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Free · Disinfection · STP/ETP Final Stage

Chlorine Dosing Calculator

Calculate NaOCl, Ca(OCl)₂, and Cl₂ consumption, dosing pump rate, and contact tank volume for disinfection of STP and ETP final effluent.

Chlorine Dosing Parameters

Enter your flow rate, chlorine product, dose, and operating parameters.

Total daily flow through the disinfection system

Hint: Treated STP effluent reuse: 5–15 mg/L | Final polishing (post-MBR): 2–5 mg/L | Pre-chlorination: 10–30 mg/L

Residual chlorine after the contact tank; CPCB limit: ≤ 1.0 mg/L in treated effluent

CT = Residual Cl₂ × contact time. Used to size the contact tank.

Cost per litre of Sodium Hypochlorite — 12% available Cl₂ (liquid)

How to Use This Calculator

  1. 1Enter your flow rate (m³/day) and select the chlorine product — sodium hypochlorite (12%, 10%, or 5%), bleaching powder (33%), HTH (65%), or chlorine gas (100%).
  2. 2Set the Cl₂ dose (total applied) and target residual — the dose hint shows typical ranges for common STP applications.
  3. 3Choose a CT target (mg/L·min) based on your required log reduction — the calculator sizes the contact tank volume automatically.
  4. 4Enter the unit price for your chemical to get monthly and annual cost estimates for budgeting and opex analysis.

Formulas Used

Cl₂ demand (mg/L) = Cl₂ dose (mg/L) − Cl₂ residual (mg/L)

Cl₂ (kg/day) = Flow (m³/day) × Dose (mg/L) ÷ 1000

NaOCl (L/day) = Cl₂ (kg/day) × 1000 ÷ [available_Cl₂% ÷ 100 × density (kg/L) × 1000]

Dry product (kg/day) = Cl₂ (kg/day) ÷ (available_Cl₂ fraction)

Contact tank (m³) = Flow (m³/hr) × CT (mg/L·min) ÷ C_residual (mg/L) ÷ 60

Pump rate (L/hr) = NaOCl (L/day) ÷ operating hours per day

Monthly cost (₹) = Product per day × 30 × unit price

Typical Chlorine Doses by Application

ApplicationDose (mg/L)Residual TargetNotes
Final STP effluent — reuse5–150.5–1.0 mg/LAfter secondary treatment
Post-MBR or tertiary filtration2–50.2–0.5 mg/LHigh quality feed
STP effluent — river discharge3–80.2–0.5 mg/LCheck consent conditions
Cooling tower makeup2–50.5–1.5 mg/LBiofouling control
Pre-chlorination (raw sewage)10–30Odour/septicity control
Swimming pool / recreation1–30.5–2.0 mg/LPer IS 3329

Always verify dose by chlorine demand test on your specific effluent. Actual demand varies with BOD, ammonia, turbidity, pH, and temperature.

Chlorine Disinfection in Wastewater Treatment: Cl₂ Demand, Dose, and Residual

Chlorine demand: what consumes your dose

When chlorine is added to treated wastewater, it does not immediately become available for disinfection. A portion of the dose is consumed by the chlorine demand of the effluent — the reducing substances present in the water that react with and deplete active chlorine before any residual builds up. The main contributors to chlorine demand are residual BOD and organic matter, ammonia nitrogen (NH₃-N), iron and manganese, nitrite, and hydrogen sulphide. Only the dose in excess of the total chlorine demand becomes the free residual chlorine that provides ongoing disinfection. This is why the dose is always greater than the residual: Dose = Demand + Residual.

Breakpoint chlorination and ammonia

Ammonia in treated sewage reacts with chlorine to form chloramines (combined chlorine), which have weaker disinfection power than free HOCl. As the chlorine dose is increased above the combined chlorine equivalent, a breakpoint is reached where chloramines are destroyed and free residual chlorine begins to accumulate. Chlorination past this breakpoint — breakpoint chlorination — is required to achieve a true free chlorine residual. For nitrified secondary effluent (low ammonia), the breakpoint dose is low and the transition is sharp. For unnitrified effluent with high NH₃-N, reaching the breakpoint requires approximately 7.6 mg Cl₂ per mg NH₃-N — which can significantly increase the required dose and chemical cost.

CT value and pathogen inactivation

The Chick-Watson CT concept (concentration × time) is the standard framework for quantifying disinfection efficacy. CT (mg/L·min) = Residual Cl₂ concentration (mg/L) × effective contact time (min). Required CT values for treated sewage at pH 7, 20°C are approximately 3–5 mg/L·min for 2-log virus inactivation and 15–25 mg/L·min for 4-log coliform reduction. These values increase at higher pH and lower temperature. For UV disinfection as an alternative or supplement to chlorination, see our UV disinfection system page.

Sodium Hypochlorite vs. Calcium Hypochlorite vs. Chlorine Gas

Sodium hypochlorite (NaOCl) — liquid, 5–12%

The most widely used disinfectant for small and medium STPs across India. Supplied as a clear to pale-yellow liquid, typically at 10–12% available chlorine. Handled with standard HDPE dosing tanks and diaphragm metering pumps — no specialist equipment or gas handling certification required. The main operational concern is shelf-life: NaOCl degrades in sunlight, heat, and on contact with metal ions. Store in covered, opaque HDPE tanks in a cool, shaded location. At 12% strength, expect 1–2% available Cl₂ loss per month at ambient temperatures; at 5% (household grade), degradation is slower but available chlorine per litre is lower.

Calcium hypochlorite — bleaching powder (33%) and HTH (65%)

Dry granular products. Bleaching powder (Ca(OCl)₂ · CaCl₂ · Ca(OH)₂) is the lower-grade form at ~30–35% available Cl₂, widely available and low-cost in India. HTH (High-Test Hypochlorite) is the stabilised granular form at 65–70% available Cl₂ — more expensive but with longer shelf life and lower bulk weight per kg of Cl₂. Both must be dissolved in water before dosing; the resulting solution is then metered in. Calcium hypochlorite raises hardness of treated water and produces calcium carbonate deposits — this can be a concern in reuse systems with membranes or heat exchangers.

Chlorine gas (Cl₂) — 100% available Cl₂

The most economical choice at large scale (above 5–10 MLD flow). Supplied in pressurised cylinders or tonners. Requires a vacuum-operated chlorinator (gas feed equipment), leak detection system, emergency gas scrubber, and trained operators. Subject to Factories Act hazardous substance provisions and MSIHC Rules 1989 for storage above threshold quantities. Cl₂ gas is denser than air — leaks accumulate at floor level and in confined spaces, requiring SCBA for emergency response. Not recommended for small residential STPs, hospitals, or sites without dedicated operator staff. Refer to IS 4023 for installation safety requirements.

Calculating equivalent doses between product forms

All chlorine products are compared on an equivalent active Cl₂ basis: 1 kg Cl₂ (gas) ≡ 1/0.12 × 1/1.17 ≈ 7.1 L of NaOCl (12%) ≡ 1/0.65 ≈ 1.54 kg HTH (65%) ≡ 1/0.33 ≈ 3.03 kg bleaching powder (33%). This calculator performs these conversions automatically for any selected product form.

CT Values and Contact Tank Design

CT requirements for treated sewage

Per Metcalf & Eddy (5th ed.) and AWWA Chlorination Practice, typical CT requirements for secondary treated sewage at pH 7, 20°C are: 2-log Giardia inactivation: CT ~15–30 mg/L·min; 2-log virus inactivation: CT ~3–5 mg/L·min; 4-log total coliform reduction: CT ~15–25 mg/L·min. These values increase at pH above 7.5 (more OCl⁻, less active HOCl) and at lower temperatures (slower inactivation kinetics). For Indian STP conditions (pH 7–7.5, 25–35°C), a design CT of 20–25 mg/L·min is commonly used for final effluent reuse.

Plug-flow vs. CFSTR contact tanks

The CT calculation assumes plug-flow conditions where every parcel of water receives the same exposure time. In practice, all contact tanks exhibit some short-circuiting, reducing the effective CT below the theoretical value. The baffling efficiency factor T₁₀/HRT (ratio of 10th-percentile residence time to mean HRT) accounts for this: well-baffled plug-flow tanks achieve T₁₀/HRT of 0.5–0.7; unbaffled tanks as low as 0.1–0.3. For reliable disinfection, design for T₁₀/HRT ≥ 0.5 using serpentine baffles or over-and-under baffling. The contact tank volume from this calculator is the theoretical value — multiply by 1/(T₁₀/HRT) to get the actual required volume. For UV disinfection as an alternative to chlorination contact tanks, see the UV disinfection system calculator. For full STP design context, visit our sewage treatment plant (STP) page.

Chlorination in Indian STPs and ETPs — Regulatory Context

CPCB discharge standards for residual chlorine

The Central Pollution Control Board (CPCB) specifies that residual chlorine in treated effluent for inland surface water discharge should not exceed 1.0 mg/L. Free chlorine above this limit is toxic to aquatic organisms, particularly fish, even at short exposure times. State PCBs may impose lower limits — check your Consent to Operate (CTO) conditions. For discharge to ecologically sensitive receiving waters (wetlands, rivers with fisheries), dechlorination using sodium thiosulphate or sodium bisulphite before discharge is required.

Post-UV chlorination for reuse systems

A common practice in Indian STPs serving high-rise residential complexes and commercial buildings is UV disinfection for primary pathogen inactivation followed by a small chlorine dose (1–3 mg/L NaOCl) to maintain a residual in the piped reuse distribution network. UV alone provides no residual protection; chlorination alone requires a large contact tank. The combination achieves both log-reduction targets and residual protection with minimal contact tank volume and chemical dose.

Chlorine gas safety regulations in India

Chlorine gas is classified as a toxic substance under Schedule 1 of the Manufacture, Storage and Import of Hazardous Chemicals (MSIHC) Rules, 1989. Sites storing above threshold quantities (10 tonnes for chlorine) are Major Accident Hazard (MAH) units and require safety reports, emergency plans, and on-site emergency response procedures. Even below threshold quantities, the Factories Act and local SPCB rules require safe storage, leak detection, and emergency procedures. Small STP operators are strongly advised to use NaOCl or HTH rather than Cl₂ gas unless chlorinator expertise and emergency response capability are in place.

Regulatory compliance and consent conditions

Chlorination system design should be reviewed against your facility's Consent to Establish (CTE) and Consent to Operate (CTO) conditions, which specify treated effluent standards including microbiological parameters. Check our CPCB Compliance Checker to verify your STP effluent against applicable discharge standards, or contact Spans Envirotech for site-specific design support.

Frequently Asked Questions

What is the typical chlorine dose for STP treated sewage reuse?

For secondary treated STP effluent used for reuse, the typical dose is 5–15 mg/L targeting 0.5–1.0 mg/L residual. Post-MBR or tertiary filtered effluent needs only 2–5 mg/L. Verify by chlorine demand testing on your specific effluent.

How do I calculate NaOCl volume needed for my STP?

Cl₂ (kg/day) = Flow (m³/day) × Dose (mg/L) ÷ 1000. For NaOCl 12% (density 1.17 kg/L): NaOCl (L/day) = Cl₂ (kg/day) × 1000 ÷ 140.4. This calculator automates the conversion for all product forms.

What is the difference between available chlorine and free chlorine?

Available chlorine is the product specification — oxidising capacity expressed as equivalent Cl₂ (e.g., 12% for liquid NaOCl). Free chlorine is the measured residual HOCl/OCl⁻ in treated water after chlorine demand is satisfied. CPCB limits free chlorine in treated effluent to ≤ 1.0 mg/L.

How large should a chlorination contact tank be?

Volume (m³) = Flow (m³/hr) × CT (mg/L·min) ÷ Residual (mg/L) ÷ 60. For 4-log coliform reduction use CT = 20–25 mg/L·min. Apply a baffling efficiency factor (T₁₀/HRT = 0.5) to account for short-circuiting.

What CT value is required for effective disinfection of treated sewage?

At pH 7, 20°C: 2-log virus reduction needs CT ~3–5 mg/L·min; 4-log coliform reduction needs CT ~15–25 mg/L·min. For Indian STP conditions, design for CT = 20–25 mg/L·min.

Is NaOCl or chlorine gas better for a small STP?

NaOCl (12%) is recommended for small STPs — safe handling, standard HDPE tanks and metering pumps, no specialist certification. Chlorine gas is cheaper at large scale (above 5–10 MLD) but requires chlorinators, leak detection, trained operators, and MSIHC Rules compliance.

Does chlorine affect pH of treated effluent?

At typical disinfection doses, the pH effect is minor (0.1–0.3 units). NaOCl slightly raises pH; Cl₂ gas slightly lowers it. For reuse systems with pH-sensitive membranes, account for this contribution when specifying final pH control.

Need Disinfection System Design for Your STP?

Spans Envirotech designs and commissions chlorine dosing systems, UV disinfection units, and contact tanks for STPs and ETPs across India — from small residential complexes to large municipal facilities.

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