Hydraulic calculation is the heart of sprinkler design: it shows whether the water supply can meet the system demand. FM Global DS 3-0 (Hydraulics of Fire Protection Systems, March 2010, 65 pages) compares two things at one reference point, the base of the riser (BOR): the hydraulic demand of the sprinkler system and the available water supply (Section 1.0). It covers the hydraulic method, not the physical layout of systems.

The Governing Relationships

  1. Sprinkler discharge: q = K × √p (Equation 7), with q in L/min, p in bar and K in L/min/bar0.5; conversely p = (q/K)² (Equation 4).
  2. Flow from density: q = D × S × L (Equation 3), with D in mm/min and S and L the sprinkler spacings in metres.
  3. Friction (Hazen-Williams): p = 6.05 × 10^5 × Q^1.85 / (C^1.85 × d^4.87) bar/m, Q in L/min, d in mm (Equation 15); total loss PF = p × L (Equation 16).
  4. Elevation: PE = 0.098 bar/m × h (0.433 psi/ft; Equation 2).
  5. Velocity pressure: not used in the FM method; total pressure is the pressure at the most remote sprinkler plus friction plus elevation (2.1.2.3.1).

For liquids other than water, such as antifreeze solutions, the Darcy-Weisbach method is used instead of Hazen-Williams (2.1.2.3.6).

K-Factor and Design Density

Sprinkler flow is coverage multiplied by density. For an HC-2 area (DS 3-26 Table 2.3.1.10: 8 mm/min over 230 m²) at 11.9 m² per sprinkler (3.5 m × 3.4 m), q = 8 × 11.9 = 95.2, about 95 L/min. A K80 sprinkler then needs (95/80)² = 1.41 bar and a K115 sprinkler (95/115)² = 0.68 bar, both above the DS 3-26 minimum of 0.5 bar at the most remote sprinkler (2.3.1.11).

Building the Demand Point

  1. Take the design format from the occupancy data sheet: density/demand area or number of sprinklers/pressure (2.1.2.2.1).
  2. Calculate the number of sprinklers in the design area and per branch line, with a shape factor of 1.2 under flat ceilings or 1.4 above 5° (Equations 10–11).
  3. Locate the most hydraulically remote sprinkler and position the design area from it (2.1.2.2.4–2.1.2.2.5).
  4. Work from the most remote sprinkler, calculating each sprinkler’s flow and pressure with the friction and elevation between them, and balance flows at junctions (Equation 19).
  5. Add friction and elevation along the cross main and riser to reach the flow and pressure at the BOR: the demand point.

For the details and a numerical example see the DS 3-0 most demanding area article.

Supply Curve Against Demand Point

FM and NFPA 13 Compared

Quick Checklist

Frequently Asked Questions

What is the demand point and why does it matter?

It is the flow and pressure the sprinkler system requires at its reference point, the base of the riser in FM DS 3-0. It is what the whole calculation produces and what is compared against the water supply curve on N^1.85 paper; the system is rated Adequate only if the supply, after deductions such as hose demand, meets it for the required duration (2.1.2.4.5).

How does FM set density and area?

For nonstorage occupancies, DS 3-26 Table 2.3.1.10 gives one density and demand area per hazard category and ceiling height, for example 8 mm/min over 230 m² for HC-2 wet systems under 9 m. NFPA 13 has used single-point density/area for new systems since its 2022 edition, keeping the density/area curves for existing systems only.

How current does the water supply flow test need to be?

FM DS 2-0 2.6.4.6 calls for flow test data no more than 12 months old for an existing supply. DS 3-0 2.1.1.4 adds that the test should be planned in advance, taking account of day and night or summer and winter differences in public system operation, and 2.1.1.3 advises against reducing public main pressure below 1.38 bar.

Is velocity pressure included?

Not in the FM method. DS 3-0 2.1.2.3.1 notes that some methods use normal pressure, but FM uses a calculation method that does not include velocity pressure; total pressure is the most remote sprinkler pressure plus friction loss plus elevation pressure.

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Standards & References

FM Global Property Loss Prevention Data Sheet DS 3-0, Hydraulics of Fire Protection Systems, March 2010 (1.0, 2.1.1, 2.1.2; Equations 1–4, 7, 10–11, 15–16, 19, 30); related: DS 2-89, DS 2-0 (Tables 2.2.1.3.3 and 2.5.1.1.2, 2.6.4.6), DS 3-26 (Table 2.3.1.10), DS 3-7 (2.4); NFPA 13 (2025) Table 28.2.4.8.1.