Examples Gallery

This gallery demonstrates pipeline sizing, pressure drop, and network modeling using ProcessPI.

---

Pipe Lines

• Chlorine Gas Optimum Diameter
  Estimate optimum pipe diameter for chlorine gas at 10 000 kg/h, 6 atm, 20 °C.

• CO₂ Transfer Line
  Pipeline design for CO₂ transfer line between plants with fittings and pressure drop limits.

• Carbon Monoxide Pipeline
  Pipeline sizing for CO at 1500 kg/h with multiple elbows and valves.

• Water Transfer (Steel vs Concrete)
  Compare carbon steel vs concrete pipe for water transfer over long distances.

• Organic Liquid Discharge
  Discharge line sizing for organic liquid with complex fittings and valves.

• Complex Network
  Demonstration of a branched pipeline network with pumps, vessels, and equipment.

• Chilled Water Loop
  Demonstrates handling large network topologies, fixed diameters, and multiple equipment elements.

Calculations

• Fluid Velocity Calculation 1
  Calculate velocity of a fluid from volumetric flow and pipe diameter.

• Fluid Velocity Calculation 2
  Alternative fluid velocity calculation with different conditions.

• Velocity and Reynolds Number (US Units)
  Compute velocity and Reynolds number using US customary units.

• Velocity and Reynolds Number (Metric Units)
  Compute velocity and Reynolds number using SI units.

• Friction Factor (Colebrook-White, US Units)
  Estimate Darcy friction factor with Colebrook-White equation in US units.

• Darcy Pressure Drop (US Units)
  Calculate pressure drop using Darcy–Weisbach equation in US units.

• Long Pipeline Pressure Drop (Metric Units)
  Pressure drop calculation for long pipelines with SI units.

• Hazen-Williams Pressure Drop (US Units)
  Estimate pressure drop using Hazen–Williams formula in US units.