Learn how to calculate chilled water pump head for closed
loop systems using a practical HVAC example, Darcy-Weisbach method, and ASHRAE
standards.
Introduction
Correct pump sizing is fundamental to the performance and
energy efficiency of any chilled water system. Despite this, many HVAC
engineers—especially early in their careers—either oversize pumps or
miscalculate head due to misunderstanding hydraulic losses.
This article explains how to calculate pump head for a
closed loop chilled water system, using a real practical example, systematic
calculation steps, and globally accepted HVAC standards such as ASHRAE and
CIBSE.
Understanding Pump Head in a Closed Loop System
In a closed loop chilled water system, the pump does not
need to overcome static height. This is because the supply and return water
columns balance each other.
According to ASHRAE, pump head in closed systems consists
only of dynamic pressure losses, which include:
- Pipe friction losses
- Losses due to fittings and valves
- Pressure drop across equipment (AHU, FCU, Chiller)
ASHRAE Handbook confirms that elevation head cancels out in
closed hydronic loops.
Step-by-Step Chilled Water Pump Head Calculation
Step 1: Identify the Critical Path
From HVAC layout drawings, identify the hydraulically
longest path from the pump to the most remote terminal unit (usually the
farthest AHU).
Only this path is used for pump head calculation, as recommended by ASHRAE and Carrier design manuals.
Step 2: Draw an Isometric Diagram
Prepare an isometric diagram showing:
- Pipe lengths
- Pipe sizes (DN)
- Flow rates (L/s)
- Valves, fittings, and equipment
This ensures no component is missed during head loss calculation.
Step 3: Assign Reference Numbers
Each pipe segment, valve, and fitting is given a reference number. Items with the same pipe size and flow may share a reference. This method improves calculation accuracy and review clarity.
Step 4: Create the Calculation Table
Prepare a spreadsheet with the following columns:
- Description
- Pipe size (DN)
- Flow rate (L/s)
- Quantity
- Equivalent length (m)
- Total length (m)
- Head loss rate (m/100 m)
- Total head loss (m)
This approach is widely used in professional HVAC design documentation.
Step 5: Determine Equivalent Lengths of Valves and Fittings
Valves and fittings are converted into equivalent pipe lengths using standard tables.
- Common components include:
- Gate valves
- Swing check valves
- Strainers
- Double regulating valves
- Elbows and tees
Equivalent length data is typically referenced from Crane Technical Paper 410, which is an industry-accepted hydraulic reference.
Step 6: Calculate Total Length
Total Length = Equivalent Length × Quantity
This converts all minor losses into an equivalent friction length.
Step 7: Calculate Pipe Friction Loss Rate
Preferred Method: Darcy–Weisbach Equation
The Darcy–Weisbach equation is the most accurate method for calculating pipe friction loss:
Δℎ = 𝑓⋅(𝐿/𝐷)⋅(𝑉²/2𝑔)
ASHRAE recommends Darcy–Weisbach for detailed HVAC hydraulic calculations.
Alternate Method: ASHRAE Friction Charts
ASHRAE friction charts may be used for quick estimation but are less accurate.
Step 8: Populate Head Loss Rate
Enter the calculated head loss rate (m/100 m) for each pipe size and flow rate into the table.
Step 9: Calculate Total Head Loss
ΔH= (Δh/100)×L
Sum losses for:
- Pipes
- Valves
- Fittings
Step 9: Calculate Total Head Loss
Add manufacturer-provided pressure drops for:
- AHUs
- FAHUs
- FCUs
- Chillers
ASHRAE and CIBSE both stress using certified manufacturer
data for equipment losses .
Step 11: Add Safety Factor
A 15% safety margin is added to account for:
- Site routing changes
- Pipe aging and fouling
- Minor design variations
Pump Head = ℎ1 + 0.15ℎ1
This margin is standard HVAC engineering practice.
Final Pump Head Result (From Practical Example)
- Total system head loss: 7.4 m
- Safety factor (15%): 1.1 m
- Final pump head selected: ≈ 11 m (1.1 bar / 110 kPa)
This ensures reliable operation and avoids undersizing.
Key Takeaways for New Engineers
- Closed loop systems do not require static head
- Always size pumps based on the critical path
- Darcy–Weisbach is preferred for accuracy
- Never guess equipment pressure drops
- Avoid oversizing pumps to reduce energy waste








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