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Chloramine Residual Collapse on a Dead-End Street

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Chloramine Residual Collapse on a Dead-End Street

Your distribution system is fully chloraminated, with 0.9 mg/L total chlorine leaving the plant at a Cl2 to NH3-N weight ratio of 4 to 1. In the Elm Street area, 3,800 ft of 4-inch cast iron dead-ends with very low flows and an estimated water age of six days, total chlorine has fallen to 0.15 mg/L. Free ammonia has risen from 0.05 to 0.55 mg/L, nitrite is 0.35 mg/L, and pH has slipped from 8.1 to 7.6. Two of five routine samples last month contained 3 total coliforms per 100 mL, confirmed non-fecal. The state requires a detectable residual throughout the system and no coliform positives. A resident complains of a swampy taste. There is no booster station in the area and the nearest 12-inch transmission main is 1,200 ft away.

1. Is this a plant dosing problem or a distribution problem? Build the case from the analytical results.

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It is nitrification in the distribution system, not an ammonia feed error at the plant.

The signature is the combination, not any single number:

  • Total chlorine falls while free ammonia rises. If the plant were underfeeding chlorine, ammonia would stay bound; instead the ammonia is being released as the chloramine is destroyed biologically.
  • Nitrite at 0.35 mg/L is direct evidence of ammonia-oxidizing bacteria at work; nitrite is an intermediate that only appears where nitrification is happening in the pipe.
  • pH and alkalinity decline (8.1 to 7.6) because nitrification consumes alkalinity and produces acid.
  • Six-day water age in a 4-inch dead-end is exactly the habitat nitrifiers need: warm, stagnant, chloramine residual decayed, oxygen present.

The coliform hits and the swampy taste are consistent with biofilm growth in the same zone. Responding by feeding more ammonia would make it worse.

2. What immediate operational actions would you take, in what order, and what would you avoid?

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Sequence matters because coliform positives are already on the record.

  1. Unidirectional flushing from the transmission main toward the dead-end, at a velocity high enough to scour (target 2.5 ft/s or better in the 4-inch), starting immediately and continuing until total chlorine is restored and turbidity clears. Document volumes and residuals.
  2. Temporarily boost chlorine in that zone toward free-chlorine conditions, either by raising the Cl2 to NH3-N ratio or by a short free-chlorine burn in the isolated area, until free ammonia drops below ~0.1 mg/L and nitrite is non-detect.
  3. Increase coliform monitoring in the affected area and coordinate with the primacy agency on the positive results; do not reduce sampling to make the numbers look better.
  4. Avoid adding ammonia or lowering the chlorine feed at the plant. Avoid large single-direction flush slugs that stir sediment into the rest of the grid without an outlet.

Re-check total chlorine, free ammonia, and nitrite daily until the zone holds a stable residual.

3. What long-term fixes would keep this from recurring, and how would you justify the cost against continued flushing?

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Flushing is a recurring labor and water-loss cost that never solves the underlying hydraulics; capital work does. The justification is water age.

  • Eliminate the dead-end: loop the 4-inch to the 12-inch main or install a blow-off with an automatic flusher. Even a modest continuous bleed drops the six-day age to something the chloramine residual can survive.
  • If looping is not feasible this year, add a small booster chloramination or chlorine injection point, or an automatic flusher on a timer, sized to turn the zone over every 48 to 72 hours.
  • Optimize the plant side for the season: hold Cl2 to NH3-N near 4.5 to 5 to 1 and pH near 8.0 to 8.3 during warm months, when nitrifiers grow fastest, and plan a system-wide free-chlorine burn each spring and fall.
  • Track it with water age modeling, plus monthly free ammonia in the ten highest-age nodes, so you can show the state a trend instead of reacting to coliform hits.