HVAC Psychrometric Chart Practice Questions Engineering Analysis: Hydraulic Calculations

Engineering Analysis: Hydraulic Calculations

Hydraulic design methodology for fire sprinkler system compliant with BS EN 12845

Technical Document

August 2023

This analysis details the hydraulic calculation methodology for the fire sprinkler system, following BS EN 12845 standards.

1Static Pressure Calculation Methodology

Static Pressure Fundamentals

The static pressure difference between two points in the pipework is calculated using the fundamental fluid statics equation:

p = h × ρ × g

Where:
p = Pressure (Pa)
h = Height difference (m)
ρ = Density of water (1000 kg/m³)
g = Gravitational acceleration (9.81 m/s²)

This simplifies to a practical engineering formula:

p = 0.0981 × h (bar)

Design Assumptions:

  • Elevation of distribution pipes relative to FFL: 3.35m
  • Elevation of alarm valve relative to FFL of LL3: 1.20m

Critical Calculation: The highest static head occurs at the 6th floor:

Elevation difference: 52.95m (6F MSL) - 8.50m (LL3 MSL) = 44.45m
Sprinkler piping elevation: 44.45m + 3.35m = 47.80m
Relative to alarm valve: 47.80m - 1.20m = 46.60m
Static head: 0.0981 × 46.60 = 4.571 bar

2Static Head Gain Concept

Static Head Gain Engineering Principle

A key engineering concept applied in this design is the static head gain for secondary design points at lower elevations.

Static Head Gain = Static Head at Highest Point - Static Head at Current Point

This gain represents available pressure that can be "consumed" as additional frictional losses in pipe sizing calculations for lower floors.

Example: Static head gain for LL3:

4.571 bar (6F) - 0.211 bar (LL3) = 4.360 bar

This approach allows for smaller pipe diameters on lower floors while maintaining adequate pressure throughout the system.

3Pipe Frictional Loss Calculations

Hazen-Williams Formula Application

Frictional pressure losses are calculated using the Hazen-Williams formula:

p = (6.05 × 10⁵ / (C¹.⁸⁵ × d⁴.⁸⁷)) × L × Q¹.⁸⁵

Where:
p = Pipe frictional loss (bar)
C = Pipe roughness coefficient (120 for galvanized steel)
d = Mean internal diameter of pipe (mm)
L = Equivalent length of pipe and fittings (m)
Q = Flow rate (L/min)

This is simplified to:

p = k × L × Q¹.⁸⁵

Where k is a constant for pipe size, type, and condition.

Nominal Diameter (mm) k Value Standard Reference
251.22 × 10⁻⁵BS 5306-2:1990, Table 36
322.93 × 10⁻⁶
401.33 × 10⁻⁶
504.09 × 10⁻⁷
651.11 × 10⁻⁷
804.97 × 10⁻⁸
1001.35 × 10⁻⁸
1501.91 × 10⁻⁹

4Equivalent Length Method for Fittings

Fitting Loss Calculations

Pressure losses through fittings are calculated using equivalent lengths of straight pipe.

Nominal Diameter (mm) 90° Elbow (m) Tee/Cross (Branch Flow) (m) Gate Valve (m) Standard Reference
651.893.810.51BS 5306-2:1990, Table 37
802.374.750.63
1003.046.100.81
1504.308.611.13

5Design Criteria for Pipe Sizing

Fundamental Design Criterion

The fundamental design criterion for pipes upstream of the most remote design point:

Frictional Loss ≤ 0.5 bar + Static Head Gain (at 1000 L/min flow rate)

Standard: BS EN 12845, Clauses 13.3.4.2 and 13.3.4.3

This ensures adequate pressure is available at all design points while optimizing pipe sizes.

6Iterative Design Approach

Iterative Calculation Process

The design follows an iterative process:

  1. Start with smallest permissible pipe size (DN65mm)
  2. Calculate total frictional loss at 1000 L/min
  3. If (Frictional Loss - Static Head Gain) > 0.5 bar, increase pipe size
  4. Repeat process until criterion is met

Example from 6th Floor Calculation:

Ø150mm pipe: 0.095 bar
Ø100mm pipe: 0.397 bar
Total: 0.492 bar < 0.5 bar → ACCEPTABLE

7Pipe Sizing Strategy Across Floors

Strategic Pipe Sizing Approach

The design employs a strategic approach to pipe sizing:

  • Upper floors: Larger diameters (DN150mm, DN100mm)
  • Lower floors: Smaller diameters (DN65mm, DN80mm)

This approach efficiently utilizes the available static head gain on lower floors to reduce pipe sizes while maintaining system performance.

Floor Level Main Distribution Pipe Diameter Zone Subsidiary Stop Valve Diameter
LL3 to 2F80mm80mm
3F to 4F100mm100mm
5F to 6F150mm150mm

8Computational Methodology

Calculation Implementation

The complex iterative calculations were implemented using MS Excel with:

  • Named variables for all parameters
  • Predefined k-values and equivalent lengths
  • Formulae replicating the Hazen-Williams equation
  • Automated calculation of static head gains

This approach provided flexibility to accommodate design changes and ensured accuracy in calculations.

9Verification of Design Compliance

Design Verification

The final design was verified against the criterion for all design points:

Floor Design Point Frictional Loss (bar) Static Head Gain (bar) Difference (bar) Compliance
LL3 V 4.755 4.361 0.394 ✓ Compliant
6F B 0.487 0.000 0.487 ✓ Compliant
3F G 1.905 1.442 0.463 ✓ Compliant

All design points show compliance with the requirement that the difference does not exceed 0.5 bar.

10Engineering Summary

Key Engineering Achievements

The hydraulic design successfully achieves:

  • Optimal pipe sizing across all floors
  • Compliance with BS EN 12845 requirements
  • Efficient use of static head gain principle
  • Verification of pressure adequacy at all design points
  • Cost-effective solution through strategic pipe sizing
The hydraulic calculations demonstrate a robust engineering approach that ensures system reliability while optimizing material usage and costs.