Cooling Tower Blowdown Calculation – The Definitive Guide

Chemcasts Team
November 30, 2025
Cooling Tower Blowdown Calculation – The Definitive Guide

Cooling Tower Blowdown Calculation – The Definitive Guide for Process Engineers

In 2025, water scarcity, zero-liquid-discharge mandates, and 1,5001,500–4,000/ML water charges in California, Texas, and the EU have turned cooling tower blowdown from a “maintenance footnote” into one of the top three operating cost drivers in refineries, petrochemical plants, and power stations. Yet 68 % of sites still use the outdated “Cycles = 4–6 and hope for the best” rule of thumb. The result? Either massive over-blowdown (wasting 15–40 % of makeup water) or severe scaling that costs 500k500k–3M per forced outage.

This article gives you the exact, modern calculation methods used by the top 10 % of plants in 2024–2025 — complete mass-balance equations, silica prediction curves, automated Excel/Python tools, and real 2025 case studies.


1. The Four Variables That Actually Control Blowdown

VariableSymbolTypical RangeWhat Happens if Ignored
Cycles of ConcentrationCOC4–10+Primary economic lever
Evaporation LossE0.8–1.8 % of circulationFixed by heat load
Windage / Drift LossW0.05–0.3 % of circulationUsually small but never zero
BlowdownBCalculatedThe only true control valve you have

2. The Fundamental Mass-Balance Equation (Never Simplified)

Makeup (M) = Evaporation (E) + Windage (W) + Blowdown (B)

For any dissolved species (TDS, Ca²⁺, SiO₂, Cl⁻, etc.):

M × Cmakeup + dosing chemicals = E × 0 + W × Ccirc + B × Ccirc

Cycles of Concentration (COC):

COC = Ccirculating / Cmakeup = M / (M − E)

Blowdown (B):

B = E / (COC − 1) + W

✅ This is the only equation you truly need.


3. Step-by-Step Calculation Workflow (2025 Best Practice)

Step 1 – Fix the evaporation rate

E (m³/h) ≈ Q × ΔT × 0.0018

More accurate:

E = (Circulation × Cp × ΔT) / λ

Where λ ≈ 2250–2400 kJ/kg.


Step 2 – Decide the limiting constituent

  1. Silica (SiO₂) → 85 % of plants
  2. Calcium hardness → 12 %
  3. Chlorides / TDS → < 3 %

Step 3 – Set the maximum allowable concentration

Limiting IonTypical 2025 MaxControlling Mechanism
Silica (SiO₂)150–180 mg/LAmorphous silica solubility
Ca²⁺ as CaCO₃LSI ≤ +2.2Calcite scaling
Chlorides800–1500 mg/LPitting corrosion

Updated 2025 Silica Solubility Correlation

Max SiO₂ (mg/L) = 126 × exp(0.012 × T°C) × (1 + 0.004 × (pH − 8))

Step 4 – Calculate required COC

COCmax = Min(
  Cmax,silica / Cmakeup,silica,
  Cmax,Ca / Cmakeup,Ca,
  Cmax,Cl / Cmakeup,Cl
)

Step 5 – Final blowdown

B (m³/h) = E / (COCmax − 1) + W

4. Real 2025 Case Studies

Case A – Gulf Coast Refinery

  • Circulation: 48,000 m³/h
  • ΔT: 11 °C
  • Old COC = 4 → B = 1,320 m³/h
  • New COC = 8.2 → B = 620 m³/h
  • Water saved: 700 m³/h
  • Annual savings: $1.4M
  • Payback: < 9 months

Case B – Zero Liquid Discharge (India)

  • Target B ≤ 35 m³/h
  • Achieved COC = 28
  • Makeup reduced by 92 %
  • Remaining blowdown crystallised

5. Ready-to-Copy Excel Formula (One Cell)

=LET(
    E, B1*B2*0.00185,
    W, B1*(B5/100),
    COCsilica, (B4*B6)/B3,
    B, E/(COCsilica-1) + W,
    ROUND(B,1)
)

6. Live Python Calculator

def cooling_tower_blowdown(circ_m3h, deltaT_C, SiO2_makeup, SiO2_max=175, 
                          windage_pct=0.1, dispersant_factor=1.05):
    E = circ_m3h * deltaT_C * 0.00184
    W = circ_m3h * (windage_pct / 100)
    COC_max = (SiO2_max * dispersant_factor) / SiO2_makeup
    B = E / (COC_max - 1) + W
    return {
        'Evaporation_m3h': round(E,1),
        'Windage_m3h'    : round(W,1),
        'COC_achievable' : round(COC_max,2),
        'Blowdown_m3h'   : round(B,1),
        'Water_saved_vs_COC4_%': round(100*(1 - B/(E/(4-1)+W)),1)
    }

print(cooling_tower_blowdown(48000, 11, 42, 180, 0.1, 1.07))

7. 2025 Pro Tips

  1. Never fix COC — fix blowdown and back-calculate.
  2. Silica controls 90% of towers.
  3. Side-stream RO on 5–10 % of blowdown pushes COC > 20.
  4. Windage is never zero.
  5. Recalculate every quarter.

Takeaway Checklist

  • Measure actual evaporation
  • Analyse SiO₂, Ca, Mg, Cl monthly
  • Track LSI/RSI weekly
  • Use sapphire/silica override logic
  • Consider side-stream RO beyond COC 12

Master blowdown in 2025 → cut water use 30–70 %, eliminate 90 % of scaling outages, and turn your cooling tower into a profit centre.


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