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.
2. Key concepts and terminology
Before delving into the calculations, it is essential to understand
some key terms:
Flow Rate (Q): The volume of fluid that passes through a given
surface per unit time. It is typically measured in gallons per
minute (gpm).
Pipe Diameter (d): The internal diameter of the pipe, usually
measured in inches (in).
Height of Liquid (H): The vertical distance from the bottom of
the pipe to the surface of the liquid, measured in feet (ft).
Equivalent Diameter (De): The diameter of a hypothetical full
pipe that would have the same flow characteristics as the
partially full pipe, measured in feet (ft).
3. Pipe full or partially filled ?
To know if the pipe is full or not, it is necessary to calculate Q/d2.5
- If ≥ 10.2 it means the pipe is
full
- If < 10.2 the pipe may be
partially full only, further calculations are required to know the
height of liquid in the pipe and the equivalent diameter
With :
Q = flow rate in gpm
d = pipe diameter in in
The rule of thumb applies only to
fully horizontal, closed-flow conditions—typically water or water-like
Newtonian fluids. Do not use for pipes with significant slope,
venting, multi-phase, or sloped gravity flow. Recommendation: Use this
Q/d^2.5 criterion only as preliminary screening at horizontal
discharge points; full pipe hydraulics (e.g. Manning,
Hazen–Williams, Darcy–Weisbach with De) should follow.
For sloped pipes, use the Manning formula or other open-channel
shallow‑flow methods → Manning requires wetted perimeter and hydraulic
radius.
4. Calculation of the Height of liquid
The method is proposing to have x
= ln (Q/d2.5)
Then calculate H/D =
0.446+0.272x+0.0397x2-0.0153x3-0.003575x4
With :
H = height of liquid in the pipe
in ft
The polynomial curves have
estimated accuracy ± 5–10 %. The method is approximate and best suited
for preliminarily sizing or confirming aesthetics, not final hydraulic
design.
5. Equivalent diameter calculation
The equivalent diameter can be
calculated from the following correlation :
The polynomial curves have
estimated accuracy ± 5–10 %. The method is approximate and best suited
for preliminarily sizing or confirming aesthetics, not final hydraulic
design.
6. Practical examples
Given:
Flow rate (Q) = 500 gpm
Pipe diameter (d) = 10 inches
Step 1: Calculate Q/d^2.5
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.
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.
7.2 Online pipe partial flow calculator
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.
Pipe Flow Calculator
⚠️ ENGINEERING NOTICE & EDUCATIONAL DISCLAIMER: This interactive calculator is provided exclusively for preliminary estimation and educational purposes. It is not intended for detailed design or equipment procurement without certified vendor rating. No warranty, expressed or implied, is provided, and no liability is assumed.
Note: This calculator
uses the method proposed by Durand to determine if a pipe is full
or partially full, and to calculate the height of liquid and
equivalent diameter.
Input Parameters
*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.
⚙️ Practical Plant Engineering Rules of Thumb & Safety Limits
Q/d2.5 screening: Use only for horizontal, closed-flow, water-like Newtonian fluids. Threshold = 10.2 (gpm, in).
Liquid velocity (full pipe): Typical design 1.0–1.5 m/s (3–5 ft/s) for pump discharge; ≤ 3 m/s (10 ft/s) absolute to limit erosion.
Gravity / partially full lines: Target 0.6–1.2 m/s (2–4 ft/s) to avoid solids settling and air entrainment.
Minimum slope for drainage: 1:100 (1%) for water-like fluids; 1:50 for slurries.
Equivalent diameter (De): Use De for downstream Darcy–Weisbach or Hazen–Williams pressure-drop checks — never the nominal pipe ID.
Accuracy: Durand polynomials ±5–10%. Always confirm with a full hydraulic model before procurement.
Failure modes: Underestimated H → pump cavitation / NPSH deficit; overestimated De → undersized line and excessive ΔP.
FAQ: Partially Full Pipes - Calculations and Concepts
1. How do you determine if a pipe is full or partially full?
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.
2. What are the key terms used in partially full pipe
calculations?
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).
3. When should the \( \frac{Q}{d^{2.5}} \) method be used?
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.
4. How is the height of liquid (\( H \)) in a partially full
pipe calculated?
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.
5. How is the equivalent diameter (\( D_e \)) calculated?
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.
6. What is the accuracy of these calculations?
The polynomial curves have an estimated accuracy of ±5–10%.
They are best suited for preliminary sizing or confirming
aesthetics, not final hydraulic design.
7. Can these methods be used for sloped pipes?
No, these methods are for horizontal pipes only. For sloped
pipes, use open-channel flow methods like the Manning formula.
8. What are the limitations of the \( \frac{Q}{d^{2.5}} \)
method?
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.
9. Are there tools available for these calculations?
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.
10. What precautions should be taken when using the
calculator?
The calculator provides approximations for quick estimations.
For detailed design, consult a reputable engineer or designer.
Source
Rules of thumb for Chemical
Engineers, Brannan, Elsevier, page 5