{"id":100185,"date":"2026-02-15T20:25:38","date_gmt":"2026-02-15T20:25:38","guid":{"rendered":"https:\/\/vibromera.eu\/?post_type=calculator&#038;p=100185"},"modified":"2026-07-13T02:37:55","modified_gmt":"2026-07-13T02:37:55","slug":"pipe-pressure-drop","status":"publish","type":"calculator","link":"https:\/\/vibromera.eu\/fi\/calculators\/pipe-pressure-drop\/","title":{"rendered":"Source-Gated Darcy\u2013Weisbach Loss Arithmetic"},"content":{"rendered":"\n<!-- NEEDS_LICENSED_SOURCE: exact closed code\/project friction-factor or K tables must be supplied by the user; none is guessed. -->\n<script type=\"application\/ld+json\">{\"@context\":\"https:\/\/schema.org\",\"@type\":\"WebApplication\",\"name\":\"Source-Gated Darcy\u2013Weisbach Loss Arithmetic\",\"description\":\"Calculates straight-pipe and documented-K dissipative pressure losses using either a documented Darcy friction factor or a verified fully developed laminar route. It does not interpolate transition flow or invent material roughness and fitting coefficients.\",\"url\":\"https:\/\/vibromera.eu\/calculators\/pipe-pressure-drop\/\",\"applicationCategory\":\"EngineeringApplication\",\"operatingSystem\":\"Any (Web Browser)\",\"offers\":{\"@type\":\"Offer\",\"price\":\"0\",\"priceCurrency\":\"EUR\"},\"creator\":{\"@type\":\"Organization\",\"name\":\"Vibromera\",\"url\":\"https:\/\/vibromera.eu\/\"},\"datePublished\":\"2024-01-01\",\"dateModified\":\"2026-07-13\",\"inLanguage\":\"en\",\"isAccessibleForFree\":true,\"featureList\":[\"Documented Darcy-factor route\",\"Verified laminar 64\/Re route\",\"Documented summed-K losses\",\"Exact SI and US conversions\",\"No transition interpolation\"],\"keywords\":\"Darcy Weisbach pressure loss,Darcy friction factor,laminar pipe loss,loss coefficient K\"}<\/script>\n<script type=\"application\/ld+json\">{\"@context\":\"https:\/\/schema.org\",\"@type\":\"FAQPage\",\"mainEntity\":[{\"@type\":\"Question\",\"name\":\"Does this calculate a turbulent friction factor from pipe material?\",\"acceptedAnswer\":{\"@type\":\"Answer\",\"text\":\"No. For non-laminar work, enter a Darcy friction factor from a controlled applicable source or calculation.\"}},{\"@type\":\"Question\",\"name\":\"What happens in the transition range?\",\"acceptedAnswer\":{\"@type\":\"Answer\",\"text\":\"No friction factor is interpolated. Use a documented factor and project procedure; transition is disturbance-dependent.\"}},{\"@type\":\"Question\",\"name\":\"Are fitting K values built in?\",\"acceptedAnswer\":{\"@type\":\"Answer\",\"text\":\"No. Enter a documented summed loss coefficient referenced to the same mean velocity, or leave it zero.\"}},{\"@type\":\"Question\",\"name\":\"Is this total system pressure drop or pump head?\",\"acceptedAnswer\":{\"@type\":\"Answer\",\"text\":\"No. It reports only the entered straight-pipe friction and documented-K dissipative terms; elevation, acceleration, equipment and other effects are excluded.\"}}]}<\/script>\n<style>:root{--s:#fff;--sa:#f8f6f2;--i:#1a1a1a;--is:#5a5650;--im:#8a857e;--a:#2a5c8c;--al:#eaf1f8;--b:#d9d4cc;--bl:#e8e4dd;--y:#8a6500;--yl:#fef9e8;--r:#a12b2b;--f:'DM Sans',sans-serif;--m:'JetBrains Mono',monospace;--d:'Fraunces',serif}.vc-calculator{font-family:var(--f);font-size:15px;line-height:1.65;color:var(--i);max-width:960px;margin:auto;padding:20px 16px 40px}.vc-calculator *{box-sizing:border-box}.vc-header{text-align:center;padding:48px 20px 40px;border-bottom:3px solid var(--a)}.vc-header-eyebrow{font:500 11px var(--m);letter-spacing:.15em;text-transform:uppercase;color:var(--a)}.vc-header-title{font:800 clamp(24px,4vw,36px)\/1.15 var(--d);margin:10px 0 14px}.vc-header-subtitle{max-width:780px;margin:auto;color:var(--is)}.vc-badges{display:flex;gap:8px;justify-content:center;flex-wrap:wrap;margin-top:18px}.vc-badge{font:500 11px var(--m);padding:4px 10px;border:1px solid var(--b);border-radius:4px}.vc-card,.vc-section{background:var(--s);border:1px solid var(--b);border-radius:12px;overflow:hidden;margin-top:28px}.vc-form{padding:24px}.vc-grid{display:grid;grid-template-columns:1fr 1fr;gap:18px}.vc-field{display:flex;flex-direction:column}.vc-full{grid-column:1\/-1}.vc-hidden{display:none!important}.vc-label{font-size:12px;font-weight:600;letter-spacing:.04em;text-transform:uppercase;color:var(--is);margin-bottom:6px}.vc-hint{font-weight:400;text-transform:none;letter-spacing:0;color:var(--im)}.vc-input,.vc-select{width:100%;padding:10px 12px;border:1.5px solid var(--b);border-radius:6px;font:14px var(--f);background:var(--s)}.vc-check{display:flex;gap:10px;padding:12px;border:1px solid var(--bl);border-radius:6px;background:var(--sa);font-size:13px;color:var(--is)}.vc-check input{margin-top:4px}.vc-validation{min-height:22px;color:var(--r);font-size:13px;margin-top:10px}.vc-results{border-top:1px solid var(--bl);background:var(--sa);padding:0;max-height:0;overflow:hidden}.vc-results.vc-visible{max-height:1600px;padding:24px}.vc-result-grid{display:grid;grid-template-columns:repeat(2,1fr);gap:12px}.vc-rcard{background:var(--s);border:1px solid var(--bl);border-radius:8px;padding:16px}.vc-primary{grid-column:1\/-1;border:2px solid var(--a);background:var(--al)}.vc-rcard-label{font:500 10px var(--m);letter-spacing:.1em;text-transform:uppercase;color:var(--im)}.vc-rcard-value{font:600 19px var(--m);overflow-wrap:anywhere}.vc-primary .vc-rcard-value{font-size:24px;color:var(--a)}.vc-status{grid-column:1\/-1;padding:12px;background:var(--yl);border-left:3px solid var(--y);font-size:13px;color:var(--is)}.vc-section-toggle{width:100%;display:flex;justify-content:space-between;padding:18px 24px;border:0;background:transparent;cursor:pointer;text-align:left}.vc-section-title{font:700 18px var(--d)}.vc-section-body{max-height:0;overflow:hidden}.vc-section.vc-open .vc-section-body{max-height:15000px}.vc-section-inner{padding:0 24px 24px;border-top:1px solid var(--bl)}.vc-theory h3{font:700 17px var(--d);margin:24px 0 8px}.vc-theory p,.vc-theory li{font-size:14px;color:var(--is)}.vc-formula{padding:14px;border:2px solid var(--b);border-radius:6px;background:var(--sa);text-align:center;font:500 14px var(--m);margin:12px 0}.vc-warning{padding:14px;background:var(--yl);border-left:3px solid var(--y);color:var(--is)}.vc-faq-item{border:1px solid var(--bl);margin-top:8px}.vc-faq-q{width:100%;padding:14px;border:0;background:var(--sa);text-align:left;font-weight:600}.vc-faq-a{display:none;padding:14px;color:var(--is)}.vc-faq-item.vc-open .vc-faq-a{display:block}.vc-footer{text-align:center;padding:30px;color:var(--im);font-size:13px}@media(max-width:600px){.vc-grid,.vc-result-grid{grid-template-columns:1fr}.vc-full,.vc-primary,.vc-status{grid-column:1}}<\/style>\n<div class=\"vc-calculator\"><header class=\"vc-header\"><p class=\"vc-header-eyebrow\">Controlled loss coefficients \u2014 no transition interpolation<\/p><h1 class=\"vc-header-title\">Source-Gated Darcy\u2013Weisbach Loss Arithmetic<\/h1><p class=\"vc-header-subtitle\">Calculate dissipative loss for one constant-ID straight length plus an optional documented summed K. Supply a controlled Darcy factor,or use the narrow verified fully developed laminar route.<\/p><div class=\"vc-badges\"><span class=\"vc-badge\">Darcy f explicitly<\/span><span class=\"vc-badge\">No roughness presets<\/span><span class=\"vc-badge\">No K presets<\/span><\/div><\/header><div class=\"vc-card\"><form class=\"vc-form\" id=\"vc-form\" autocomplete=\"off\" novalidate><div class=\"vc-grid\"><div class=\"vc-field vc-full\"><label class=\"vc-label\" for=\"vc-mode\">Friction-factor basis<\/label><select class=\"vc-select\" id=\"vc-mode\"><option value=\"documented\">Documented Darcy friction factor fD<\/option><option value=\"laminar\">Verified fully developed laminar circular flow: fD=64\/ReD<\/option><\/select><\/div><div class=\"vc-field\"><label class=\"vc-label\" for=\"vc-flow\">Actual volumetric flow Q<\/label><input class=\"vc-input\" id=\"vc-flow\" inputmode=\"decimal\"><\/div><div class=\"vc-field\"><label class=\"vc-label\" for=\"vc-flow-unit\">Flow unit<\/label><select class=\"vc-select\" id=\"vc-flow-unit\"><option value=\"m3s\">m\u00b3\/s<\/option><option value=\"m3h\">m\u00b3\/h<\/option><option value=\"lmin\">L\/min<\/option><option value=\"usgpm\">US gal\/min<\/option><\/select><\/div><div class=\"vc-field\"><label class=\"vc-label\" for=\"vc-diameter\">Actual constant internal diameter D<\/label><input class=\"vc-input\" id=\"vc-diameter\" inputmode=\"decimal\"><\/div><div class=\"vc-field\"><label class=\"vc-label\" for=\"vc-diameter-unit\">Diameter unit<\/label><select class=\"vc-select\" id=\"vc-diameter-unit\"><option value=\"mm\">mm<\/option><option value=\"in\">in<\/option><\/select><\/div><div class=\"vc-field\"><label class=\"vc-label\" for=\"vc-length\">Straight constant-ID length L<\/label><input class=\"vc-input\" id=\"vc-length\" inputmode=\"decimal\"><\/div><div class=\"vc-field\"><label class=\"vc-label\" for=\"vc-length-unit\">Length unit<\/label><select class=\"vc-select\" id=\"vc-length-unit\"><option value=\"m\">m<\/option><option value=\"ft\">ft<\/option><\/select><\/div><div class=\"vc-field\"><label class=\"vc-label\" for=\"vc-density\">Same-state density \u03c1<\/label><input class=\"vc-input\" id=\"vc-density\" inputmode=\"decimal\"><\/div><div class=\"vc-field\"><label class=\"vc-label\" for=\"vc-density-unit\">Density unit<\/label><select class=\"vc-select\" id=\"vc-density-unit\"><option value=\"kgm3\">kg\/m\u00b3<\/option><option value=\"lbft3\">lb\/ft\u00b3<\/option><\/select><\/div><div class=\"vc-field\" id=\"vc-f-field\"><label class=\"vc-label\" for=\"vc-f\">Documented Darcy friction factor fD<\/label><input class=\"vc-input\" id=\"vc-f\" inputmode=\"decimal\"><\/div><div class=\"vc-field vc-hidden\" id=\"vc-nu-field\"><label class=\"vc-label\" for=\"vc-nu\">Same-state kinematic viscosity \u03bd<\/label><input class=\"vc-input\" id=\"vc-nu\" inputmode=\"decimal\"><\/div><div class=\"vc-field vc-hidden\" id=\"vc-nu-unit-field\"><label class=\"vc-label\" for=\"vc-nu-unit\">Viscosity unit<\/label><select class=\"vc-select\" id=\"vc-nu-unit\"><option value=\"mm2s\">mm\u00b2\/s = cSt<\/option><option value=\"m2s\">m\u00b2\/s<\/option><option value=\"ft2s\">ft\u00b2\/s<\/option><\/select><\/div><div class=\"vc-field\"><label class=\"vc-label\" for=\"vc-k\">Documented summed loss coefficient \u03a3K <span class=\"vc-hint\">(blank=0)<\/span><\/label><input class=\"vc-input\" id=\"vc-k\" inputmode=\"decimal\"><\/div><div class=\"vc-field vc-full\"><label class=\"vc-label\" for=\"vc-source\">Section,state,f\/K or laminar evidence source<\/label><input class=\"vc-input\" id=\"vc-source\" type=\"text\" placeholder=\"end planes;fluid\/state;Q,D,L,rho sources;Darcy-f method and conditions or laminar evidence;K definitions\/reference velocity;revision\/date\"><\/div><div class=\"vc-field vc-full\"><label class=\"vc-check\" for=\"vc-gate\"><input id=\"vc-gate\" type=\"checkbox\"><span>All inputs describe the same steady single-phase Newtonian state and constant full circular ID.The result is dissipative straight-pipe plus entered-K loss between documented planes.Entered f is the Darcy\u2014not Fanning\u2014factor and is applicable to this Re,relative roughness and state;or the laminar route has controlled fully developed laminar evidence.Each K uses this same mean-velocity reference.Elevation,acceleration,equipment and other terms are separate.<\/span><\/label><\/div><\/div><div class=\"vc-validation\" id=\"vc-validation\" role=\"status\" aria-live=\"polite\"><\/div><\/form><div class=\"vc-results\" id=\"vc-results\"><div class=\"vc-result-grid\"><div class=\"vc-rcard vc-primary\"><div class=\"vc-rcard-label\">Entered-model dissipative pressure loss<\/div><div class=\"vc-rcard-value\" id=\"vc-r-total\">\u2014<\/div><\/div><div class=\"vc-rcard\"><div class=\"vc-rcard-label\">Straight-pipe friction term<\/div><div class=\"vc-rcard-value\" id=\"vc-r-major\">\u2014<\/div><\/div><div class=\"vc-rcard\"><div class=\"vc-rcard-label\">Documented-K term<\/div><div class=\"vc-rcard-value\" id=\"vc-r-minor\">\u2014<\/div><\/div><div class=\"vc-rcard\"><div class=\"vc-rcard-label\">Mean velocity<\/div><div class=\"vc-rcard-value\" id=\"vc-r-v\">\u2014<\/div><\/div><div class=\"vc-rcard\"><div class=\"vc-rcard-label\">Darcy factor \/ Reynolds basis<\/div><div class=\"vc-rcard-value\" id=\"vc-r-basis\">\u2014<\/div><\/div><div class=\"vc-status\" id=\"vc-r-note\">Partial-system dissipative loss only.<\/div><\/div><\/div><\/div>\n<div class=\"vc-section vc-open\"><button class=\"vc-section-toggle\" type=\"button\" aria-expanded=\"true\"><span class=\"vc-section-title\">Equations and boundaries<\/span><span>\u2304<\/span><\/button><div class=\"vc-section-body\"><div class=\"vc-section-inner vc-theory\"><div class=\"vc-formula\">v\u0304=4Q\/(\u03c0D\u00b2); \u0394pmajor=fD(L\/D)(\u03c1v\u0304\u00b2\/2); \u0394pK=\u03a3K(\u03c1v\u0304\u00b2\/2); \u0394ploss=\u0394pmajor+\u0394pK<\/div><p>fD is the Darcy friction factor,not the Fanning factor.\u03a3K is dimensionless and must be referenced to the same mean velocity.The equations return positive dissipative loss magnitude,not a signed static-pressure difference or a complete energy equation.<\/p><h3>Laminar route<\/h3><div class=\"vc-formula\">ReD=v\u0304D\/\u03bd;&nbsp; fD=64\/ReD<\/div><p>The 64\/ReD route is restricted to controlled fully developed laminar Newtonian flow in a full straight circular pipe and is rejected at or above the conventional ReD=2300 screen.Roughness does not enter that theoretical relation.<\/p><h3>No transition model<\/h3><p>No linear interpolation between laminar and turbulent friction factors is used.Transition is disturbance-dependent.For turbulent or transition work,supply fD from a documented method whose inputs,range and conventions match the assessed state.<\/p><div class=\"vc-warning\"><strong>Not calculated:<\/strong> material-based roughness,Colebrook\/Moody selection,fitting K values,pipe sizing,acceptable loss,pump duty,elevation,acceleration,compressibility,two-phase flow,heat transfer,water hammer or cavitation.<\/div><h3>Sources<\/h3><p><a href=\"https:\/\/www2.latech.edu\/~hhegab\/pages\/me354\/Lab3\/Lab3_minorlosses_Sp97.htm\" target=\"_blank\" rel=\"noopener\">Louisiana Tech Darcy\u2013Weisbach and empirical K-factor scope<\/a>; <a href=\"https:\/\/eaglepubs.erau.edu\/introductiontoaerospaceflightvehicles\/chapter\/internal-flows\/\" target=\"_blank\" rel=\"noopener\">ERAU fully developed laminar 64\/Re relation<\/a>; <a href=\"https:\/\/www.princeton.edu\/~asmits\/Bicycle_web\/pictures\/transition.html\" target=\"_blank\" rel=\"noopener\">Princeton disturbance-dependent transition<\/a>; <a href=\"https:\/\/www.nist.gov\/pml\/special-publication-811\/nist-guide-si-appendix-b-conversion-factors\" target=\"_blank\" rel=\"noopener\">NIST conversion factors<\/a>.<\/p><\/div><\/div><\/div><div class=\"vc-section\"><button class=\"vc-section-toggle\" type=\"button\" aria-expanded=\"false\"><span class=\"vc-section-title\">Frequently asked questions<\/span><span>\u2304<\/span><\/button><div class=\"vc-section-body\"><div class=\"vc-section-inner\"><div id=\"vc-faq-list\"><\/div><\/div><\/div><\/div><footer class=\"vc-footer\">\u00a9 2024\u20132026 Vibromera \u2014 reviewed 13 July 2026<\/footer><\/div>\n<script>(function(){'use strict';function $(id){return document.getElementById(id)}function token(raw){var t=String(raw||'').trim();if(!t||(t.includes(',')&&t.includes('.')))return null;t=t.replace(',','.');if(!\/^(?:\\d+(?:\\.\\d*)?|\\.\\d+)$\/.test(t))return null;var v=Number(t);return Number.isFinite(v)?v:null}function pos(raw){var v=token(raw);return v!==null&&v>0?v:null}function nonneg(raw,blankZero){var t=String(raw||'').trim();if(!t&&blankZero)return 0;var v=token(t);return v!==null&&v>=0?v:null}function fmt(v){if(v===0)return'0';if(Math.abs(v)>=1e9||Math.abs(v)<1e-6)return v.toExponential(8);return Number(v.toPrecision(11)).toString()}function qSI(v,u){return v*({m3s:1,m3h:1\/3600,lmin:.001\/60,usgpm:.003785411784\/60})[u]}function dSI(v,u){return v*(u==='in'?.0254:.001)}function lSI(v,u){return v*(u==='ft'?.3048:1)}function rhoSI(v,u){return v*(u==='lbft3'?.45359237\/.028316846592:1)}function nuSI(v,u){return v*({mm2s:1e-6,m2s:1,ft2s:.09290304})[u]}function hide(m){$('vc-results').classList.remove('vc-visible');$('vc-validation').textContent=m||''}function setMode(){var lam=$('vc-mode').value==='laminar';$('vc-f-field').classList.toggle('vc-hidden',lam);$('vc-nu-field').classList.toggle('vc-hidden',!lam);$('vc-nu-unit-field').classList.toggle('vc-hidden',!lam);calc()}function pressure(v){return fmt(v)+' Pa | '+fmt(v\/1000)+' kPa | '+fmt(v\/1e5)+' bar | '+fmt(v\/6894.757293168)+' psi'}function calc(){if(!$('vc-source').value.trim())return hide('Enter the controlled section,state and coefficient evidence source.');if(!$('vc-gate').checked)return hide('Confirm the Darcy-factor\/K conventions and model boundaries.');var qr=pos($('vc-flow').value),dr=pos($('vc-diameter').value),lr=nonneg($('vc-length').value,false),rr=pos($('vc-density').value),K=nonneg($('vc-k').value,true);if(qr===null||dr===null||lr===null||rr===null||K===null)return hide('Enter positive Q,D,rho and non-negative complete L and summed K values.');var Q=qSI(qr,$('vc-flow-unit').value),D=dSI(dr,$('vc-diameter-unit').value),L=lSI(lr,$('vc-length-unit').value),rho=rhoSI(rr,$('vc-density-unit').value),A=Math.PI*D*D\/4,v=Q\/A,f,Re=null,basis;if($('vc-mode').value==='laminar'){var nr=pos($('vc-nu').value);if(nr===null)return hide('Enter positive same-state kinematic viscosity for the laminar route.');var nu=nuSI(nr,$('vc-nu-unit').value);Re=v*D\/nu;if(!(Re<2300-1e-9))return hide('Laminar 64\/Re route is suppressed at or above the conventional ReD=2300 screen.Use a documented Darcy factor and controlled procedure.');f=64\/Re;basis='fD='+fmt(f)+' from64\/ReD; ReD='+fmt(Re)}else{f=pos($('vc-f').value);if(f===null)return hide('Enter a positive documented Darcy friction factor.');basis='documented Darcy fD='+fmt(f)+'; ReD not inferred'}var dynamic=rho*v*v\/2,major=f*(L\/D)*dynamic,minor=K*dynamic,total=major+minor;if(![Q,D,L,rho,A,v,f,dynamic,major,minor,total].every(Number.isFinite)||[major,minor,total].some(function(x){return x<0}))return hide('The arithmetic did not produce finite non-negative losses.');$('vc-r-total').textContent=pressure(total);$('vc-r-major').textContent=pressure(major);$('vc-r-minor').textContent=pressure(minor);$('vc-r-v').textContent=fmt(v)+' m\/s | '+fmt(v\/.3048)+' ft\/s';$('vc-r-basis').textContent=basis+'; \u03a3K='+fmt(K);$('vc-r-note').textContent='Positive dissipative loss magnitude for only the entered straight length and documented-K terms.No static elevation,acceleration,equipment,pump or acceptance conclusion is included.';$('vc-validation').textContent='';$('vc-results').classList.add('vc-visible')}$('vc-form').addEventListener('input',calc);$('vc-form').addEventListener('change',function(e){if(e.target===$('vc-mode'))setMode();else calc()});document.querySelectorAll('.vc-section-toggle').forEach(function(b){b.addEventListener('click',function(){var s=this.closest('.vc-section');s.classList.toggle('vc-open');this.setAttribute('aria-expanded',String(s.classList.contains('vc-open')))})});var faq=[['Why not choose roughness from a material name?','Actual roughness depends on product,condition,age,deposits and the friction-factor method.Use a controlled applicable fD instead.'],['Can I use a Fanning factor?','No.The displayed Darcy\u2013Weisbach form requires Darcy fD;Fanning and Darcy factors differ by four.'],['Can I add catalog K values?','Only when the source geometry,Reynolds range and reference velocity match.Sum those controlled coefficients before entry.'],['Does zero length work?','Yes.With L=0 the major term is zero and a documented K term can still be evaluated;with both L and K zero the modeled loss is zero.']];var list=$('vc-faq-list');faq.forEach(function(x){var w=document.createElement('div');w.className='vc-faq-item';var b=document.createElement('button');b.type='button';b.className='vc-faq-q';b.textContent=x[0];var a=document.createElement('div');a.className='vc-faq-a';a.textContent=x[1];w.appendChild(b);w.appendChild(a);list.appendChild(w)});list.addEventListener('click',function(e){var b=e.target.closest('.vc-faq-q');if(b)b.closest('.vc-faq-item').classList.toggle('vc-open')});setMode()})();<\/script>\n","protected":false},"excerpt":{"rendered":"<p>Calculate straight-pipe and documented-K dissipative loss using a controlled Darcy factor or verified laminar 64\/Re route,without transition interpolation or coefficient presets.<\/p>","protected":false},"featured_media":0,"template":"","meta":{"ai_generated_summary":"","footnotes":""},"categories":[],"tags":[],"class_list":["post-100185","calculator","type-calculator","status-publish","hentry"],"_links":{"self":[{"href":"https:\/\/vibromera.eu\/fi\/wp-json\/wp\/v2\/calculator\/100185","targetHints":{"allow":["GET"]}}],"collection":[{"href":"https:\/\/vibromera.eu\/fi\/wp-json\/wp\/v2\/calculator"}],"about":[{"href":"https:\/\/vibromera.eu\/fi\/wp-json\/wp\/v2\/types\/calculator"}],"version-history":[{"count":3,"href":"https:\/\/vibromera.eu\/fi\/wp-json\/wp\/v2\/calculator\/100185\/revisions"}],"predecessor-version":[{"id":102523,"href":"https:\/\/vibromera.eu\/fi\/wp-json\/wp\/v2\/calculator\/100185\/revisions\/102523"}],"wp:attachment":[{"href":"https:\/\/vibromera.eu\/fi\/wp-json\/wp\/v2\/media?parent=100185"}],"wp:term":[{"taxonomy":"category","embeddable":true,"href":"https:\/\/vibromera.eu\/fi\/wp-json\/wp\/v2\/categories?post=100185"},{"taxonomy":"post_tag","embeddable":true,"href":"https:\/\/vibromera.eu\/fi\/wp-json\/wp\/v2\/tags?post=100185"}],"curies":[{"name":"wp","href":"https:\/\/api.w.org\/{rel}","templated":true}]}}