Fire Water Demand Calculations

Accurate fire water demand calculation is vital for a reliable fire-protection system. Understanding flow rate, duration, components, and standards ensures safety, compliance, and effective system design.

Understanding the Concept of Fire Water Demand

Define fire water demand and its purpose

Fire water demand refers to the quantity (flow and volume) of water that must be available to supply firefighting or cooling operations in the worst-case fire scenario within a facility or installation. The purpose is to ensure the fire-protection system can deliver sufficient water to extinguish or control fire, protect exposure equipment, meet regulatory obligations and ensure safety of people and assets.

Key terms (flow rate, duration, contingency)

  • Flow rate: typically expressed in litres per minute (LPM) or cubic metres per hour (m³/hr) — the instantaneous or sustained water rate needed in the firefighting scenario.

  • Duration: the time for which that flow must be maintained, e.g., 4 hours of cooling plus additional period of foam application as per standards like Oil Industry Safety Directorate (OISD).

  • Contingency: allowances for worst-case scenarios, simultaneous fires, exposure protection, foam systems, pump redundancy, etc. For example OISD STD-116 requires design for two major fires simultaneously in many cases.

Why accurate calculation matters for fire protection and compliance

  • Under-estimating demand can lead to insufficient water supply, pump capacity, pressure loss or network failure at a critical moment, increasing risk of damage or casualties.

  • Over-design may lead to unnecessary cost, oversized tanks or equipment, but under-design is a major non-compliance hazard and risk.

  • Standards (e.g., NFPA, OISD) and regulatory bodies expect documented calculations and justification of system capacity.

  • Good calculations support audit, insurance, engineering review and safe commissioning.

Relevant Standards and Guidelines

National and international standards (e.g., NFPA, OISD)

  • OISD-STD-116: Fire Protection Facilities for Petroleum Refineries & Oil/Gas Processing Plants — specifies flow rates, simultaneous fire basis, tank cooling, foam rates.

  • OISD-STD-117: Fire Protection Facilities for Petroleum Depots, Terminals, Pipeline Installations & Lube Oil Installations — includes sample calculation for two major fires simultaneously.

  • NFPA standards: e.g., NFPA 13 (Sprinkler Systems), NFPA 15 (Water Spray Fixed Systems), NFPA 20 (Fire Pumps), NFPA 24 (Private Fire Service Mains).

Application in different sectors (industrial, residential, storage tanks)

  • Industrial and oil & gas installations (tank farms, process plants) have higher fire-water demand scenarios and often require dedicated fire-water storage, monitors, foam, exposure cooling.

  • Residential or light commercial systems may follow sprinkler/hydrant standards and be less demanding in terms of volume, but still must meet local fire-flow standards and hydrant pressure.

  • Storage tanks (floating-roof, cone-roof) in petrochemical sectors have specific formulas and guidance in OISD for cooling/foam application.

Implications of non-compliance or under-design

  • Non-compliance with standards may lead to regulatory penalties, invalidated insurance, or operational shutdown.

  • Under-design can result in first-aid firefighting failure or uncontrolled escalation.

  • OISD guidance emphasizes that fire-water systems must be designed to fight two major fires simultaneously or the largest tank roof sinking case.

Methodology for Calculating Fire Water Demand

Identify fire hazard scenario(s) and worst-case events

Identify credible worst-case fire scenarios: largest tank on fire, two major fires simultaneously, jet fire, storage fire, process unit fire. Determine affected equipment and exposure considerations, and define the design basis (number of fires, duration).

Determine flow rate requirements (fixed systems, hose/monitors, cooling, foam)

Calculate:

  • Cooling water for tanks (e.g., 3 L/min/m² shell area for tank on fire as per OISD).

  • Foam/monitor/hose demand: fixed foam rate for rim seal area plus supplementary hydrants or monitors.

  • Include hydrant and monitor streams (e.g., 4 hydrants + 1 monitor).

Calculate storage volume and duration of supply

Multiply flow rate by duration to determine required fire-water storage (plus make-up water or reliability allowances). Example: OISD STD-117 uses design flow × 4 hours where make-up water is unavailable.

Assess pump and distribution network capacity

Ensure pumps deliver required flow and pressure (e.g., 7 kg/cm² at farthest hydrant as per OISD). Hydraulic network design must account for friction losses and provide redundancy.

Common Formulas and Empirical Approaches

Empirical formulas based on population/area (e.g., Kuichling’s, Freeman’s, Buston’s)

  • Kuichling: Q = 3182 √P (L/min)

  • Freeman: Q = 1136 × [(P/10) + 10] (L/min)

  • Buston: Q = 5663 √P (L/min)
    These are used for general municipal planning, not detailed industrial system design.

Code-based formulas tailored to asset type (e.g., tank cooling, foam application)

  • Tank cooling: π × D × H × 3 L/min/m² of shell area for tank-on-fire (OISD).

  • Foam water: rate based on rim-seal area and tank diameter per OISD tables.

How to select and apply the appropriate formula for your situation

  • Use empirical formulas for early-stage or municipal planning.

  • Use code-based formulas (OISD/NFPA) for industrial design.

  • Sum total demands (cooling + foam + monitors + hydrants) and validate against the worst-case scenario.

Fire Water Demand for Specialized Installations

Storage tanks (floating-roof, cone-roof) demand calculation

Cooling: π × D × H × 3 L/min/m² for tank on fire. Nearby tanks (within R + 30 m) use 3 L/min/m²; others 1 L/min/m².
Foam: apply as per rim-seal and surface area calculations.

Process plants / petrochemical & oil-gas installations

Includes flow for fixed spray, hydrants, monitors, and foam systems. Often requires a risk-based approach and simultaneous fire planning.

Simultaneous fires and contingency planning for major fire events

Design must consider two major fires simultaneously for large installations (OISD STD-116). Include contingency for backup pumps and make-up water.

System Components & Checklist for Implementation

Fire-water storage tank sizing and layout

Storage volume = flow × duration (+ margin). Example: 4 hours as per OISD STD-117.
Ensure separation from process area, alarms, and make-up provisions.

Fire pump selection and redundancy requirements

Pumps must provide flow and 7 kg/cm² pressure at farthest hydrant.
Include redundancy (diesel + electric drives, standby units, auto-changeover).

Pipe network, valves, monitors/hydrants — hydraulic design considerations

Looped mains, friction loss analysis, valve spacing, hydrant/monitor layout and hydraulic modeling are essential.

Verification, testing and maintenance of fire-water system

Regular pump run tests, hydrant flow checks, foam testing, and documentation per OISD.

Practical Examples and Case Studies

Walk-through of a calculation for a storage tank farm

Example: Floating-roof tank 79 m dia × 14.4 m height.

  • Cooling: 3 L/min/m² → 10,721 L/min = 643 m³/hr

  • Adjacent tanks: 1 L/min/m² → 215 m³/hr

  • Total ≈ 1,369 m³/hr including foam and streams.

Example for a process plant including monitors, fixed spray, foam

Risk-based approach (NFPA/API) calculates maximum flow from jet/pool fire, spray systems, hydrants, and monitors to size pumps and storage.

Lessons learned and typical pitfalls

  • Ignoring simultaneous fires.

  • Missing exposure cooling for nearby tanks.

  • Excluding foam/monitor demand.

Not updating calculations when facility scope changes.

Common Mistakes and How to Avoid Them

Under-estimating duration or simultaneous fires

Always apply correct design duration (4 hours + foam) and simultaneous fire requirement per OISD STD-116/117.

Ignoring hose/monitor demand or foam system requirements

Do not focus only on sprinklers—include monitors, hoses, and foam systems.

Overlooking maintenance, testing, or design margin

Ensure redundancy, margin, and testing programs are in place.

Summary & Actionable Take-aways

Key stresses to ask/design for (flow, duration, reliability)

  • Define worst-case scenario.

  • Confirm flow rate & duration.

  • Check simultaneous fire requirement.

  • Verify storage, pumps, network, foam, and redundancy.

Checklist for engineers/owners to ensure adequacy

  1. Define design basis and hazards.

  2. Calculate flow rates (cooling, foam, hydrant, monitor).

  3. Compute storage = flow × duration + margin.

  4. Size pumps & piping for flow & pressure.

  5. Validate with NFPA/OISD.

  6. Review redundancy, make-up water, and maintenance.

  7. Test regularly and update calculations when scope changes.

Next steps: audits, simulation, revisiting calculation when scope changes

Perform audits, hydraulic simulations, and recalculate after plant expansion or layout change. Maintain full documentation for review and compliance.

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Frequently Ask Question

Typically 4 hours based on design flow when no make-up water is available (OISD STD-117).

Include foam or spray for hydrocarbon fires, per OISD/NFPA guidance.

Kuichling’s, Freeman’s, and Buston’s formulas are used for population-based estimation

No. OISD STD-116 requires two major fires simultaneously for large installations.

After any facility expansion, hazard reclassification, or major modification.

Ignoring simultaneous fires, under-estimating foam/hose demand, or missing redundancy and testing.

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