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Disinfectant Dosing

Chlorine, chlorine dioxide and peracetic acid each have a specific niche in water and wastewater disinfection. This page covers the chemistry, CT value targets, disinfection byproduct (DBP) trade-offs, residual measurement and dosing-system design for each.

The CT Concept

Disinfection is a product of concentration and time, not just dose.

All chemical disinfectants achieve pathogen inactivation as a function of disinfectant concentration C (mg/L) multiplied by contact time t (minutes) at a given temperature and pH. The product C·t (in mg·min/L) is called the CT value. Each disinfectant has published CT values for various pathogens at 99% (2-log) and 99.9% (3-log) inactivation; design engineers must size the contact tank, target residual concentration and operating pH to deliver the required CT in worst-case conditions (low temperature, high pH, low concentration). Drinking-water regulators specify minimum CT values for Giardia, Cryptosporidium and viruses; wastewater consent typically targets E. coli and faecal coliform counts. CT calculations are central to disinfection compliance.

Sodium Hypochlorite (NaOCl)

The most widely-deployed disinfectant, supplied as 10–15% w/v solution. Hypochlorite is convenient and relatively safe vs chlorine gas, but degrades over weeks of storage — especially in heat and sunlight.

  • Typical dose: 1–10 mg/L as Cl₂ for drinking water; up to 50 mg/L for industrial
  • Effective pH window: 6.5–8.0 (HOCl form dominates — the more germicidal form)
  • CT for Giardia (1-log): 36 mg·min/L at pH 7, 5°C
  • DBPs: trihalomethanes (THMs), haloacetic acids (HAAs) from organic precursors
  • Degradation: 2–5% per month in cool storage; 10%+ in summer

Best for: drinking-water primary disinfection, secondary disinfection (residual), wastewater effluent before discharge, water reuse.

Hypochlorite handling reality

Decomposition products

NaOCl decomposes to chlorate (ClO₃⁻) and chloride (Cl⁻) over time. Chlorate is regulated (UK: 0.7 mg/L drinking-water limit). Hot, sunlit storage accelerates decomposition.

On-site generation (OSEC)

For sites with high consumption or remote location, electrolytic generation of 0.8% NaOCl from brine eliminates bulk delivery, chlorate accumulation and storage risks. Capital expenditure higher; Operating expenditure lower at large scale.

Storage life

Cool, dark storage extends shelf life. Tank volume typically sized for 7–14 days’ consumption to ensure freshness.

Chlorine Dioxide (ClO₂)

Chlorine dioxide is a strong selective oxidant generated on site from sodium chlorite (NaClO₂) + acid, or NaClO₂ + sodium hypochlorite. It cannot be stored in bulk and must be produced as needed.

  • Typical dose: 0.1–1.0 mg/L for drinking water; up to 5 mg/L for industrial
  • Effective pH window: 4–10 (broad — works at high pH where chlorine doesn’t)
  • CT for Giardia: 7–15 mg·min/L at 5°C (much lower than chlorine)
  • DBPs: chlorite (ClO₂⁻) and chlorate (ClO₃⁻) — THMs/HAAs negligible
  • Inactivates Cryptosporidium (chlorine does not)

Best for: high-pH source water, biofilm control in distribution networks, hospital water systems, food processing, refinery cooling water.

ClO₂ generation comparison

MethodReagentsYieldUse case
Chlorine-chloriteNaClO₂ + Cl₂ gas90–95%Large plants with Cl₂ gas
Acid-chloriteNaClO₂ + HCl80–85%Mid-size; safer than gas Cl₂
ElectrolyticNaCl + electricity30–60% (mixed oxidant)Small / remote
Two-precursor (NaClO₂ + NaOCl)Both as liquids80–90%Most common for industrial

Peracetic Acid (PAA)

Peracetic acid (CH₃COOOH) is a strong oxidising disinfectant supplied as 5–15% w/w solution stabilised with acetic acid and hydrogen peroxide. It is widely used in food, dairy and pharmaceutical industries for surface and CIP disinfection and is gaining ground in wastewater effluent disinfection.

  • Typical dose: 1–15 mg/L for wastewater effluent; up to 50 mg/L for CIP
  • Effective pH window: 3–8 (acidic preferred)
  • CT for total coliform (2-log): 10–25 mg·min/L
  • Decomposition: acetic acid + water + oxygen (food-safe by-products)
  • DBPs: virtually none; no THM/HAA formation

Best for: food/dairy/brewery CIP, wastewater effluent before discharge to sensitive waters, hospital effluent, low-DBP applications.

Why PAA is gaining ground

Wastewater treatment plants increasingly choose PAA over chlorine because: no THM/HAA formation, no need for downstream dechlorination, food-safe degradation products, ambient pH operation.

Cost & storage

PAA is ~3–5x more expensive per kg active disinfectant vs hypochlorite. Storage stable for ~6–12 months refrigerated; less in warm warehouses. Vapours irritate eyes & lungs; ventilation required.

Choosing the Right Disinfectant

CriterionNaOClClO₂PAAUVO₃
Capital costLowMedLowMed-HighHigh
Operating requirementLowMedMed-HighMedHigh
Crypto inactivationPoorGoodModerateExcellentExcellent
Distribution residualYesYesShortNoNo
DBP riskTHM, HAAClO₂⁻ ClO₃⁻NegligibleNoneBromate (if Br present)
Effective pH6.5–8.04–103–8n/a5–9
Best forDrinking water, generalBiofilm, high pHFood, CIP, wastewaterWastewater, reuseTertiary, ozone+BAC

For information on UV and ozone systems, see the UV disinfection and ozonation pages.

Dosing System Design

Storage Tank

HDPE or FRP for NaOCl/PAA; PE or PP for chlorite. Vented to scrubber; bunded to 110%; UV-shielded for hypochlorite.

Temperature Control

Hypochlorite degradation doubles per 10°C rise. Insulated tanks & pipework essential in summer; consider chilled storage for high-consumption sites.

Dosing Pumps

Solenoid or motorised diaphragm; PVDF or PTFE wetted parts. Pulsation dampener on discharge. Auto-prime feature for solenoid pumps.

Contact Tank

Sized for required CT at minimum-temperature, maximum-flow scenario. Baffled to approach plug-flow (T₁₀/T > 0.5). Outlet sample tap for residual measurement.

Residual Monitor

Continuous online amperometric or DPD-colorimetric analyser. Trends back to SCADA. Loop-back to dosing pump speed control via PID.

Safety

Eyewash + emergency shower within 10 m. Gas detection for chlorine gas systems. PPE storage. Bund leak detection. Spill kit. Cl₂ gas: scrubber + bypass alarm.

Residual Monitoring & Closed-Loop Control

Match dose to demand: too little fails disinfection; too much costs money and creates DBPs.

Disinfection demand varies with temperature, organics, ammonia and flow. Fixed-dose operation either over-doses on cold/clear days or under-doses during peak. Modern installations use closed-loop residual control:

  • Flow-paced + trim: dosing pump speed proportional to flow; residual analyser fine-tunes via PID
  • Setpoint-residual: pump speed driven directly by residual deviation from setpoint
  • Cascaded: ammonia + chlorine measured before contact tank; predicted breakpoint informs dose
  • Distribution-network feedback: remote chlorine analysers in the network feed back to the central plant

Modern plants commonly save 15–30% chemical requirement vs fixed-dose, plus material DBP reductions.

Read more on dosing control strategy

Residual target by application

Drinking-water (entry to network)0.5–1.0 mg/L FC
Drinking-water (network end)0.1–0.3 mg/L FC
Hospital water0.5–1.5 mg/L FC or ClO₂
Wastewater effluent (consent)typically <0.5 mg/L FC (or PAA-based)
Cooling tower (biofilm control)0.5–2.0 mg/L FC continuous, shock at 3–5
Food & dairy CIP50–200 mg/L FC during cycle

Disinfection By-Products & Mitigation

Every chemical disinfectant produces some by-products by reaction with natural organic matter (NOM). Some are regulated; all should be minimised.

  • THMs (chloroform, BDCM, DBCM, bromoform): from chlorine + NOM
  • HAAs (mono/di/tri-chloroacetic acid): from chlorine + NOM
  • Chlorite / chlorate: from chlorine dioxide and degraded hypochlorite
  • Bromate: from ozone + bromide
  • NDMA: from chloramines + dimethylamine precursors

Mitigation strategies: remove NOM upstream (coagulation + GAC), switch to lower-DBP disinfectant (PAA, UV, ClO₂), reduce contact time at high chlorine concentration, replace breakpoint chlorination with monochloramine.

GAC for DBP Precursor Removal

Granular activated carbon removes 30–70% of TOC ahead of chlorination, reducing THM/HAA formation potential dramatically. The single most effective DBP-mitigation step.

Read about GAC for DBP control

Related Pages

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