In process industries, it is not uncommon for pipes to be only partially full of liquid. This can occur in various scenarios, such as in return pipes or condensate lines. Assuming that a pipe is full when it is not can lead to erroneous calculations, which can have significant implications for process efficiency, safety, and cost. This article discusses a method proposed by Durand and reported by Brannan to determine if a pipe is totally full or partially full, and how to calculate the height of liquid in the pipe and the equivalent diameter.
Before delving into the calculations, it is essential to understand some key terms:
Given:
Q/d^2.5 = 500 / (10)^2.5 = 500 / 316.23 = 1.58
Since Q/d^2.5 < 10.2, the pipe may be partially full.
x = ln(1.58) ≈ 0.457
H/D = 0.446 + 0.272(0.457) + 0.0397(0.457)^2 - 0.0153(0.457)^3 - 0.003575(0.457)^4 ≈ 0.582
H = (H/D) * D = 0.582 * (10/12) ≈ 0.485 feet
De/D = -0.01130 + 3.040(0.582) - 3.461(0.582)^2 + 4.108(0.582)^3 - 2.638(0.582)^4 ≈ 0.786
De = (De/D) * D = 0.786 * (10/12) ≈ 0.655 feet
Warning : this calculator is provided to illustrate the concepts mentioned in this webpage, it is not intended for detail design. It is not a commercial product, no guarantee is given on the results. Please consult a reputable designer for all detail design you may need.

Warning : this calculator is provided to illustrate the concepts mentioned in this webpage, it is not intended for detail design. It is not a commercial product, no guarantee is given on the results. Please consult a reputable designer for all detail design you may need.
Calculate \( \frac{Q}{d^{2.5}} \), where \( Q \) is flow rate (gpm) and \( d \) is pipe diameter (inches). If \( \frac{Q}{d^{2.5}} \geq 10.2 \), the pipe is full. If \( \frac{Q}{d^{2.5}} < 10.2 \), the pipe may be partially full, and further calculations are needed.
Key terms include: - Flow Rate (\( Q \)): Volume of fluid per unit time (gpm). - Pipe Diameter (\( d \)): Internal diameter of the pipe (inches). - Height of Liquid (\( H \)): Vertical distance from the pipe bottom to the liquid surface (feet). - Equivalent Diameter (\( D_e \)): Diameter of a hypothetical full pipe with equivalent flow characteristics (feet).
This method is applicable only for horizontal, closed-flow conditions with Newtonian fluids like water. It should not be used for sloped pipes, vented systems, or multi-phase flows. Use it as a preliminary screening tool, followed by full pipe hydraulics calculations.
First, calculate \( x = \ln\left(\frac{Q}{d^{2.5}}\right) \). Then, use the polynomial: \[ \frac{H}{D} = 0.446 + 0.272x + 0.0397x^2 - 0.0153x^3 - 0.003575x^4 \] Finally, \( H = \frac{H}{D} \times D \), where \( D \) is pipe diameter in feet.
Use the polynomial: \[ \frac{D_e}{D} = -0.01130 + 3.040\left(\frac{H}{D}\right) - 3.461\left(\frac{H}{D}\right)^2 + 4.108\left(\frac{H}{D}\right)^3 - 2.638\left(\frac{H}{D}\right)^4 \] Then, \( D_e = \frac{D_e}{D} \times D \), where \( D \) is pipe diameter in feet.
The polynomial curves have an estimated accuracy of ±5–10%. They are best suited for preliminary sizing or confirming aesthetics, not final hydraulic design.
No, these methods are for horizontal pipes only. For sloped pipes, use open-channel flow methods like the Manning formula.
The method is limited to horizontal, closed-flow conditions with water-like fluids. It should not be used for pipes with significant slope, venting, multi-phase flow, or sloped gravity flow.
Yes, our website offers a free Excel calculator for determining if a pipe is full or partially full and calculating liquid height and equivalent diameter.
The calculator provides approximations for quick estimations. For detailed design, consult a reputable engineer or designer.