Calculations based on Darcy-Weisbach equation for pressure drop and empirical correlations for friction factor (e.g., Colebrook-White or explicit approximations). Flow rate is derived from pressure drop and pipe characteristics.
Assumptions: Steady, incompressible, single-phase flow. Inlet and outlet pressures are absolute or gauge as per input. Unit consistency is crucial.
Flow Rate vs. Pressure Drop
Visualizing the relationship between flow rate and pressure drop under constant pipe conditions.
Reynolds Number vs. Friction Factor
Illustrating the influence of Reynolds number on the friction factor for different relative roughness values.
What is Flow Through Pipe?
Flow through pipe refers to the movement of fluids (liquids or gases) within enclosed conduits like pipes, tubes, or channels. This fundamental concept in fluid dynamics is critical across a vast spectrum of engineering disciplines, including civil, mechanical, chemical, and petroleum engineering. Understanding how fluids behave under various conditions within a pipe system allows engineers to design efficient and safe fluid transport networks, predict system performance, and troubleshoot operational issues. Essentially, any system involving the movement of fluids from one point to another via a pipe is an example of flow through pipe.
Who should use a flow through pipe calculator? This calculator is invaluable for:
Engineers (Mechanical, Chemical, Civil, Environmental): Designing piping systems for water, oil, gas, steam, or other fluids.
Plumbers and HVAC Technicians: Sizing pipes for water supply, drainage, or HVAC systems.
Process Designers: Optimizing fluid transfer in manufacturing and chemical plants.
Students and Educators: Learning and demonstrating principles of fluid mechanics.
Homeowners: Estimating water pressure and flow rates for domestic plumbing.
Common Misconceptions:
Pressure Drop Equals Flow Rate: While related, pressure drop is the *resistance* to flow, not the flow rate itself. You need to know pipe properties and fluid characteristics to link them.
Frictionless Flow: In reality, all fluid flow involves some friction, leading to energy loss and pressure drop. Assuming zero friction is only valid for highly idealized scenarios.
Constant Friction Factor: The friction factor is not constant; it depends significantly on the flow regime (laminar vs. turbulent), characterized by the Reynolds number, and the pipe's relative roughness.
Flow Through Pipe Formula and Mathematical Explanation
Calculating flow through pipes typically involves understanding the relationship between pressure drop, flow rate, pipe geometry, and fluid properties. The most widely used equation for pressure drop due to friction in turbulent flow is the Darcy-Weisbach equation.
The Darcy-Weisbach Equation
The Darcy-Weisbach equation relates the head loss (pressure drop) in a pipe to the flow velocity, pipe dimensions, fluid properties, and a dimensionless friction factor.
$$ h_f = f \frac{L}{D} \frac{v^2}{2g} $$
Where:
$h_f$ = Head loss due to friction (in meters or feet)
$f$ = Darcy friction factor (dimensionless)
$L$ = Equivalent length of the pipe (in meters or feet)
$D$ = Inner diameter of the pipe (in meters or feet)
$v$ = Average flow velocity (in m/s or ft/s)
$g$ = Acceleration due to gravity (approx. 9.81 m/s² or 32.2 ft/s²)
To convert head loss ($h_f$) to pressure drop ($\Delta P$), we use the relationship:
$$ \Delta P = \rho g h_f = f \frac{L}{D} \frac{\rho v^2}{2} $$
Where:
$\Delta P$ = Pressure drop (in Pascals or psi)
$\rho$ = Fluid density (in kg/m³ or lb/ft³)
Determining the Friction Factor ($f$)
The friction factor ($f$) is the most challenging parameter to determine, as it depends on the flow regime and pipe roughness.
Reynolds Number (Re): This dimensionless number indicates the flow regime.
$$ Re = \frac{\rho v D}{\mu} $$
Where $\mu$ is the dynamic viscosity of the fluid.
Flow Regimes:
Laminar Flow ($Re < 2300$): $f = \frac{64}{Re}$
Turbulent Flow ($Re > 4000$): The friction factor depends on both Re and relative roughness ($\epsilon/D$), where $\epsilon$ is the absolute roughness. The Colebrook-White equation is the standard for turbulent flow, but it's implicit and requires iteration:
$$ \frac{1}{\sqrt{f}} = -2.0 \log_{10} \left( \frac{\epsilon/D}{3.7} + \frac{2.51}{Re\sqrt{f}} \right) $$
For practical calculations, explicit approximations like the Swamee-Jain equation are often used:
$$ f = \frac{0.25}{\left[ \log_{10} \left( \frac{\epsilon/D}{3.7} + \frac{5.74}{Re^{0.9}} \right) \right]^2} $$
Transitional Flow ($2300 < Re < 4000$): This region is complex and often avoided in design. Interpolation or specialized correlations are used.
Calculating Flow Rate ($Q$)
Once the pressure drop ($\Delta P$) is known or calculated, the flow rate ($Q$) can be determined using the relationship between velocity and flow rate:
$$ Q = A \times v = \frac{\pi D^2}{4} \times v $$
Where:
$Q$ = Volumetric flow rate (in m³/s or ft³/s)
$A$ = Cross-sectional area of the pipe (in m² or ft²)
Our calculator uses these principles, solving iteratively or using approximations to find the friction factor and then calculating the flow rate based on specified pressure differences or vice versa.
Variables Table
Variable
Meaning
Unit (SI)
Unit (Imperial)
Typical Range
$Q$
Volumetric Flow Rate
m³/s
ft³/s (or gpm, cfs)
Variable
$\Delta P$
Pressure Drop
Pa
psi
Variable
$v$
Average Flow Velocity
m/s
ft/s
0.1 – 10 m/s (typical)
$D$
Pipe Inner Diameter
m
in, ft
0.01 – 2 m (typical)
$L$
Pipe Length
m
ft
1 – 1000 m (typical)
$\rho$
Fluid Density
kg/m³
lb/ft³
Water: ~1000 kg/m³; Air: ~1.2 kg/m³
$\mu$
Fluid Dynamic Viscosity
Pa·s
cP
Water: ~1×10⁻³ Pa·s; Air: ~1.8×10⁻⁵ Pa·s
$\epsilon$
Absolute Roughness
m
ft, mm
1.5×10⁻⁶ m (smooth plastic) – 0.00015 m (cast iron)
$Re$
Reynolds Number
Dimensionless
Dimensionless
0 – 106+
$f$
Darcy Friction Factor
Dimensionless
Dimensionless
0.008 – 0.1
Practical Examples (Real-World Use Cases)
Let's illustrate the calculator's use with practical scenarios. We'll assume SI units for consistency in the explanation, but the calculator handles various units.
Example 1: Water Supply to a Building
A building requires a certain water flow rate. Engineers need to determine the pressure drop in a proposed supply pipe to ensure adequate pressure at the highest point.
Scenario: Pumping water (Density $\rho = 1000 \, kg/m^3$, Dynamic Viscosity $\mu = 1 \times 10^{-3} \, Pa \cdot s$) through a 100-meter long pipe with an inner diameter ($D$) of 0.05 m (50 mm). The pipe material is commercial steel with an absolute roughness ($\epsilon$) of $4.5 \times 10^{-5}$ m. The desired flow rate ($Q$) is 0.01 m³/s.
Goal: Calculate the pressure drop ($\Delta P$).
Inputs for Calculator:
Pipe Inner Diameter: 0.05 m
Pipe Length: 100 m
Fluid Dynamic Viscosity: 0.001 Pa·s
Fluid Density: 1000 kg/m³
Pipe Absolute Roughness: 0.000045 m (Note: Since we are calculating pressure drop from flow rate, we'd conceptually set an inlet/outlet pressure difference or infer it.)
Let's assume we input a flow rate (e.g. 0.01 m³/s) and calculate the pressure drop. The calculator might work inversely or require pressure inputs to find flow. For demonstration, let's *use the calculator to find flow based on a known pressure difference*.
Revised Scenario Inputs (to find Flow):
Pipe Inner Diameter: 0.05 m
Pipe Length: 100 m
Fluid Dynamic Viscosity: 0.001 Pa·s
Fluid Density: 1000 kg/m³
Pipe Absolute Roughness: 0.000045 m
Inlet Pressure: 500,000 Pa (5 bar)
Outlet Pressure: 300,000 Pa (3 bar)
Calculator Output (Illustrative):
Pressure Drop: 200,000 Pa (calculated, matches input difference)
Flow Rate: ~0.012 m³/s (12 liters/second)
Reynolds Number: ~600,000 (Turbulent Flow)
Friction Factor: ~0.023
Interpretation: With a 200,000 Pa pressure difference available, the system can deliver approximately 12 liters per second. If this flow rate is insufficient, engineers might need a larger diameter pipe, higher pump pressure, or a smoother pipe material. This calculation is crucial for pipe sizing.
Example 2: Natural Gas Pipeline
Transporting natural gas over long distances requires careful pressure and flow management.
Scenario: Transporting natural gas (Density $\rho \approx 0.7 \, kg/m^3$, Dynamic Viscosity $\mu \approx 1.8 \times 10^{-5} \, Pa \cdot s$) through a 5 km (5000 m) pipeline with an inner diameter ($D$) of 0.3 m. The pipe is welded steel with an absolute roughness ($\epsilon$) of $0.000045$ m. The inlet pressure ($P_{in}$) is 5 MPa (5,000,000 Pa), and the desired outlet pressure ($P_{out}$) is 4 MPa (4,000,000 Pa).
Goal: Calculate the resulting flow rate ($Q$).
Inputs for Calculator:
Pipe Inner Diameter: 0.3 m
Pipe Length: 5000 m
Fluid Dynamic Viscosity: 0.000018 Pa·s
Fluid Density: 0.7 kg/m³
Pipe Absolute Roughness: 0.000045 m
Inlet Pressure: 5,000,000 Pa
Outlet Pressure: 4,000,000 Pa
Calculator Output (Illustrative):
Pressure Drop: 1,000,000 Pa (1 MPa)
Flow Rate: ~0.95 m³/s (equivalent to ~2000 standard cubic feet per minute)
Reynolds Number: ~7.9 x 106 (Highly Turbulent Flow)
Friction Factor: ~0.012
Interpretation: The calculated flow rate indicates the volume of gas passing per second. For gas pipelines, flow is often expressed in standard conditions (e.g., m³/hr at 1 atm and 15°C). This requires compressibility factors and adjustments, which this basic calculator doesn't include. However, it provides a crucial basis for initial pipeline design and pressure loss estimations. This highlights the importance of understanding fluid properties for accurate fluid dynamics calculations.
How to Use This Flow Through Pipe Calculator
Using the flow through pipe calculator is straightforward. Follow these steps to get accurate results for your fluid dynamics calculations:
Gather Input Data: Collect all necessary information about your piping system and the fluid you are analyzing. This includes:
Pipe Inner Diameter
Pipe Length
Fluid Dynamic Viscosity
Fluid Density
Pipe Absolute Roughness (material dependent)
Inlet Pressure
Outlet Pressure
Crucially, ensure all units are consistent. If you input diameter in meters, length should be in meters, density in kg/m³, viscosity in Pa·s, roughness in meters, and pressures in Pascals. The calculator is designed for consistency.
Enter Values: Input each piece of data into the corresponding field in the calculator. Use decimal numbers where appropriate.
Validate Inputs: The calculator provides inline validation. If you enter a negative value or leave a field blank, an error message will appear below the input box. Correct any errors before proceeding.
Calculate: Click the "Calculate" button. The calculator will process your inputs using the underlying fluid dynamics equations.
Review Results: The results section will appear, displaying:
Main Result: The calculated Flow Rate (or Pressure Drop, depending on how the calculation is framed/solved).
Intermediate Values: Reynolds Number, Friction Factor (Darcy-Weisbach), and the calculated Pressure Drop (or Flow Rate if that was the primary input).
Formula Explanation: A brief description of the methods used.
Assumptions: Important notes about the calculation's limitations (e.g., incompressible flow).
Interpret Results: Analyze the outputs in the context of your project. Does the flow rate meet your needs? Is the pressure drop within acceptable limits? Use this information for system design and optimization.
Copy Results: If you need to document or share the results, click "Copy Results". This will copy the key figures and assumptions to your clipboard.
Reset Calculator: To start over with a new calculation, click "Reset" to revert all fields to sensible default or empty states.
This tool is a powerful aid for engineers and technicians performing fluid mechanics analysis and making informed decisions about fluid systems.
Key Factors That Affect Flow Through Pipe Results
Several factors significantly influence the behavior of fluids moving through pipes, impacting flow rate, pressure drop, and overall system efficiency. Understanding these is key to accurate pipe flow calculations:
Pipe Diameter (D): This is arguably the most critical factor. A larger diameter pipe offers significantly less resistance to flow for the same flow rate. Doubling the diameter increases the cross-sectional area by four times, drastically reducing velocity and thus the $v^2$ term in the Darcy-Weisbach equation, leading to a much lower pressure drop.
Fluid Viscosity ($\mu$): Higher viscosity fluids are more resistant to flow. Viscosity directly impacts the Reynolds number ($Re = \rho v D / \mu$). A higher viscosity decreases $Re$, potentially shifting flow from turbulent to laminar, which has a different friction factor ($f$). Increased viscosity also directly increases frictional losses, hence higher pressure drop. Think of honey vs. water.
Fluid Density ($\rho$): Density plays a role in the Reynolds number and the pressure drop calculation ($\Delta P \propto \rho v^2$). Denser fluids generally lead to higher Reynolds numbers (more likely turbulent flow) and exert greater force (pressure) at a given velocity, contributing to higher pressure drops. However, its effect is often less dominant than velocity or diameter.
Pipe Roughness ($\epsilon$): The internal surface texture of the pipe directly affects friction, especially in turbulent flow. Smoother pipes (like plastic or drawn tubing) have lower roughness values and thus lower friction factors ($f$), resulting in less pressure loss. Rougher pipes (like cast iron or corroded steel) increase $f$ and significantly raise the pressure drop, particularly at high Reynolds numbers. The relative roughness ($\epsilon/D$) is the key parameter used in friction factor calculations.
Flow Velocity ($v$) / Flow Rate ($Q$): Velocity is squared in the Darcy-Weisbach equation ($\Delta P \propto v^2$), meaning pressure drop increases dramatically with higher velocities. Higher flow rates necessitate higher velocities (since $Q = A \times v$), leading to disproportionately larger pressure drops and potentially requiring more powerful pumps. This relationship emphasizes the importance of optimizing flow rates in engineering designs.
Pipe Length (L): Pressure drop is directly proportional to the length of the pipe. Longer pipes offer more surface area for friction to act upon, accumulating greater resistance to flow. Doubling the pipe length doubles the frictional pressure loss, assuming all other factors remain constant.
System Components (Minor Losses): While this calculator focuses on the Darcy-Weisbach equation for straight pipe sections, real-world systems include fittings, valves, bends, and expansions/contractions. Each of these introduces additional localized pressure losses (minor losses) that add to the total system head loss. These are typically calculated using loss coefficients ($K_L$) and add to the overall pressure drop.
Temperature: Temperature primarily affects fluid viscosity and density. As temperature changes, these properties change, influencing the Reynolds number, friction factor, and ultimately the pressure drop and flow rate.
Frequently Asked Questions (FAQ)
Q1: What is the difference between laminar and turbulent flow in pipes?
Laminar flow (low Reynolds number, typically 4000) involves chaotic, swirling eddies and significant mixing. The friction factor calculation differs drastically between these regimes.
Q2: Does the calculator account for compressible flow (gases)?
This basic calculator assumes incompressible flow, which is a reasonable approximation for liquids and low-velocity gas flows. For high-velocity gas flows or significant pressure changes where density varies considerably, a compressible flow model is required, which is more complex.
Q3: What units should I use?
Consistency is key. The calculator is designed to work with consistent unit sets. For example, use meters for diameter and length, kg/m³ for density, Pa·s for viscosity, and Pascals for pressure. Or, use feet for diameter and length, lb/ft³ for density, reynolds/second for viscosity (less common, often use cP and convert), and psi for pressure. The calculator internally handles common unit conversions if you select them consistently.
Q4: How do I find the absolute roughness ($\epsilon$) for my pipe?
Absolute roughness values depend on the pipe material and manufacturing process. Standard engineering handbooks (like Cameron Hydraulic Data, Crane Technical Paper 410) provide tables of typical $\epsilon$ values for common materials (e.g., PVC, copper, steel, cast iron). You can also find these values from pipe manufacturers.
Q5: What if my pipe has fittings and valves?
This calculator primarily addresses pressure drop due to friction in straight pipe sections (major losses). For a complete system analysis, you must also account for minor losses caused by fittings, valves, elbows, etc. These are typically calculated using loss coefficients ($K_L$) and added to the friction loss.
Q6: Can this calculator determine pump requirements?
Indirectly. By calculating the total pressure drop (head loss) in the system, you know the minimum pressure the pump must overcome to achieve the desired flow rate. The pump's required horsepower would then depend on this pressure difference and the flow rate, along with pump efficiency.
Q7: What is the Colebrook equation and why is it important?
The Colebrook equation is an implicit formula used to accurately calculate the Darcy friction factor ($f$) for turbulent flow in pipes. It considers both the Reynolds number and the relative roughness ($\epsilon/D$). Because it's implicit (f appears on both sides), it usually requires iterative numerical methods or graphical solutions. Our calculator uses explicit approximations derived from it for easier computation.
Q8: How does temperature affect pipe flow?
Temperature significantly impacts fluid properties, primarily viscosity and density. For most liquids, viscosity decreases as temperature increases, leading to lower friction factors and pressure drops. For gases, viscosity generally increases with temperature, while density decreases (at constant pressure). These changes alter the Reynolds number and consequently affect the flow behavior and pressure loss.
Related Tools and Internal Resources
Pipe Sizing Guide: Learn how to select the optimal pipe diameter for your application to balance cost and efficiency.
Fluid Dynamics Principles Explained: Deep dive into the physics governing fluid motion, including Bernoulli's principle and viscosity effects.
Pressure Unit Converter: Quickly convert pressure values between various units like PSI, Pascals, bar, and atm.
Fluid Viscosity Database: Look up viscosity and density values for a wide range of common fluids at different temperatures.
Pump Performance Calculator: Estimate pump head, flow rate, and power requirements based on system parameters.
Piping System Design Checklist: A comprehensive guide to ensure all aspects of your piping system design are considered.
// — Calculator Logic —
var initialData = {
pipeDiameter: ",
pipeLength: ",
fluidViscosity: ",
fluidDensity: ",
roughness: ",
inletPressure: ",
outletPressure: "
};
function getInputValue(id) {
var element = document.getElementById(id);
if (!element) return null;
var value = parseFloat(element.value);
return isNaN(value) ? null : value;
}
function setErrorMessage(id, message) {
var errorElement = document.getElementById(id);
if (errorElement) {
errorElement.textContent = message;
errorElement.style.display = message ? 'block' : 'none';
}
}
function isValidNumber(value, min, max) {
if (value === null || typeof value === 'undefined') return false;
if (typeof value !== 'number' || isNaN(value)) return false;
if (min !== null && value max) return false;
return true;
}
var chartReynoldsFriction = null;
var chartFlowPressure = null;
function calculateFlow() {
// — Clear previous errors and results —
setErrorMessage('pipeDiameterError', ");
setErrorMessage('pipeLengthError', ");
setErrorMessage('fluidViscosityError', ");
setErrorMessage('fluidDensityError', ");
setErrorMessage('roughnessError', ");
setErrorMessage('inletPressureError', ");
setErrorMessage('outletPressureError', ");
document.getElementById('results').style.display = 'none';
// — Get Input Values —
var diameter = getInputValue('pipeDiameter'); // meters
var length = getInputValue('pipeLength'); // meters
var viscosity = getInputValue('fluidViscosity'); // Pa·s
var density = getInputValue('fluidDensity'); // kg/m³
var roughness = getInputValue('roughness'); // meters
var inletPressure = getInputValue('inletPressure'); // Pascals
var outletPressure = getInputValue('outletPressure'); // Pascals
// — Input Validation —
var errors = false;
if (!isValidNumber(diameter, 0.001, null)) { setErrorMessage('pipeDiameterError', 'Please enter a valid pipe diameter (e.g., 0.05 meters).'); errors = true; }
if (!isValidNumber(length, 0.1, null)) { setErrorMessage('pipeLengthError', 'Please enter a valid pipe length (e.g., 100 meters).'); errors = true; }
if (!isValidNumber(viscosity, 1e-6, null)) { setErrorMessage('fluidViscosityError', 'Please enter a valid viscosity (e.g., 0.001 Pa·s for water).'); errors = true; }
if (!isValidNumber(density, 0.1, null)) { setErrorMessage('fluidDensityError', 'Please enter a valid density (e.g., 1000 kg/m³ for water).'); errors = true; }
if (!isValidNumber(roughness, 0, null)) { setErrorMessage('roughnessError', 'Please enter a valid roughness value (e.g., 4.5e-5 meters).'); errors = true; }
if (!isValidNumber(inletPressure, 0, null)) { setErrorMessage('inletPressureError', 'Please enter a valid inlet pressure.'); errors = true; }
if (!isValidNumber(outletPressure, 0, null)) { setErrorMessage('outletPressureError', 'Please enter a valid outlet pressure.'); errors = true; }
// Handle pressure comparison
if (isValidNumber(inletPressure, 0, null) && isValidNumber(outletPressure, 0, null) && inletPressure <= outletPressure) {
setErrorMessage('outletPressureError', 'Outlet pressure must be lower than inlet pressure for flow calculation.');
errors = true;
}
if (errors) {
return; // Stop calculation if there are errors
}
var pressureDrop = inletPressure – outletPressure; // Pascals
// — Calculations —
var frictionFactor = 0;
var reynoldsNumber = 0;
var velocity = 0;
var flowRate = 0;
var calculatedPressureDrop = 0; // To compare with input or to calculate flow
// Use Swamee-Jain for initial guess or iterative calculation
var relativeRoughness = roughness / diameter;
var maxIterations = 100;
var tolerance = 1e-6;
var currentF = 0.02; // Initial guess for friction factor
// Calculate initial velocity and Reynolds number to guess flow rate
// This is an iterative process if we only have pressure drop.
// Let's assume we are calculating flow rate FROM pressure drop.
var maxVelocity = Math.sqrt(2 * pressureDrop * diameter / (density * length * relativeRoughness)); // Rough upper bound
var minVelocity = 0.01; // Lower bound
var iterVelocity = (minVelocity + maxVelocity) / 2;
for (var i = 0; i < maxIterations; ++i) {
reynoldsNumber = density * iterVelocity * diameter / viscosity;
var f_iter;
if (reynoldsNumber < 2300) {
f_iter = 64 / reynoldsNumber;
} else {
// Swamee-Jain explicit approximation for turbulent flow
f_iter = Math.pow(
-2.0 * Math.log10(
(relativeRoughness / 3.7) + (2.51 / (reynoldsNumber * Math.sqrt(currentF))) // Colebrook implicit form inside log
// Using Swamee-Jain explicit form directly:
// f_iter = Math.pow(-2.0 * Math.log10((relativeRoughness / 3.7) + (5.74 / Math.pow(reynoldsNumber, 0.9))), -2); // Swamee-Jain explicit
), -2);
// Let's use Swamee-Jain explicit form for simplicity and performance
f_iter = Math.pow(
-2.0 * Math.log10(
(relativeRoughness / 3.7) + (5.74 / Math.pow(reynoldsNumber, 0.9))
), -2);
}
calculatedPressureDrop = f_iter * (length / diameter) * (density * Math.pow(iterVelocity, 2) / 2);
if (Math.abs(calculatedPressureDrop – pressureDrop) pressureDrop) {
maxVelocity = iterVelocity;
} else {
minVelocity = iterVelocity;
}
iterVelocity = (minVelocity + maxVelocity) / 2;
currentF = f_iter; // Update guess for next iteration if needed by implicit form
if (i === maxIterations – 1) {
// Could not converge well, use last calculated values
frictionFactor = f_iter;
velocity = iterVelocity;
calculatedPressureDrop = f_iter * (length / diameter) * (density * Math.pow(iterVelocity, 2) / 2); // Recalculate with last v
console.warn("Flow calculation may not have fully converged.");
}
}
flowRate = (Math.PI * Math.pow(diameter, 2) / 4) * velocity;
// — Display Results —
document.getElementById('mainResultFlowRate').textContent = formatNumber(flowRate, 5) + ' m³/s';
document.getElementById('intermediateReynolds').textContent = formatNumber(reynoldsNumber, 0);
document.getElementById('intermediateFrictionFactor').textContent = formatNumber(frictionFactor, 4);
document.getElementById('intermediatePressureDrop').textContent = formatNumber(pressureDrop, 0) + ' Pa'; // Display the input pressure drop
document.getElementById('results').style.display = 'block';
// Update Charts
updateCharts(diameter, length, viscosity, density, roughness);
}
// Function to calculate flow rate for chart generation if needed
function calculateFlowForChart(velocity, diameter, length, viscosity, density, roughness) {
var reynolds = density * velocity * diameter / viscosity;
var f = 0;
var relativeRoughness = roughness / diameter;
if (reynolds < 2300) {
f = 64 / reynolds;
} else {
f = Math.pow(
-2.0 * Math.log10(
(relativeRoughness / 3.7) + (5.74 / Math.pow(reynolds, 0.9))
), -2);
}
var pressureDrop = f * (length / diameter) * (density * Math.pow(velocity, 2) / 2);
return { velocity: velocity, pressureDrop: pressureDrop, reynolds: reynolds, frictionFactor: f };
}
function updateCharts(diameter, length, viscosity, density, roughness) {
// Reynolds Number vs Friction Factor Chart Data
var reynoldsData = [1000, 5000, 10000, 50000, 100000, 500000, 1000000, 5000000];
var frictionFactorData = [];
var frictionFactorDataRough = [];
var frictionFactorDataVeryRough = [];
var relativeRoughness = roughness / diameter;
// Use a moderate roughness and a very rough one for comparison
var moderateRoughness = 0.0001; // e.g., steel
var veryRough = 0.0005; // e.g., heavily corroded pipe
for (var i = 0; i < reynoldsData.length; i++) {
var re = reynoldsData[i];
var f_current, f_moderate, f_veryRough;
// Calculate for the actual roughness entered
if (re < 2300) {
f_current = 64 / re;
} else {
f_current = Math.pow(-2.0 * Math.log10((relativeRoughness / 3.7) + (5.74 / Math.pow(re, 0.9))), -2);
}
frictionFactorData.push(f_current);
// Calculate for moderate roughness
if (re < 2300) {
f_moderate = 64 / re;
} else {
f_moderate = Math.pow(-2.0 * Math.log10((moderateRoughness / diameter / 3.7) + (5.74 / Math.pow(re, 0.9))), -2);
}
frictionFactorDataRough.push(f_moderate);
// Calculate for very rough pipe
if (re < 2300) {
f_veryRough = 64 / re;
} else {
f_veryRough = Math.pow(-2.0 * Math.log10((veryRough / diameter / 3.7) + (5.74 / Math.pow(re, 0.9))), -2);
}
frictionFactorDataVeryRough.push(f_veryRough);
}
if (chartReynoldsFriction) {
chartReynoldsFriction.destroy();
}
var ctxReynolds = document.getElementById('reynoldsFrictionChart').getContext('2d');
chartReynoldsFriction = new Chart(ctxReynolds, {
type: 'line',
data: {
labels: reynoldsData.map(function(r) { return formatNumber(r, 0); }),
datasets: [{
label: 'Your Pipe Roughness',
data: frictionFactorData,
borderColor: '#004a99',
fill: false,
tension: 0.1
}, {
label: 'Moderate Roughness (e.g., Steel)',
data: frictionFactorDataRough,
borderColor: '#28a745',
fill: false,
tension: 0.1
}, {
label: 'Very Rough Pipe',
data: frictionFactorDataVeryRough,
borderColor: '#dc3545',
fill: false,
tension: 0.1
}]
},
options: {
responsive: true,
maintainAspectRatio: true,
scales: {
x: {
title: {
display: true,
text: 'Reynolds Number (Re)'
},
type: 'logarithmic' // Re is often plotted on log scale
},
y: {
title: {
display: true,
text: 'Friction Factor (f)'
},
type: 'linear' // Friction factor is linear
}
},
plugins: {
tooltip: {
callbacks: {
label: function(context) {
var label = context.dataset.label || '';
if (label) {
label += ': ';
}
if (context.parsed.y !== null) {
label += context.parsed.y.toFixed(4);
}
return label;
}
}
}
}
}
});
// Flow Rate vs Pressure Drop Chart Data
var velocities = [];
var pressureDrops = [];
// Generate velocities from a reasonable range up to slightly higher than current flow
var currentVelocity = getInputValue('mainResultFlowRate') ? (parseFloat(document.getElementById('mainResultFlowRate').textContent.replace(' m³/s','')) / (Math.PI * Math.pow(diameter, 2) / 4)) : 1; // Fallback if not calculated yet
currentVelocity = isNaN(currentVelocity) || currentVelocity === 0 ? 1 : currentVelocity; // Ensure fallback
for (var v = 0.1; v 0) {
var calcResult = calculateFlowForChart(v, diameter, length, viscosity, density, roughness);
if (calcResult.pressureDrop > 0 && calcResult.pressureDrop < Infinity) {
velocities.push(v);
pressureDrops.push(calcResult.pressureDrop);
}
}
}
if (chartFlowPressure) {
chartFlowPressure.destroy();
}
var ctxFlowPressure = document.getElementById('flowPressureChart').getContext('2d');
chartFlowPressure = new Chart(ctxFlowPressure, {
type: 'line',
data: {
labels: velocities.map(function(vel) { return formatNumber(vel, 2); }), // Velocity labels
datasets: [{
label: 'Pressure Drop (Pa)',
data: pressureDrops,
borderColor: '#004a99',
fill: false,
tension: 0.1
}]
},
options: {
responsive: true,
maintainAspectRatio: true,
scales: {
x: {
title: {
display: true,
text: 'Flow Velocity (m/s)'
}
},
y: {
title: {
display: true,
text: 'Pressure Drop (Pa)'
}
}
},
plugins: {
tooltip: {
callbacks: {
label: function(context) {
var label = context.dataset.label || '';
if (label) {
label += ': ';
}
if (context.parsed.y !== null) {
label += context.parsed.y.toLocaleString(); // UsetoLocaleString for large numbers
}
return label;
}
}
}
}
}
});
}
function formatNumber(num, decimals) {
if (num === null || typeof num === 'undefined' || isNaN(num)) return '–';
return num.toFixed(decimals).replace(/\B(?=(\d{3})+(?!\d))/g, ",");
}
function resetCalculator() {
document.getElementById('pipeDiameter').value = '';
document.getElementById('pipeLength').value = '';
document.getElementById('fluidViscosity').value = '';
document.getElementById('fluidDensity').value = '';
document.getElementById('roughness').value = '';
document.getElementById('inletPressure').value = '';
document.getElementById('outletPressure').value = '';
setErrorMessage('pipeDiameterError', '');
setErrorMessage('pipeLengthError', '');
setErrorMessage('fluidViscosityError', '');
setErrorMessage('fluidDensityError', '');
setErrorMessage('roughnessError', '');
setErrorMessage('inletPressureError', '');
setErrorMessage('outletPressureError', '');
document.getElementById('results').style.display = 'none';
document.getElementById('mainResultFlowRate').textContent = '–';
document.getElementById('intermediateReynolds').textContent = '–';
document.getElementById('intermediateFrictionFactor').textContent = '–';
document.getElementById('intermediatePressureDrop').textContent = '–';
// Reset chart data if needed, or just var updateCharts handle it next time
if (chartReynoldsFriction) chartReynoldsFriction.destroy();
if (chartFlowPressure) chartFlowPressure.destroy();
// Re-initialize empty charts maybe
initializeCharts();
}
function copyResults() {
var mainResult = document.getElementById('mainResultFlowRate').textContent;
var reynolds = document.getElementById('intermediateReynolds').textContent;
var friction = document.getElementById('intermediateFrictionFactor').textContent;
var pressureDrop = document.getElementById('intermediatePressureDrop').textContent;
var assumptions = "Assumptions: Steady, incompressible flow. Consistent units used (e.g., SI).";
var resultsText = "Flow Through Pipe Calculation Results:\n\n";
resultsText += "Main Result – Flow Rate: " + mainResult + "\n";
resultsText += "Reynolds Number: " + reynolds + "\n";
resultsText += "Friction Factor (Darcy-Weisbach): " + friction + "\n";
resultsText += "Pressure Drop: " + pressureDrop + "\n\n";
resultsText += assumptions;
// Use a temporary textarea to copy to clipboard
var textArea = document.createElement("textarea");
textArea.value = resultsText;
textArea.style.position = "fixed";
textArea.style.left = "-9999px";
document.body.appendChild(textArea);
textArea.focus();
textArea.select();
try {
var successful = document.execCommand('copy');
var msg = successful ? 'Results copied!' : 'Copy failed!';
// Optionally display a temporary message to the user
alert(msg);
} catch (err) {
alert('Copying failed: ' + err);
}
document.body.removeChild(textArea);
}
// Chart.js initialization (needs to be included or defined)
// Assuming Chart.js is available globally
function initializeCharts() {
// Initialize empty charts
var ctxReynolds = document.getElementById('reynoldsFrictionChart').getContext('2d');
chartReynoldsFriction = new Chart(ctxReynolds, {
type: 'line',
data: {
labels: [], datasets: [{ label: 'No Data', data: [], borderColor: '#ccc', fill: false }]
},
options: { scales: { x: {}, y: {} }, plugins: { legend: { display: false } } }
});
var ctxFlowPressure = document.getElementById('flowPressureChart').getContext('2d');
chartFlowPressure = new Chart(ctxFlowPressure, {
type: 'line',
data: {
labels: [], datasets: [{ label: 'No Data', data: [], borderColor: '#ccc', fill: false }]
},
options: { scales: { x: {}, y: {} }, plugins: { legend: { display: false } } }
});
}
// Call initialization on load
window.onload = function() {
// Set some default values for better user experience
// Example: Water properties
// document.getElementById('fluidViscosity').value = '0.001'; // Pa·s
// document.getElementById('fluidDensity').value = '1000'; // kg/m³
// Example: Smooth pipe
// document.getElementById('roughness').value = '1.5e-6'; // meters
initializeCharts(); // Initialize empty charts
// Trigger initial chart update if default values are set or if calculation should run on load
// calculateFlow(); // Optional: auto-calculate on load if defaults are set
};