Two 1000 L tanks, roughly 320 meters apart, connected by a small plastic pipe with only gravity to move the water. This ChemForge example uses 5.8 meters of usable driving head after subtracting the lower tank stand height, then sweeps inlet flow from 0 to 50 L/min.
The curve is the useful part: increase the requested flow until the pipeline outlet pressure reaches about 0 psig. Above that flow, the pipe would need more gravity head than the tanks provide.
| Model input | Value | Why it matters |
|---|---|---|
| Pipe length | 320 m | Long enough that friction dominates the answer. |
| Pipe size | 1" Sch 40 | Small diameter means high velocity and high head loss. |
| Elevation change | -5.8 m | The lower tank stand subtracts 3 m from the gross elevation. |
| Sweep range | 0-50 L/min | Shows the operating limit without manually guessing flows. |
A valve can reduce the flow rate because it adds resistance. It does not create more available elevation head; it moves the operating point to a lower flow where the pipe friction and valve loss fit inside the gravity head. For this kind of system, increasing pipe diameter is usually the cleanest way to keep useful flow without needing a pump.
ChemForge uses Darcy-Weisbach with a friction factor approximation to Colebrook-White, then adds fitting K-factors and any elevation term on the connector. This example keeps the inlet's Mass Flow field intact; the Sensitivity Study temporarily uses the inlet flow-basis logic to evaluate each L/min point in the sweep.
Launches ChemForge with the gravity tank transfer line pre-loaded. Free, no sign-up.
Open in ChemForge