg.com\/wp-content\/uploads\/2026\/08\/friction-loss-formula-h2_02.png\" alt=\"Darcy-Weisbach Equation: Inputs, Friction Factor, and Units \u2014 BBP\" class=\"wp-image-6551\" width=\"1200\" height=\"800\" loading=\"lazy\" style=\"max-width:100%; height:auto; border-radius:8px;\" srcset=\"https:\/\/bbpmfg.com\/wp-content\/uploads\/2026\/08\/friction-loss-formula-h2_02.png 1200w, https:\/\/bbpmfg.com\/wp-content\/uploads\/2026\/08\/friction-loss-formula-h2_02-300x200.png 300w, https:\/\/bbpmfg.com\/wp-content\/uploads\/2026\/08\/friction-loss-formula-h2_02-1024x683.png 1024w, https:\/\/bbpmfg.com\/wp-content\/uploads\/2026\/08\/friction-loss-formula-h2_02-768x512.png 768w, https:\/\/bbpmfg.com\/wp-content\/uploads\/2026\/08\/friction-loss-formula-h2_02-18x12.png 18w\" sizes=\"auto, (max-width: 1200px) 100vw, 1200px\" \/><\/figure>\n<p>One common mistake is to treat one friction factor as fixed across every flow. That can produce a wrong pressure-drop result because Reynolds number and relative roughness change the resistance model.<\/p>\n<p>The Darcy-Weisbach equation calculates major head loss along a constant-diameter pipe. In head form, it is:<\/p>\n<div style=\"margin:20px 0; padding:18px 20px; background:#f5f5f5; border:1px solid #e0e0e0; border-left:3px solid #2d2d2d; font-family:monospace; font-size:1.06em;\">h<sub>f<\/sub> = f \u00d7 (L \/ D) \u00d7 (v<sup>2<\/sup> \/ 2g)<\/div>\n<p>Here, <strong>h<sub>f<\/sub><\/strong> is friction head loss in meters or feet of the flowing liquid; <strong>f<\/strong> is the dimensionless Darcy friction factor; <strong>L<\/strong> is straight-pipe length; <strong>D<\/strong> is actual inside diameter; <strong>v<\/strong> is mean velocity; and <strong>g<\/strong> is gravitational acceleration. Keep L and D in the same length unit. Head then comes out in that unit.<\/p>\n<p>The diameter of the pipe and the length of pipe set the geometry; the viscosity of the fluid, the pipe surface condition, and turbulence determine resistance. Record the internal diameter, Schedule 40 or another exact wall schedule, and the loss of pressure at each design flow. A Moody diagram can provide a theoretical friction factor, but an accurate and efficient pump selection still depends on the actual supply-line condition.<\/p>\n<p>Velocity comes from the actual flow area, not the nominal pipe label:<\/p>\n<div style=\"margin:20px 0; padding:18px 20px; background:#f5f5f5; border:1px solid #e0e0e0; border-left:3px solid #2d2d2d; font-family:monospace; font-size:1.06em;\">A = \u03c0D<sup>2<\/sup> \/ 4 \u00a0\u00a0\u00a0 and \u00a0\u00a0\u00a0 v = Q \/ A<\/div>\n<p>Next, classify the flow with Reynolds number:<\/p>\n<div style=\"margin:20px 0; padding:18px 20px; background:#f5f5f5; border:1px solid #e0e0e0; border-left:3px solid #2d2d2d; font-family:monospace; font-size:1.06em;\">Re = vD \/ &nu;<\/div>\n<p>The <a href=\"https:\/\/datatool.pumps.org\/fluid-flow-iii\/general\" style=\"text-decoration:underline; text-underline-offset:3px;\" target=\"_blank\" rel=\"noopener\">Hydraulic Institute pipe-friction reference<\/a> places laminar flow below about Re = 2,000, turbulent flow above about Re = 4,000, and calls the interval between them a critical or transition zone. For laminar flow, f = 64\/Re. For turbulent flow, use a documented Colebrook solution, Moody chart, or named explicit approximation. Do not feed a transition-zone Reynolds number into a turbulent correlation and report the result as uniquely determined.<\/p>\n<blockquote style=\"margin:24px 0; padding:20px 24px; background:#f5f5f5; border-left:3px solid #2d2d2d;\">\n<p style=\"margin:0;\">\u201cThe Colebrook Equation offers a reliable means for computing the Darcy-Weisbach friction factor.\u201d<\/p>\n<footer style=\"margin-top:8px; color:#6b7280;\">\u2014 <a href=\"https:\/\/datatool.pumps.org\/fluid-flow-iii\/general\" style=\"text-decoration:underline; text-underline-offset:3px;\" target=\"_blank\" rel=\"noopener\">Hydraulic Institute Data Tool<\/a><\/footer>\n<\/blockquote>\n<p>For a turbulent example that must be reproducible without an iterative solver, this article uses the Swamee-Jain approximation:<\/p>\n<div style=\"margin:20px 0; padding:18px 20px; background:#f5f5f5; border:1px solid #e0e0e0; border-left:3px solid #2d2d2d; font-family:monospace; font-size:1.02em;\">f = 0.25 \/ [log<sub>10<\/sub>(\u03b5\/(3.7D) + 5.74\/Re<sup>0.9<\/sup>)]<sup>2<\/sup><\/div>\n<p>That choice is part of the record. Someone repeating the work with an iterative Colebrook solution may obtain a slightly different last decimal. That is acceptable; hiding the selected friction-factor convention is not.<\/p>\n<h2 style=\"margin:48px 0 16px; padding-bottom:10px; border-bottom:2px solid #2d2d2d;\">Darcy-Weisbach Worked Example in SI Units<\/h2>\n<figure style=\"margin:28px 0; text-align:center;\"><img decoding=\"async\" src=\"https:\/\/bbpmfg.com\/wp-content\/uploads\/2026\/08\/friction-loss-formula-h2_03.png\" alt=\"Darcy-Weisbach Worked Example in SI Units \u2014 BBP\" class=\"wp-image-6552\" width=\"1200\" height=\"800\" loading=\"lazy\" style=\"max-width:100%; height:auto; border-radius:8px;\" srcset=\"https:\/\/bbpmfg.com\/wp-content\/uploads\/2026\/08\/friction-loss-formula-h2_03.png 1200w, https:\/\/bbpmfg.com\/wp-content\/uploads\/2026\/08\/friction-loss-formula-h2_03-300x200.png 300w, https:\/\/bbpmfg.com\/wp-content\/uploads\/2026\/08\/friction-loss-formula-h2_03-1024x683.png 1024w, https:\/\/bbpmfg.com\/wp-content\/uploads\/2026\/08\/friction-loss-formula-h2_03-768x512.png 768w, https:\/\/bbpmfg.com\/wp-content\/uploads\/2026\/08\/friction-loss-formula-h2_03-18x12.png 18w\" sizes=\"auto, (max-width: 1200px) 100vw, 1200px\" \/><\/figure>\n<p>Suppose water at approximately 20&deg;C flows through 100 m of commercial-steel pipe. The declared inputs are Q = 0.010 m<sup>3<\/sup>\/s, D = 0.100 m actual inside diameter, absolute roughness &epsilon; = 0.000045 m, and assumed kinematic viscosity &nu; = 1.004 &times; 10<sup>-6<\/sup> m<sup>2<\/sup>\/s. The example ignores fittings and elevation so that it isolates major loss under the <a href=\"https:\/\/datatool.pumps.org\/fluid-flow-iii\/general\" style=\"text-decoration:underline; text-underline-offset:3px;\" target=\"_blank\" rel=\"noopener\">Hydraulic Institute major-loss formulation<\/a>.<\/p>\n<ol style=\"padding-left:22px;\">\n<li><strong>Calculate area:<\/strong> A = \u03c0(0.100)<sup>2<\/sup>\/4 = 0.007854 m<sup>2<\/sup>.<\/li>\n<li><strong>Calculate velocity:<\/strong> v = 0.010\/0.007854 = 1.273 m\/s.<\/li>\n<li><strong>Calculate Reynolds number:<\/strong> Re = (1.273 \u00d7 0.100)\/(1.004 \u00d7 10<sup>-6<\/sup>) = 126,817. This is well above 4,000, so the turbulent method is appropriate.<\/li>\n<li><strong>Calculate Darcy friction factor:<\/strong> the stated Swamee-Jain form gives f = 0.01960.<\/li>\n<li><strong>Calculate head loss:<\/strong> h<sub>f<\/sub> = 0.01960 \u00d7 (100\/0.100) \u00d7 [1.273<sup>2<\/sup>\/(2 \u00d7 9.80665)] = 1.620 m.<\/li>\n<li><strong>Convert head to pressure for water:<\/strong> using assumed \u03c1 = 1,000 kg\/m<sup>3<\/sup>, \u0394p = \u03c1gh = 1,000 \u00d7 9.80665 \u00d7 1.620 = 15.89 kPa.<\/li>\n<\/ol>\n<div class=\"ecc-takeaway\" style=\"margin:24px 0; padding:20px 24px; background:#f5f5f5; border:1px solid #e0e0e0; border-top:3px solid #2d2d2d;\"><strong>Darcy example result:<\/strong> 1.620 m of friction head, equal to about 15.89 kPa for water, across 100 m of straight pipe at the stated duty point. This is not the pump&#8217;s total dynamic head because static elevation, endpoint pressure, and component losses have not been added.<\/div>\n<p>The arithmetic is auditable, but the field result is only as sound as the inputs. A 5% diameter assumption error can create a much larger head-loss error because velocity and L\/D both change. If the pipe has deposits, corrosion, a different schedule, or a temperature that changes viscosity, rerun the calculation with measured or project-approved values. \u201cCommercial steel\u201d is not a substitute for inspecting an old line.<\/p>\n<h2 style=\"margin:48px 0 16px; padding-bottom:10px; border-bottom:2px solid #2d2d2d;\">Hazen-Williams Formula: Where the C-Factor Fits<\/h2>\n<figure style=\"margin:28px 0; text-align:center;\"><img decoding=\"async\" src=\"https:\/\/bbpmfg.com\/wp-content\/uploads\/2026\/08\/friction-loss-formula-h2_04.png\" alt=\"Hazen-Williams Formula: Where the C-Factor Fits \u2014 BBP\" class=\"wp-image-6553\" width=\"1200\" height=\"800\" loading=\"lazy\" style=\"max-width:100%; height:auto; border-radius:8px;\" srcset=\"https:\/\/bbpmfg.com\/wp-content\/uploads\/2026\/08\/friction-loss-formula-h2_04.png 1200w, https:\/\/bbpmfg.com\/wp-content\/uploads\/2026\/08\/friction-loss-formula-h2_04-300x200.png 300w, https:\/\/bbpmfg.com\/wp-content\/uploads\/2026\/08\/friction-loss-formula-h2_04-1024x683.png 1024w, https:\/\/bbpmfg.com\/wp-content\/uploads\/2026\/08\/friction-loss-formula-h2_04-768x512.png 768w, https:\/\/bbpmfg.com\/wp-content\/uploads\/2026\/08\/friction-loss-formula-h2_04-18x12.png 18w\" sizes=\"auto, (max-width: 1200px) 100vw, 1200px\" \/><\/figure>\n<p>Hazen-Williams is an empirical water-pipe formula. In one common U.S. customary pressure-loss form, with pressure loss in psi, length in feet, flow in U.S. gallons per minute, and inside diameter in inches, it is:<\/p>\n<div style=\"margin:20px 0; padding:18px 20px; background:#f5f5f5; border:1px solid #e0e0e0; border-left:3px solid #2d2d2d; font-family:monospace; font-size:1.04em;\">\u0394p (psi) = 4.52 \u00d7 L \u00d7 Q<sup>1.852<\/sup> \/ (C<sup>1.852<\/sup> \u00d7 d<sup>4.87<\/sup>)<\/div>\n<p>The constant 4.52 belongs to that exact unit set and pressure form. A metric head-loss version uses a different constant. Copying the constant while changing gallons per minute to cubic meters per hour, inches to millimeters, or psi to meters of head will not produce a unit conversion; it will produce a wrong answer.<\/p>\n<p>The C-factor is not a measured wall height like Darcy roughness. It is an empirical resistance coefficient tied to pipe material, condition, diameter, and the data behind the selected value. An attributed comparison published on <a href=\"https:\/\/aspe.org\/pipeline\/hazen-williams-and-darcy-weisbach-equations-similarities-and-differences\/\" style=\"text-decoration:underline; text-underline-offset:3px;\" target=\"_blank\" rel=\"noopener\">ASPE Pipeline<\/a> notes that Hazen-Williams does not contain temperature, density, or viscosity terms. That is why this article keeps its use to turbulent water service and treats C as a design assumption.<\/p>\n<h3 style=\"margin:28px 0 12px;\">3-Level Coefficient-Provenance Framework<\/h3>\n<div class=\"ecc-dodont\" style=\"margin:24px 0; display:grid; grid-template-columns:repeat(auto-fit,minmax(260px,1fr)); gap:16px;\">\n<section style=\"padding:20px; background:#f5f5f5; border-left:4px solid #2d2d2d;\">\n<h3 style=\"margin:0 0 10px;\">Coefficient-Provenance Stoplight: Green<\/h3>\n<p style=\"margin:0;\">Project specification, calibrated model, recent test, or owner-approved value; actual inside diameter and water temperature are recorded; the duty point is turbulent.<\/p>\n<\/section>\n<section style=\"padding:20px; background:#fafafa; border-left:4px solid #9ca3af;\">\n<h3 style=\"margin:0 0 10px;\">Yellow<\/h3>\n<p style=\"margin:0;\">Handbook C-factor for a known new pipe material. Use for an estimate, label the source and pipe condition, then test sensitivity.<\/p>\n<\/section>\n<section style=\"padding:20px; background:#fff; border-left:4px solid #6b7280;\">\n<h3 style=\"margin:0 0 10px;\">Red<\/h3>\n<p style=\"margin:0;\">Unknown pipe age, unknown lining, visible deposits, guessed nominal diameter, non-water liquid, or an undocumented C-factor copied from a calculator.<\/p>\n<\/section>\n<\/div>\n<p>A green provenance record does not promise that the installed line matches the coefficient forever. It means the assumption is traceable and was suitable for the stated design decision. Field calibration remains the stronger basis when aging, deposits, or operating history can change resistance.<\/p>\n<h2 style=\"margin:48px 0 16px; padding-bottom:10px; border-bottom:2px solid #2d2d2d;\">Hazen-Williams Worked Example in US Customary Units<\/h2>\n<figure style=\"margin:28px 0; text-align:center;\"><img decoding=\"async\" src=\"https:\/\/bbpmfg.com\/wp-content\/uploads\/2026\/08\/friction-loss-formula-h2_05.png\" alt=\"Hazen-Williams Worked Example in US Customary Units \u2014 BBP\" class=\"wp-image-6554\" width=\"1200\" height=\"800\" loading=\"lazy\" style=\"max-width:100%; height:auto; border-radius:8px;\" srcset=\"https:\/\/bbpmfg.com\/wp-content\/uploads\/2026\/08\/friction-loss-formula-h2_05.png 1200w, https:\/\/bbpmfg.com\/wp-content\/uploads\/2026\/08\/friction-loss-formula-h2_05-300x200.png 300w, https:\/\/bbpmfg.com\/wp-content\/uploads\/2026\/08\/friction-loss-formula-h2_05-1024x683.png 1024w, https:\/\/bbpmfg.com\/wp-content\/uploads\/2026\/08\/friction-loss-formula-h2_05-768x512.png 768w, https:\/\/bbpmfg.com\/wp-content\/uploads\/2026\/08\/friction-loss-formula-h2_05-18x12.png 18w\" sizes=\"auto, (max-width: 1200px) 100vw, 1200px\" \/><\/figure>\n<p>Consider 500 ft of water pipe carrying 500 gpm. The actual inside diameter is 6.065 in and the declared Hazen-Williams C-factor is 130. The <a href=\"https:\/\/www.nist.gov\/pml\/special-publication-811\/nist-guide-si-appendix-b-conversion-factors\/nist-guide-si-appendix-b8\" style=\"text-decoration:underline; text-underline-offset:3px;\" target=\"_blank\" rel=\"noopener\">NIST SI conversion table<\/a> lists 1 U.S. gpm as 6.309020 &times; 10<sup>-5<\/sup> m<sup>3<\/sup>\/s; retaining that conversion in the receipt makes the cross-check reproducible.<\/p>\n<ol style=\"padding-left:22px;\">\n<li><strong>Insert the stated values:<\/strong> \u0394p = 4.52 \u00d7 500 \u00d7 500<sup>1.852<\/sup> \/ [130<sup>1.852<\/sup> \u00d7 6.065<sup>4.87<\/sup>].<\/li>\n<li><strong>Calculate pressure loss:<\/strong> &Delta;p = 4.219 psi across 500 ft.<\/li>\n<li><strong>Normalize by length:<\/strong> 4.219\/5 = 0.844 psi per 100 ft.<\/li>\n<li><strong>Convert to water head:<\/strong> 4.219 psi corresponds to about 9.73 ft of water head at the stated water condition.<\/li>\n<\/ol>\n<div class=\"ecc-takeaway\" style=\"margin:24px 0; padding:20px 24px; background:#f5f5f5; border:1px solid #e0e0e0; border-top:3px solid #2d2d2d;\"><strong>Hazen-Williams example result:<\/strong> 4.219 psi, or 9.73 ft of water head, across 500 ft of pipe. The per-100-ft value is 0.844 psi. Keep the 500-ft total when assembling system head; the normalized value is only a comparison aid.<\/div>\n<p>This example is also turbulent. Using the same line&#8217;s flow and diameter with ordinary water gives Re &asymp; 230,599, comfortably above the transition zone. That check matters because \u201cwater service\u201d alone is not a complete Hazen-Williams boundary.<\/p>\n<h2 style=\"margin:48px 0 16px; padding-bottom:10px; border-bottom:2px solid #2d2d2d;\">Darcy-Weisbach vs Hazen-Williams: Same-Line Reconciliation<\/h2>\n<figure style=\"margin:28px 0; text-align:center;\"><img decoding=\"async\" src=\"https:\/\/bbpmfg.com\/wp-content\/uploads\/2026\/08\/friction-loss-formula-h2_06.png\" alt=\"Darcy-Weisbach vs Hazen-Williams: Same-Line Reconciliation \u2014 BBP\" class=\"wp-image-6555\" width=\"1200\" height=\"800\" loading=\"lazy\" style=\"max-width:100%; height:auto; border-radius:8px;\" srcset=\"https:\/\/bbpmfg.com\/wp-content\/uploads\/2026\/08\/friction-loss-formula-h2_06.png 1200w, https:\/\/bbpmfg.com\/wp-content\/uploads\/2026\/08\/friction-loss-formula-h2_06-300x200.png 300w, https:\/\/bbpmfg.com\/wp-content\/uploads\/2026\/08\/friction-loss-formula-h2_06-1024x683.png 1024w, https:\/\/bbpmfg.com\/wp-content\/uploads\/2026\/08\/friction-loss-formula-h2_06-768x512.png 768w, https:\/\/bbpmfg.com\/wp-content\/uploads\/2026\/08\/friction-loss-formula-h2_06-18x12.png 18w\" sizes=\"auto, (max-width: 1200px) 100vw, 1200px\" \/><\/figure>\n<p>The practical risk is a pump-selection mismatch: two valid-looking methods can disagree because their resistance inputs represent different pipe assumptions. The <a href=\"https:\/\/www.epa.gov\/water-research\/epanet\" style=\"text-decoration:underline; text-underline-offset:3px;\" target=\"_blank\" rel=\"noopener\">U.S. Environmental Protection Agency&#8217;s EPANET method list<\/a> keeps Darcy-Weisbach and Hazen-Williams as distinct choices, so treat the gap as a review trigger, not a reason to average the answers.<\/p>\n<p>Now apply Darcy-Weisbach to the same 500 gpm, 6.065 in ID, 500 ft water line. Declare commercial-steel roughness as 0.00015 ft and assumed water kinematic viscosity as 1.217 &times; 10<sup>-5<\/sup> ft<sup>2<\/sup>\/s. The calculation gives velocity 5.553 ft\/s, Re = 230,599, Darcy f = 0.01749, and head loss = 8.292 ft. That equals about 3.594 psi for water.<\/p>\n<div style=\"margin:24px 0; overflow-x:auto;\">\n<table style=\"width:100%; border-collapse:collapse; border:1px solid #e0e0e0;\">\n<caption style=\"caption-side:top; text-align:left; font-weight:600; padding:8px 0; color:#2d2d2d;\">Same-Line Dual-Method Reconciliation Table<\/caption>\n<thead>\n<tr style=\"background:#2d2d2d; color:#fff;\">\n<th scope=\"col\" style=\"padding:11px 14px; text-align:left;\">Audit category<\/th>\n<th scope=\"col\" style=\"padding:11px 14px; text-align:left;\">Darcy-Weisbach<\/th>\n<th scope=\"col\" style=\"padding:11px 14px; text-align:left;\">Hazen-Williams<\/th>\n<\/tr>\n<\/thead>\n<tbody>\n<tr style=\"border-bottom:1px solid #e0e0e0;\">\n<td style=\"padding:10px 14px;\">Flow<\/td>\n<td colspan=\"2\" style=\"padding:10px 14px;\">500 gpm<\/td>\n<\/tr>\n<tr style=\"background:#f5f5f5; border-bottom:1px solid #e0e0e0;\">\n<td style=\"padding:10px 14px;\">Actual inside diameter<\/td>\n<td colspan=\"2\" style=\"padding:10px 14px;\">6.065 in<\/td>\n<\/tr>\n<tr style=\"border-bottom:1px solid #e0e0e0;\">\n<td style=\"padding:10px 14px;\">Straight-pipe length<\/td>\n<td colspan=\"2\" style=\"padding:10px 14px;\">500 ft<\/td>\n<\/tr>\n<tr style=\"background:#f5f5f5; border-bottom:1px solid #e0e0e0;\">\n<td style=\"padding:10px 14px;\">Fluid and regime<\/td>\n<td colspan=\"2\" style=\"padding:10px 14px;\">Water; turbulent at Re = 230,599<\/td>\n<\/tr>\n<tr style=\"border-bottom:1px solid #e0e0e0;\">\n<td style=\"padding:10px 14px;\">Resistance input<\/td>\n<td style=\"padding:10px 14px;\">\u03b5 = 0.00015 ft; f = 0.01749<\/td>\n<td style=\"padding:10px 14px;\">C = 130<\/td>\n<\/tr>\n<tr style=\"background:#f5f5f5; border-bottom:1px solid #e0e0e0;\">\n<td style=\"padding:10px 14px;\">Velocity<\/td>\n<td colspan=\"2\" style=\"padding:10px 14px;\">5.553 ft\/s<\/td>\n<\/tr>\n<tr style=\"border-bottom:1px solid #e0e0e0;\">\n<td style=\"padding:10px 14px;\">Head loss<\/td>\n<td style=\"padding:10px 14px;\"><strong>8.292 ft<\/strong><\/td>\n<td style=\"padding:10px 14px;\"><strong>9.731 ft<\/strong><\/td>\n<\/tr>\n<tr style=\"background:#f5f5f5; border-bottom:1px solid #e0e0e0;\">\n<td style=\"padding:10px 14px;\">Pressure loss<\/td>\n<td style=\"padding:10px 14px;\">3.594 psi<\/td>\n<td style=\"padding:10px 14px;\">4.219 psi<\/td>\n<\/tr>\n<tr style=\"border-bottom:1px solid #e0e0e0;\">\n<td style=\"padding:10px 14px;\">Difference in this scenario<\/td>\n<td colspan=\"2\" style=\"padding:10px 14px;\">Hazen-Williams is 17.4% higher than Darcy-Weisbach.<\/td>\n<\/tr>\n<\/tbody>\n<\/table>\n<\/div>\n<p>The 17.4% gap is not a universal correction factor. It is the result of pairing one roughness assumption with one C-factor at one duty point. Other valid water-distribution inputs may make the methods agree more closely or diverge further. The table&#8217;s purpose is to expose the modeling assumptions, not crown a winner from one line.<\/p>\n<p>When the two answers differ enough to affect pump selection, pipe size, or energy cost, do not average them. Check actual inside diameter, flow measurement, temperature, roughness or C-factor origin, and flow-regime method. Then choose the equation that matches the project&#8217;s design basis.<\/p>\n<h2 style=\"margin:48px 0 16px; padding-bottom:10px; border-bottom:2px solid #2d2d2d;\">Add Minor Losses Before You Use Friction Loss in TDH<\/h2>\n<figure style=\"margin:28px 0; text-align:center;\"><img decoding=\"async\" src=\"https:\/\/bbpmfg.com\/wp-content\/uploads\/2026\/08\/friction-loss-formula-h2_07.png\" alt=\"Add Minor Losses Before You Use Friction Loss in TDH \u2014 BBP\" class=\"wp-image-6556\" width=\"1200\" height=\"800\" loading=\"lazy\" style=\"max-width:100%; height:auto; border-radius:8px;\" srcset=\"https:\/\/bbpmfg.com\/wp-content\/uploads\/2026\/08\/friction-loss-formula-h2_07.png 1200w, https:\/\/bbpmfg.com\/wp-content\/uploads\/2026\/08\/friction-loss-formula-h2_07-300x200.png 300w, https:\/\/bbpmfg.com\/wp-content\/uploads\/2026\/08\/friction-loss-formula-h2_07-1024x683.png 1024w, https:\/\/bbpmfg.com\/wp-content\/uploads\/2026\/08\/friction-loss-formula-h2_07-768x512.png 768w, https:\/\/bbpmfg.com\/wp-content\/uploads\/2026\/08\/friction-loss-formula-h2_07-18x12.png 18w\" sizes=\"auto, (max-width: 1200px) 100vw, 1200px\" \/><\/figure>\n<p>Darcy-Weisbach major loss covers wall friction in straight pipe. A valve, elbow, tee, reducer, strainer, entrance, or exit adds a local loss. The Hydraulic Institute fitting reference expresses one component as:<\/p>\n<div style=\"margin:20px 0; padding:18px 20px; background:#f5f5f5; border:1px solid #e0e0e0; border-left:3px solid #2d2d2d; font-family:monospace; font-size:1.06em;\">h<sub>m<\/sub> = K \u00d7 (v<sup>2<\/sup> \/ 2g)<\/div>\n<p>If all K values use the same reference velocity and compatible definitions, major and minor losses can be combined:<\/p>\n<div style=\"margin:20px 0; padding:18px 20px; background:#f5f5f5; border:1px solid #e0e0e0; border-left:3px solid #2d2d2d; font-family:monospace; font-size:1.06em;\">h<sub>loss<\/sub> = [f(L\/D) + \u03a3K] \u00d7 (v<sup>2<\/sup> \/ 2g)<\/div>\n<p>The <a href=\"https:\/\/datatool.pumps.org\/fluid-flow-iii\/fr-loss-water\" style=\"text-decoration:underline; text-underline-offset:3px;\" target=\"_blank\" rel=\"noopener\">Hydraulic Institute fitting-loss page<\/a> also shows why K is not a magic fixed number. Published ranges vary with fitting type, geometry, size, and condition; the page&#8217;s examples range from roughly &plusmn;10% for some 45-degree elbows to +200%\/-80% for a flanged check valve. Record valve position and fitting geometry rather than copying a bare K column.<\/p>\n<p>Total dynamic head goes one step further:<\/p>\n<div style=\"margin:20px 0; padding:18px 20px; background:#f5f5f5; border:1px solid #e0e0e0; border-left:3px solid #2d2d2d; font-family:monospace; font-size:1.04em;\">TDH = static elevation difference + required pressure head + major losses + minor losses<\/div>\n<p>Do not add nozzle pressure, static head, or fitting losses inside the straight-pipe formula and then add them again in TDH. That double-counting produces an oversized duty point. Use BBP&#8217;s <a href=\"https:\/\/bbpmfg.com\/irrigation-pumps\/agriculture-pump\/total-dynamic-head-tdh-calculator\/\" style=\"text-decoration:underline; text-underline-offset:3px;\">total dynamic head calculator<\/a> when you are ready to assemble the complete head balance.<\/p>\n<h2 style=\"margin:48px 0 16px; padding-bottom:10px; border-bottom:2px solid #2d2d2d;\">Why Flow, Diameter, and Roughness Change the Result<\/h2>\n<figure style=\"margin:28px 0; text-align:center;\"><img decoding=\"async\" src=\"https:\/\/bbpmfg.com\/wp-content\/uploads\/2026\/08\/friction-loss-formula-h2_08.png\" alt=\"Why Flow, Diameter, and Roughness Change the Result \u2014 BBP\" class=\"wp-image-6557\" width=\"1200\" height=\"800\" loading=\"lazy\" style=\"max-width:100%; height:auto; border-radius:8px;\" srcset=\"https:\/\/bbpmfg.com\/wp-content\/uploads\/2026\/08\/friction-loss-formula-h2_08.png 1200w, https:\/\/bbpmfg.com\/wp-content\/uploads\/2026\/08\/friction-loss-formula-h2_08-300x200.png 300w, https:\/\/bbpmfg.com\/wp-content\/uploads\/2026\/08\/friction-loss-formula-h2_08-1024x683.png 1024w, https:\/\/bbpmfg.com\/wp-content\/uploads\/2026\/08\/friction-loss-formula-h2_08-768x512.png 768w, https:\/\/bbpmfg.com\/wp-content\/uploads\/2026\/08\/friction-loss-formula-h2_08-18x12.png 18w\" sizes=\"auto, (max-width: 1200px) 100vw, 1200px\" \/><\/figure>\n<p>At fixed flow, a smaller inside diameter raises velocity and increases the length-to-diameter ratio at the same time. That makes diameter errors far more damaging than their percentage suggests. Recomputing the 500 gpm Darcy line at three actual diameters gives:<\/p>\n<div style=\"margin:24px 0; overflow-x:auto;\">\n<table style=\"width:100%; border-collapse:collapse; border:1px solid #e0e0e0;\">\n<caption style=\"caption-side:top; text-align:left; font-weight:600; padding:8px 0; color:#2d2d2d;\">Inside-diameter sensitivity at fixed 500 gpm and 500 ft<\/caption>\n<thead>\n<tr style=\"background:#2d2d2d; color:#fff;\">\n<th scope=\"col\" style=\"padding:11px 14px; text-align:left;\">Actual ID change<\/th>\n<th scope=\"col\" style=\"padding:11px 14px; text-align:left;\">Darcy head loss<\/th>\n<th scope=\"col\" style=\"padding:11px 14px; text-align:left;\">Change from base<\/th>\n<\/tr>\n<\/thead>\n<tbody>\n<tr style=\"border-bottom:1px solid #e0e0e0;\">\n<td style=\"padding:10px 14px;\">-5%<\/td>\n<td style=\"padding:10px 14px;\">10.721 ft<\/td>\n<td style=\"padding:10px 14px;\"><strong>+29.3%<\/strong><\/td>\n<\/tr>\n<tr style=\"background:#f5f5f5; border-bottom:1px solid #e0e0e0;\">\n<td style=\"padding:10px 14px;\">Base: 6.065 in<\/td>\n<td style=\"padding:10px 14px;\">8.292 ft<\/td>\n<td style=\"padding:10px 14px;\">0%<\/td>\n<\/tr>\n<tr>\n<td style=\"padding:10px 14px;\">+5%<\/td>\n<td style=\"padding:10px 14px;\">6.497 ft<\/td>\n<td style=\"padding:10px 14px;\"><strong>-21.6%<\/strong><\/td>\n<\/tr>\n<\/tbody>\n<\/table>\n<\/div>\n<p>This is the Head-to-Pressure Dimensional Checksum: confirm flow unit, confirm actual diameter, compute velocity, classify Reynolds number, select the resistance method, calculate head, and only then convert head to pressure for a named fluid. Reversing that order often hides a unit error.<\/p>\n<p>One duty-point result still does not describe the full system curve. Flow changes velocity, Reynolds number, friction factor, and loss. The 2026 <a href=\"https:\/\/www.pumps.org\/2026\/04\/20\/the-hydraulic-institute-hi-data-tool-for-pump-systems\/\" style=\"text-decoration:underline; text-underline-offset:3px;\" target=\"_blank\" rel=\"noopener\">Hydraulic Institute data-tool overview<\/a> treats system curves, pump curves, and their intersection as separate parts of pump-system analysis. Calculate enough points to locate the expected operating range, then compare that curve with the selected pump curve.<\/p>\n<p>Once the duty head is established, connect it to motor demand with BBP&#8217;s <a href=\"https:\/\/bbpmfg.com\/blog\/pump-power-formula\/\" style=\"text-decoration:underline; text-underline-offset:3px;\">pump power formula<\/a>. Friction head raises required pump head; required head and flow then determine hydraulic power.<\/p>\n<h2 style=\"margin:48px 0 16px; padding-bottom:10px; border-bottom:2px solid #2d2d2d;\">Friction Loss Calculation Audit Checklist<\/h2>\n<figure style=\"margin:28px 0; text-align:center;\"><img decoding=\"async\" src=\"https:\/\/bbpmfg.com\/wp-content\/uploads\/2026\/08\/friction-loss-formula-h2_09.png\" alt=\"Friction Loss Calculation Audit Checklist \u2014 BBP\" class=\"wp-image-6558\" width=\"1200\" height=\"800\" loading=\"lazy\" style=\"max-width:100%; height:auto; border-radius:8px;\" srcset=\"https:\/\/bbpmfg.com\/wp-content\/uploads\/2026\/08\/friction-loss-formula-h2_09.png 1200w, https:\/\/bbpmfg.com\/wp-content\/uploads\/2026\/08\/friction-loss-formula-h2_09-300x200.png 300w, https:\/\/bbpmfg.com\/wp-content\/uploads\/2026\/08\/friction-loss-formula-h2_09-1024x683.png 1024w, https:\/\/bbpmfg.com\/wp-content\/uploads\/2026\/08\/friction-loss-formula-h2_09-768x512.png 768w, https:\/\/bbpmfg.com\/wp-content\/uploads\/2026\/08\/friction-loss-formula-h2_09-18x12.png 18w\" sizes=\"auto, (max-width: 1200px) 100vw, 1200px\" \/><\/figure>\n<p>A calculation record should let another engineer reproduce the result without guessing what \u201cstandard pipe\u201d or \u201cnormal water\u201d meant. Save the following items with the pump request for quotation or design note:<\/p>\n<ul style=\"padding-left:22px;\">\n<li>Fluid name, concentration if relevant, temperature, density, and viscosity source.<\/li>\n<li>Flow rate, unit, operating range, and whether it was measured or specified.<\/li>\n<li>Pipe material, schedule, actual inside diameter, length by diameter, age, lining, and known deposits.<\/li>\n<li>Selected formula and exact unit form.<\/li>\n<li>Reynolds number and the flow-regime decision.<\/li>\n<li>Darcy friction factor method plus roughness source, or Hazen-Williams C-factor plus provenance.<\/li>\n<li>Every fitting and valve, its position, K or equivalent-length source, and reference velocity.<\/li>\n<li>Major loss, minor loss, static head, required endpoint pressure, and final TDH shown separately.<\/li>\n<li>Head-to-pressure conversion with named fluid density.<\/li>\n<li>Known exclusions, uncertainty, revision date, and calculation owner.<\/li>\n<\/ul>\n<div class=\"ecc-takeaway\" style=\"margin:24px 0; padding:20px 24px; background:#f5f5f5; border:1px solid #e0e0e0; border-top:3px solid #2d2d2d;\"><strong>Decision rule:<\/strong> use the simplest formula whose assumptions you can defend. A shorter input form is not a better engineering model. If the result changes the pump size or pipe size, test coefficient and diameter sensitivity before issuing the duty point.<\/div>\n<p>Send this record with your request for quotation to compare the duty point with the relevant <a href=\"https:\/\/bbpmfg.com\/centrifugal-pumps\/\" style=\"text-decoration:underline; text-underline-offset:3px;\">centrifugal pump range<\/a> or <a href=\"https:\/\/bbpmfg.com\/irrigation-pumps\/\" style=\"text-decoration:underline; text-underline-offset:3px;\">irrigation pump system<\/a>. For slurry or another specialized fluid, provide the fluid data and application details rather than substituting the clean-water examples above.<\/p>\n<h2 id=\"faq\" style=\"margin:48px 0 16px; padding-bottom:10px; border-bottom:2px solid #2d2d2d;\">Frequently Asked Questions<\/h2>\n<div style=\"margin:16px 0;\">\n<h3 style=\"margin:0 0 6px;\">How do you calculate friction loss in a pipe?<\/h3>\n<details style=\"border:1px solid #e0e0e0;\">\n<summary style=\"padding:12px 20px; cursor:pointer; background:#f5f5f5;\">Calculate velocity from flow and actual inside diameter, select a valid resistance method, then convert the resulting head loss to pressure for the stated fluid only if needed.<\/summary>\n<div style=\"padding:12px 20px 16px;\">For Darcy-Weisbach, calculate Reynolds number, select the flow-regime friction-factor method, and solve h<sub>f<\/sub> = f(L\/D)(v<sup>2<\/sup>\/2g). For turbulent water service using Hazen-Williams, state the C-factor and exact unit form. Add fittings separately, then assemble static head, pressure head, and all losses into total dynamic head. Repeat the calculation at several flows if the answer will be compared with a pump curve, because one duty point does not define the system curve. Record the coefficient source, fluid temperature, actual inside diameter, and unit set so another reviewer can reproduce the result.<\/div>\n<\/details>\n<\/div>\n<div style=\"margin:16px 0;\">\n<h3 style=\"margin:0 0 6px;\">Is friction loss measured in psi or feet of head?<\/h3>\n<details style=\"border:1px solid #e0e0e0;\">\n<summary style=\"padding:12px 20px; cursor:pointer; background:#f5f5f5;\">Friction loss can be reported as pressure drop or as feet of head, but converting between the two requires the density of the named fluid.<\/summary>\n<div style=\"padding:12px 20px 16px;\">Darcy-Weisbach commonly returns meters or feet of the flowing liquid. Pressure follows from \u0394p = \u03c1gh. For water near ordinary temperature, convenient pressure-to-head factors are often used, but they change with density. Record whether a result is psi, kPa, feet of water, or meters of the actual fluid. Keep head for the pump-system balance and convert to pressure only after the fluid density and gravitational basis are declared.<\/div>\n<\/details>\n<\/div>\n<div style=\"margin:16px 0;\">\n<h3 style=\"margin:0 0 6px;\">What is the difference between major and minor head loss?<\/h3>\n<details style=\"border:1px solid #e0e0e0;\">\n<summary style=\"padding:12px 20px; cursor:pointer; background:#f5f5f5;\">Major loss is wall friction along straight pipe; minor loss is the local resistance of fittings, valves, entrances, exits, and geometry changes within the selected system.<\/summary>\n<div style=\"padding:12px 20px 16px;\">\u201cMinor\u201d does not mean negligible. A short system with several valves or a partly open check valve can have component losses that rival straight-pipe loss. Use sourced K values or compatible equivalent lengths, identify the reference velocity, and keep component losses visible until the TDH balance is complete. Do not add the same fitting through both methods.<\/div>\n<\/details>\n<\/div>\n<div style=\"margin:16px 0;\">\n<h3 style=\"margin:0 0 6px;\">Can Hazen-Williams be used for fluids other than water?<\/h3>\n<details style=\"border:1px solid #e0e0e0;\">\n<summary style=\"padding:12px 20px; cursor:pointer; background:#f5f5f5;\">No generic Hazen-Williams C-factor should be carried into oil, slurry, concentrated solution, or non-Newtonian service because the formula omits explicit fluid-property terms during pump-system design.<\/summary>\n<div style=\"padding:12px 20px 16px;\">The formula has no explicit density or viscosity term. Use a method and fluid model that represents the actual liquid, temperature, solids, and flow behavior. Darcy-Weisbach may form part of that work, but specialized slurry and non-Newtonian calculations require more than swapping one handbook coefficient.<\/div>\n<\/details>\n<\/div>\n<div style=\"margin:16px 0;\">\n<h3 style=\"margin:0 0 6px;\">Why does actual inside diameter matter so much?<\/h3>\n<details style=\"border:1px solid #e0e0e0;\">\n<summary style=\"padding:12px 20px; cursor:pointer; background:#f5f5f5;\">Diameter changes both flow area and the length-to-diameter ratio, so a small inside-diameter error can create a much larger head-loss error at the same flow.<\/summary>\n<div style=\"padding:12px 20px 16px;\">In the same 500 gpm Darcy example, reducing actual ID by 5% raises calculated head loss by about 29%. Pipe schedule, lining, deposits, and corrosion can all move actual ID away from a nominal label. Use the manufacturer&#8217;s inside-diameter table or a measured value.<\/div>\n<\/details>\n<\/div>\n<div style=\"margin:48px 0 24px; padding:20px 24px; background:#f5f5f5; border:1px solid #e0e0e0;\">\n<h3 style=\"margin:0 0 12px;\">Calculation and Source Note<\/h3>\n<p style=\"margin:0; color:#6b7280;\">Prepared for BBP Manufacturing Co., Ltd. from the cited public technical sources. All worked-example arithmetic was independently recomputed and retained in a calculation receipt. No BBP field dataset, installed-line calibration, or third-party certification is claimed.<\/p>\n<\/div>\n<div style=\"margin:24px 0;\"><a href=\"https:\/\/bbpmfg.com\/contact-us\/\" style=\"display:inline-block; padding:14px 32px; background:#2d2d2d; color:#ffffff; font-weight:700; text-decoration:none;\">Send BBP Your Pump Duty Point \u2192<\/a><\/div>\n<div style=\"margin:48px 0 24px; padding:24px; background:#f5f5f5; border:1px solid #e0e0e0; border-top:3px solid #2d2d2d;\">\n<h3 style=\"margin:0 0 16px;\">References &amp; Sources<\/h3>\n<ol style=\"padding-left:20px; color:#6b7280;\">\n<li style=\"padding:4px 0;\"><a href=\"https:\/\/datatool.pumps.org\/fluid-flow-iii\/general\" style=\"text-decoration:underline; text-underline-offset:3px; color:#2d2d2d;\" target=\"_blank\" rel=\"noopener\">Fluid Flow: Pipe Frictional Losses<\/a> Hydraulic Institute Data Tool<\/li>\n<li style=\"padding:4px 0;\"><a href=\"https:\/\/datatool.pumps.org\/fluid-flow-iii\/fr-loss-water\" style=\"text-decoration:underline; text-underline-offset:3px; color:#2d2d2d;\" target=\"_blank\" rel=\"noopener\">Frictional Losses in Valves, Fittings, and Bends<\/a> Hydraulic Institute Data Tool<\/li>\n<li style=\"padding:4px 0;\"><a href=\"https:\/\/www.epa.gov\/water-research\/epanet\" style=\"text-decoration:underline; text-underline-offset:3px; color:#2d2d2d;\" target=\"_blank\" rel=\"noopener\">EPANET: Application for Modeling Drinking Water Distribution Systems<\/a> U.S. Environmental Protection Agency<\/li>\n<li style=\"padding:4px 0;\"><a href=\"https:\/\/www.nist.gov\/pml\/special-publication-811\/nist-guide-si-appendix-b-conversion-factors\/nist-guide-si-appendix-b8\" style=\"text-decoration:underline; text-underline-offset:3px; color:#2d2d2d;\" target=\"_blank\" rel=\"noopener\">NIST Guide to the SI, Appendix B.8<\/a> National Institute of Standards and Technology<\/li>\n<li style=\"padding:4px 0;\"><a href=\"https:\/\/irrigation.wsu.edu\/Content\/Calculators\/General\/Pipeline-Pressure-Loss.php\" style=\"text-decoration:underline; text-underline-offset:3px; color:#2d2d2d;\" target=\"_blank\" rel=\"noopener\">Pipeline Pressure Loss<\/a> Washington State University Extension<\/li>\n<li style=\"padding:4px 0;\"><a href=\"https:\/\/www.usbr.gov\/tsc\/techreferences\/mands\/wmm\/chap02_16.html\" style=\"text-decoration:underline; text-underline-offset:3px; color:#2d2d2d;\" target=\"_blank\" rel=\"noopener\">Pipe Flow Measurement<\/a> U.S. Bureau of Reclamation Water Measurement Manual<\/li>\n<li style=\"padding:4px 0;\"><a href=\"https:\/\/www.pumpsandsystems.com\/article\/how-do-i-determine-frictional-loss-flow-pipe\/\" style=\"text-decoration:underline; text-underline-offset:3px; color:#2d2d2d;\" target=\"_blank\" rel=\"noopener\">How Do I Determine the Frictional Loss for Flow in a Pipe?<\/a> Hydraulic Institute Pump FAQs, Pumps &amp; Systems<\/li>\n<li style=\"padding:4px 0;\"><a href=\"https:\/\/www.pumps.org\/2026\/04\/20\/the-hydraulic-institute-hi-data-tool-for-pump-systems\/\" style=\"text-decoration:underline; text-underline-offset:3px; color:#2d2d2d;\" target=\"_blank\" rel=\"noopener\">The Hydraulic Institute Data Tool for Pump Systems<\/a> Hydraulic Institute<\/li>\n<\/ol>\n<\/div>\n<div style=\"margin:48px 0 24px; padding:24px; background:#f5f5f5; border:1px solid #e0e0e0;\">\n<h3 style=\"margin:0 0 16px;\">Related BBP Resources<\/h3>\n<ul style=\"padding-left:20px; margin:0;\">\n<li style=\"padding:4px 0;\"><a href=\"https:\/\/bbpmfg.com\/blog\/pipe-friction-loss-calculator\/\" style=\"text-decoration:underline; text-underline-offset:3px; color:#2d2d2d;\">Pipe Friction Loss Calculator<\/a> run a quick Darcy-Weisbach calculation<\/li>\n<li style=\"padding:4px 0;\"><a href=\"https:\/\/bbpmfg.com\/irrigation-pumps\/agriculture-pump\/total-dynamic-head-tdh-calculator\/\" style=\"text-decoration:underline; text-underline-offset:3px; color:#2d2d2d;\">Total Dynamic Head Calculator<\/a> add elevation, pressure, and loss terms<\/li>\n<li style=\"padding:4px 0;\"><a href=\"https:\/\/bbpmfg.com\/blog\/pump-power-formula\/\" style=\"text-decoration:underline; text-underline-offset:3px; color:#2d2d2d;\">Pump Power Formula<\/a> convert flow and head into hydraulic and shaft power<\/li>\n<\/ul>\n<\/div>\n<\/div>\n","protected":false},"excerpt":{"rendered":"<p>Updated August 2026 A friction loss formula is a calculation that converts resistance inside a pipe into head loss or pressure drop. For ordinary water service, the two formulas you will see most often are Darcy-Weisbach and Hazen-Williams. Darcy-Weisbach starts from velocity, pipe geometry, viscosity, and roughness. Hazen-Williams replaces those fluid and surface terms with [&hellip;]<\/p>\n","protected":false},"author":1,"featured_media":6549,"comment_status":"open","ping_status":"open","sticky":false,"template":"","format":"standard","meta":{"_gspb_post_css":"","footnotes":""},"categories":[1],"tags":[],"class_list":["post-6559","post","type-post","status-publish","format-standard","has-post-thumbnail","hentry","category-bbp-blogs"],"blocksy_meta":{"styles_descriptor":{"styles":{"desktop":"","tablet":"","mobile":""},"google_fonts":[],"version":8}},"_links":{"self":[{"href":"https:\/\/bbpmfg.com\/ar\/wp-json\/wp\/v2\/posts\/6559","targetHints":{"allow":["GET"]}}],"collection":[{"href":"https:\/\/bbpmfg.com\/ar\/wp-json\/wp\/v2\/posts"}],"about":[{"href":"https:\/\/bbpmfg.com\/ar\/wp-json\/wp\/v2\/types\/post"}],"author":[{"embeddable":true,"href":"https:\/\/bbpmfg.com\/ar\/wp-json\/wp\/v2\/users\/1"}],"replies":[{"embeddable":true,"href":"https:\/\/bbpmfg.com\/ar\/wp-json\/wp\/v2\/comments?post=6559"}],"version-history":[{"count":0,"href":"https:\/\/bbpmfg.com\/ar\/wp-json\/wp\/v2\/posts\/6559\/revisions"}],"wp:featuredmedia":[{"embeddable":true,"href":"https:\/\/bbpmfg.com\/ar\/wp-json\/wp\/v2\/media\/6549"}],"wp:attachment":[{"href":"https:\/\/bbpmfg.com\/ar\/wp-json\/wp\/v2\/media?parent=6559"}],"wp:term":[{"taxonomy":"category","embeddable":true,"href":"https:\/\/bbpmfg.com\/ar\/wp-json\/wp\/v2\/categories?post=6559"},{"taxonomy":"post_tag","embeddable":true,"href":"https:\/\/bbpmfg.com\/ar\/wp-json\/wp\/v2\/tags?post=6559"}],"curies":[{"name":"wp","href":"https:\/\/api.w.org\/{rel}","templated":true}]}}