2.4 Disinfection Chemistry, CT Calculations & Disinfection Byproducts

Key Takeaways

  • Free available chlorine in water exists in a pH-dependent equilibrium between hypochlorous acid (HOCl, 80-100x more germicidal) and hypochlorite ion (OCl⁻), with HOCl dominating at pH < 7.5.
  • Breakpoint chlorination progresses through four zones: destroying inorganic demand, forming combined chloramines, destroying chloramines at the breakpoint (Cl2:NH3-N ratio ~ 7.6:1 to 10:1), and establishing free available chlorine residual.
  • Disinfection compliance is verified via the CT equation (CT = Residual Concentration in mg/L × T10 Contact Time in minutes), where T10 incorporates basin baffling factors (BF from 0.1 to 1.0) under peak hourly flow.
  • Stage 2 Disinfectants and Disinfection Byproducts (D/DBP) Rule enforces Maximum Contaminant Levels (MCLs) based on Locational Running Annual Averages (LRAA): Total Trihalomethanes (TTHM) at 0.080 mg/L (80 µg/L) and Haloacetic Acids (HAA5) at 0.060 mg/L (60 µg/L).
  • EPA Enhanced Coagulation mandates Step 1 Total Organic Carbon (TOC) removal percentage targets (15% to 50%) based on raw water TOC and alkalinity matrix to eliminate DBP precursors before primary chlorination.
Last updated: August 2026

Primary Chemical Disinfectants & Properties

Disinfection is the selective destruction or inactivation of pathogenic microorganisms (bacteria, viruses, and protozoan cysts). Disinfection must achieve primary inactivation at the treatment facility and maintain a secondary protective residual throughout the distribution network.

Disinfectant Types & Operational Characteristics

DisinfectantPhysical Form & Available StrengthReaction Chemistry & PropertiesOperational Advantages & Limitations
Chlorine Gas ($Cl_2$)Liquefied compressed gas ($100%$ available chlorine) in $150\text{-lb}$ cylinders or $1\text{-ton}$ containers.Hydrolyzes instantly to $HOCl + H^+ + Cl^-$; highly acidic; consumes $1.1-1.4\text{ mg/L}$ alkalinity per $\text{mg/L } Cl_2$.Lowest chemical cost; gas is $2.5\times$ denser than air; lethal hazard; requires vacuum chlorinators and fusible plugs ($158-165^\circ\text{F}$).
Sodium Hypochlorite ($NaOCl$)Yellow liquid solution ($12.5%$ available chlorine by weight, $\sim 125\text{ g/L}$).Strongly basic ($pH,11-13$); adds minor hydroxide alkalinity.Safer than gas; degrades over time with heat, UV light, and metal contact into chlorate ($NaClO_3$) and oxygen.
Calcium Hypochlorite ($Ca(OCl)_2$)Dry white granules/tablets ($65-70%$ available chlorine).Dissolves to release $HOCl + OCl^- + Ca^{2+}$; raises pH and calcium hardness.Stable dry shelf life; high fire/explosion risk if contaminated with organic oils; creates scaling in feed pumps.
Chloramines ($NH_2Cl$)Formed on-site by dosing chlorine and ammonia ($NH_3$) at $4:1\text{ to }5:1;Cl_2:N$ ratio at $pH,7.5-8.5$.Combined chlorine; weak oxidizer.Extremely stable in distribution systems; minimizes TTHM/HAA5 formation; weak disinfectant against Giardia and Cryptosporidium.
Chlorine Dioxide ($ClO_2$)Synthetic gas generated on-site: $2NaClO_2 + Cl_2 \rightarrow 2ClO_2 + 2NaCl$.True dissolved gas; selective oxidant; does not hydrolyze; unaffected by pH ($4-10$).Destroys phenolic tastes/odors; does not form THMs/HAAs; highly effective against Cryptosporidium; Chlorite ($ClO_2^-$) byproduct $\text{MCL} = 1.0\text{ mg/L}$.
Ozone ($O_3$)Unstable gas generated on-site via electrical corona discharge ($6-20\text{ kV}$) in dry oxygen.Extremely powerful oxidant; attacks cell membranes directly.Rapid inactivation of Cryptosporidium and Giardia; zero distribution residual; converts bromide ($Br^-$) to bromate ($BrO_3^-, \text{MCL} = 0.010\text{ mg/L}$).
Ultraviolet (UV)Electromagnetic radiation at $254\text{ nm}$ germicidal wavelength from mercury vapor lamps.Photochemical dimerization of microbial thymine DNA/RNA, halting cellular replication.Extremely potent against Cryptosporidium at low doses ($5-15\text{ mJ/cm}^2$); zero chemical DBPs; zero residual; high dose ($186\text{ mJ/cm}^2$) required for Adenovirus.

Aqueous Chlorine Chemistry & pH Equilibria

When chlorine gas ($Cl_2$) or hypochlorite ($NaOCl / Ca(OCl)_2$) dissolves in water, it undergoes two fundamental chemical reactions:

1. Hydrolysis to Hypochlorous Acid

Cl2+H2OHOCl+H++Cl(Instantaneous, <0.1 second)Cl_2 + H_2O \rightleftharpoons HOCl + H^+ + Cl^- \quad (\text{Instantaneous, } < 0.1\text{ second})

2. Temperature- and pH-Dependent Dissociation

Hypochlorous acid ($HOCl$) is a weak acid that partially dissociates into the hypochlorite ion ($OCl^-$):

HOClH++OCl(pKa=7.53 at 25C)HOCl \rightleftharpoons H^+ + OCl^- \quad (pK_a = 7.53 \text{ at } 25^\circ\text{C})

The sum of $[HOCl] + [OCl^-]$ is defined as Free Available Chlorine (FAC).

   100% HOCl |********************\                                  
             |                     \                                 
    75% HOCl |                      \                                
             |                       \  <-- pH 7.5 (50% HOCl / 50% OCl-)
    50% HOCl |                        \                              
             |                         \                             
    25% HOCl |                          \                            
             |                           \******************** 100% OCl-
      0%     +-------+-------+-------+-------+-------+-------+-------
            pH 5    pH 6    pH 7   pH 7.5   pH 8    pH 9    pH 10
  • At pH 6.0: $\sim 97%;HOCl$ and $3%;OCl^-$
  • At pH 7.5: $\sim 50%;HOCl$ and $50%;OCl^-$
  • At pH 8.0: $\sim 22%;HOCl$ and $78%;OCl^-$
  • At pH 9.0: $\sim 3%;HOCl$ and $97%;OCl^-$

Germicidal Kinetic Significance: Hypochlorous acid ($HOCl$) is an uncharged, neutral molecule structurally similar to water ($H_2O$), allowing it to rapidly penetrate the lipid cell membranes of bacteria and viruses to oxidize internal enzyme systems. The hypochlorite ion ($OCl^-$) carries a negative electrical charge and is electrostatically repelled by the negative cell wall. Consequently, $HOCl$ is 80 to 100 times more effective as a germicide than $OCl^-$. As treated water pH rises above $7.5$, chlorine disinfection potency drops exponentially, requiring higher doses or longer contact times.


Breakpoint Chlorination Dynamics

When chlorine is added to raw water containing reducing inorganics and ammonia ($NH_3$), it reacts along the classic Breakpoint Chlorination Curve:

  Residual Chlorine (mg/L)
     |
     |                                      / (Zone 4: Free Available Residual)
     |              C (Peak Combined)      /  (HOCl + OCl-)
     |             /\                     /
     |            /  \                   /
     |           /    \ (Zone 3)        /
     |   (Zone 2)/     \               /
     |          /       \             / 
     | (Zone 1)/         \           /  
     +--------+-----------+---------+----------------------------->
     0        A           B         D (BREAKPOINT)      Chlorine Dose (mg/L)

The Four Zones of Breakpoint Chlorination

  1. Zone 1: Inorganic Demand (0 to Point A): Chlorine reacts immediately with reducing inorganic compounds: ferrous iron ($Fe^{2+}$), manganous manganese ($Mn^{2+}$), hydrogen sulfide ($H_2S$), and nitrite ($NO_2^-$). Chlorine is reduced to chloride ($Cl^-$); zero chlorine residual is established.
  2. Zone 2: Combined Chlorine Formation (Point A to Point C): Chlorine reacts with ammonia-nitrogen ($NH_3\text{-}N$) to form inorganic chloramines:

NH3+HOClNH2Cl (Monochloramine)+H2ONH_3 + HOCl \rightarrow NH_2Cl \text{ (Monochloramine)} + H_2O NH2Cl+HOClNHCl2 (Dichloramine)+H2ONH_2Cl + HOCl \rightarrow NHCl_2 \text{ (Dichloramine)} + H_2O

The residual measured is entirely Combined Available Chlorine. Peak combined residual occurs at Point C ($Cl_2:NH_3\text{-}N$ weight ratio $\approx 5:1$). 3. Zone 3: Chloramine Destruction (Point C to Point D): Adding chlorine beyond the $5:1$ ratio causes chlorine to oxidize chloramines into nitrogen gas ($N_2$), nitrous oxide ($N_2O$), and hydrochloric acid:

2NH2Cl+HOClN2+3HCl+H2O2NH_2Cl + HOCl \rightarrow N_2\uparrow + 3HCl + H_2O

During this reaction, intermediate nitrogen trichloride ($NCl_3$, trichloramine) forms at $pH < 7.5$, creating foul, pungent chemical odors. Total residual drops sharply to its minimum at Point D (The Breakpoint). 4. Zone 4: Free Available Residual (Past Point D): Once all ammonia is fully oxidized (at a stoichiometric $Cl_2:NH_3\text{-}N$ weight ratio of $7.6:1\text{ to }10:1$), the breakpoint is reached. Any additional chlorine added beyond Point D exists $100%$ as Free Available Chlorine ($HOCl + OCl^-$), increasing on a direct $1:1$ ratio with added dose.

Total Chlorine Residual=Free Chlorine Residual+Combined Chlorine Residual\text{Total Chlorine Residual} = \text{Free Chlorine Residual} + \text{Combined Chlorine Residual} Chlorine Demand=Chlorine DoseTotal Chlorine Residual\text{Chlorine Demand} = \text{Chlorine Dose} - \text{Total Chlorine Residual}


CT Calculations & Pathogen Inactivation Standards

Under the EPA Surface Water Treatment Rule (SWTR), disinfection adequacy is quantified by the $CT$ Concept:

CTcalc=C×T10CT_{\text{calc}} = C \times T_{10}

Where:

  • $C$ = Free chlorine (or other disinfectant) residual concentration measured at the contact chamber effluent in $\text{mg/L}$.
  • $T_{10}$ = The effective contact time in minutes during which exactly $90%$ of the water remains in the basin at peak hourly flow ($Q_{\text{peak}}$), accounting for hydraulic short-circuiting.

Basin Baffling Factors ($BF$) & $T_{10}$ Determination

T10=θ×BF=(Basin Volume (gallons)Peak Hourly Flow (gpm))×BFT_{10} = \theta \times BF = \left(\frac{\text{Basin Volume (gallons)}}{\text{Peak Hourly Flow (gpm)}}\right) \times BF

Baffling ClassificationBaffle Factor ($BF$)Physical Basin Description
Unbaffled (Poor)$0.10$Open circular or rectangular tank; common inlet/outlet; severe short-circuiting.
Poor Baffling$0.30$Single dividing wall; minimal internal turning baffles.
Average Baffling$0.50$Intermediate intra-basin baffles; standard clarifier configuration.
Superior Baffling$0.70$Serpentine (labyrinth) baffled clearwell with length-to-width ratio $> 40:1$.
Perfect Plug Flow$1.00$Long transmission pipeline with no back-mixing.

SWTR Log-Inactivation Compliance

Surface water systems must achieve total multi-barrier pathogen reduction credits:

  • Giardia lamblia: $3.0\text{-log (}99.9%\text{)}$ removal/inactivation.
  • Viruses: $4.0\text{-log (}99.99%\text{)}$ removal/inactivation.
  • Cryptosporidium: $2.0\text{-log to }5.5\text{-log}$ reduction under LT2ESWTR.

In a conventional filtration plant, regulatory rules award $2.5\text{-log}$ Giardia credit and $2.0\text{-log}$ Virus credit for coagulation, sedimentation, and filtration. The remaining $0.5\text{-log}$ Giardia and $2.0\text{-log}$ Virus inactivation must be achieved through chemical disinfection $CT$.

Inactivation Ratio (IR)=CTcalculatedCTrequired (from EPA Tables)1.00\text{Inactivation Ratio (IR)} = \frac{CT_{\text{calculated}}}{CT_{\text{required (from EPA Tables)}}} \ge 1.00

Environmental Sensitivity: Required $CT$ values from EPA lookup tables increase dramatically when water temperature drops (cold water slows disinfection kinetics) and when pH rises (shifting $HOCl$ to $OCl^-$).


Disinfection Byproducts (DBPs) & Stage 2 D/DBP Compliance

Disinfection Byproducts (DBPs) form when chemical disinfectants (especially free chlorine) react with Natural Organic Matter (NOM precursors: humic and fulvic acids) and bromide ($Br^-$).

   [Natural Organic Matter (TOC)] + [Free Chlorine (HOCl)] ===> [TTHM (80 ug/L)] + [HAA5 (60 ug/L)]

Primary Regulated DBP Classes & Maximum Contaminant Levels (MCLs)

  1. Total Trihalomethanes (TTHM): $\text{MCL} = \mathbf{0.080\text{ mg/L}} \text{ (}80,\mu\text{g/L)}$
    • Sum of: Chloroform ($CHCl_3$), Bromoform ($CHBr_3$), Bromodichloromethane ($CHBrCl_2$), Dibromochloromethane ($CHBr_2Cl$).
  2. Five Haloacetic Acids (HAA5): $\text{MCL} = \mathbf{0.060\text{ mg/L}} \text{ (}60,\mu\text{g/L)}$
    • Sum of: Monochloroacetic, Dichloroacetic, Trichloroacetic, Monobromoacetic, Dibromoacetic acids.
  3. Bromate ($BrO_3^-$): $\text{MCL} = \mathbf{0.010\text{ mg/L}} \text{ (}10,\mu\text{g/L)}$ (Formed when ozone reacts with raw water bromide $Br^-$).
  4. Chlorite ($ClO_2^-$): $\text{MCL} = \mathbf{1.0\text{ mg/L}}$ (Byproduct of chlorine dioxide).
  5. Maximum Residual Disinfectant Levels (MRDL): Free Chlorine = $4.0\text{ mg/L}$; Chloramines = $4.0\text{ mg/L}$; Chlorine Dioxide = $0.8\text{ mg/L}$.

Stage 1 vs. Stage 2 D/DBP Rule Compliance

  • Stage 1 D/DBP Rule: Evaluated compliance based on a system-wide Running Annual Average (RAA) across all sampling points combined, which masked localized distribution hotspots.
  • Stage 2 D/DBP Rule: Mandates compliance based on a Locational Running Annual Average (LRAA) calculated quarterly at each individual monitoring site. Every single sampling site must independently maintain an $\text{LRAA} \le \text{MCL}$.
  • Operational Evaluation Level (OEL): An early warning metric calculated quarterly to identify impending exceedances before a violation occurs:

OEL=Quarter 1+Quarter 2+2×(Current Quarter 3)4>MCL\text{OEL} = \frac{\text{Quarter } 1 + \text{Quarter } 2 + 2 \times (\text{Current Quarter } 3)}{4} > \text{MCL}

If the calculated $\text{OEL} > \text{MCL}$, the utility must submit an Operational Evaluation Report to VDH within 90 days identifying root causes (water age, storage tank turnover, precursor removal efficiency).

EPA Enhanced Coagulation Precursor Removal Matrix

Utilities with surface water sources must practice Enhanced Coagulation to achieve mandatory Step 1 Total Organic Carbon (TOC) removal percentages before chlorination:

Raw Water TOC (mg/L)Raw Water Alkalinity: $0-60\text{ mg/L}$Raw Water Alkalinity: $60-120\text{ mg/L}$Raw Water Alkalinity: $> 120\text{ mg/L}$
$2.0 - 4.0$$35.0%$ TOC Removal$25.0%$ TOC Removal$15.0%$ TOC Removal
$> 4.0 - 8.0$$45.0%$ TOC Removal$35.0%$ TOC Removal$25.0%$ TOC Removal
$> 8.0$$50.0%$ TOC Removal$40.0%$ TOC Removal$30.0%$ TOC Removal
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Breakpoint Chlorination Curve & Chemical Zones
Test Your Knowledge

At a treated finished water pH of 8.2, which chemical species of free available chlorine predominates in solution, and how does its germicidal potency compare to hypochlorous acid (HOCl)?

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Test Your Knowledge

A clearwell contact basin has a total volume of 600,000 gallons. During peak hourly operating conditions, the waterworks treats a flow rate of 3,000 gpm. The clearwell is designed with serpentine baffles providing an EPA Baffling Factor of 0.70. What is the effective T10 contact time for CT compliance calculations?

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Test Your Knowledge

Under the Stage 2 Disinfectants and Disinfection Byproducts (D/DBP) Rule, what are the Maximum Contaminant Levels (MCLs) for TTHM and HAA5, and on what mathematical basis is compliance determined?

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Test Your Knowledge

What chemical phenomenon occurs in Zone 3 of the breakpoint chlorination curve?

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D