Exclusive Repack - Module 3 Process Piping Hydraulics Sizing And Pressure Rating Pdf
cap A equals the fraction with numerator cap Q and denominator v end-fraction : Calculate the required ID from the area (
Power Piping (Steam generation stations, boiler systems).
tm=P⋅Do2(S⋅E⋅W+P⋅Y)+ct sub m equals the fraction with numerator cap P center dot cap D sub o and denominator 2 open paren cap S center dot cap E center dot cap W plus cap P center dot cap Y close paren end-fraction plus c
): Fluid particles move in highly irregular, chaotic paths. Inertial forces dominate. Most industrial process piping operates in the turbulent regime. Pressure Drop and Friction Loss cap A equals the fraction with numerator cap
To calculate the minimum required inside cross-sectional area based on volumetric flow rate ( ) and target velocity (
Exceeding recommended velocity limits causes erosion, water hammer, and excessive noise. Excessively low velocities lead to particle sedimentation and oversized, expensive piping. Fluid Type Recommended Velocity Range (m/s) Recommended Velocity Range (ft/s) 0.5 – 1.2 1.5 – 4.0 Water (Pump Discharge) 1.5 – 3.0 5.0 – 10.0 Steam (Saturated) 30.0 – 40.0 100.0 – 130.0 Steam (Superheated) 40.0 – 60.0 130.0 – 200.0 Air / Gases (Low Pressure) 15.0 – 30.0 50.0 – 100.0 Step 2: Calculate Internal Diameter
Calculating the Reynolds number determines the flow regime (laminar, transition, or turbulent). Sanitary systems, for example, often require full turbulence ( ) to prevent stagnation. CEDengineering.com 2. Pressure Drop and Friction Loss Most industrial process piping operates in the turbulent
Hydraulics play a crucial role in process piping, as they determine the flow rate, pressure drop, and energy loss in the piping system. The goal of hydraulic analysis is to ensure that the piping system can handle the required flow rates, pressures, and temperatures, while also minimizing energy losses and pressure drops.
) must also account for mechanical allowances, corrosion allowances (
Where the complexity lies is in the friction factor ($f$). In modern engineering, this is solved using the or the Moody Chart . If it does
Calculate the actual pressure drop across the selected pipe size to ensure it falls within acceptable limits. 3. Calculating Friction and Pressure Losses
For now, this guide serves as your launchpad. With a firm grasp of these principles, you are equipped to tackle the technical challenges of industrial piping design and take the next step in your engineering career.
In pump suction piping, pressure must never drop below the fluid's vapor pressure. If it does, vapor bubbles form and collapse violently (cavitation), destroying pump impellers. Ensure that exceeds NPSH Required (NPSHR) by a safety margin of at least 0.5 meters (1.5 feet). Water Hammer (Surge Pressure)