DC Water Operator study materials
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DC Water Operator flashcards

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32 cards. Read the term and the definition here. The deck at the top of this page is optional.

CT value
The product of disinfectant residual concentration in mg/L and contact time in minutes. Required CT varies with disinfectant, pH, temperature, and target organism.
Chlorine demand
The difference between the chlorine dose applied and the residual remaining after a specified contact time. It reflects consumption by organics, ammonia, and other reducing substances.
Jar test purpose
A bench-scale test that mixes raw water with varied coagulant doses and pH to identify the combination producing the lowest settled turbidity before full-scale adjustment.
Filter loading rate
Flow through a filter divided by its surface area, usually expressed in gpm/ft². It determines hydraulic stress on the media and affects particle penetration.
Backwash bed expansion
The percentage increase in filter media depth during backwash, typically 15 to 25 percent. It is controlled by backwash flow rate and varies with water temperature.
Turbidity units
Turbidity is measured in nephelometric turbidity units (NTU). Combined filter effluent is commonly limited to 0.3 NTU in 95 percent of monthly samples and never above 1 NTU.
Log removal
A logarithmic expression of pathogen reduction: 1-log is 90 percent, 2-log is 99 percent, 3-log is 99.9 percent, and 4-log is 99.99 percent removal or inactivation.
Coagulation versus flocculation
Coagulation neutralizes particle charges so they can stick together; flocculation is gentle mixing that builds those particles into larger, settleable flocs.
Pressure head conversion
One foot of water column equals 0.433 psi, and one psi equals 2.31 feet of head. These conversions are used constantly for pressure and elevation calculations.
Hazen-Williams equation
A head loss formula for full pipes: hf = 10.44 × L × Q^1.85 divided by (C^1.85 × d^4.87) in US customary units, where C is pipe roughness.
Minimum distribution pressure
Normal operating pressure in a distribution system is generally kept at or above 20 psi. Lower pressure raises contamination risk and triggers investigation and public notice.
Air gap backflow protection
A physical separation between a potable water outlet and the flood level of a receiving vessel. It provides the highest level of cross-connection protection.
Reduced-pressure-zone assembly
A testable backflow preventer with two check valves and a relief valve between them. It protects against both backpressure and backsiphonage in high-hazard connections.
Water age
The average time water spends in storage or piping. High water age depletes disinfectant residual and promotes disinfection byproduct formation and nitrification.
Main disinfection dose
New or repaired water mains are commonly disinfected with 25 to 50 mg/L free chlorine for 24 hours, followed by flushing and bacteriological sampling before service.
Minimum night flow
The lowest system flow, usually overnight. Elevated minimum night flow relative to normal use suggests leakage or unauthorized consumption in the distribution network.
Pipe flow equation
Flow equals area times velocity, Q = A × V. For a full circular pipe, area is 0.7854 times the diameter squared, using consistent units.
BOD5 definition
Biochemical oxygen demand measured over five days at 20 degrees Celsius. It estimates biodegradable organic matter consumed by microorganisms in a wastewater sample.
Solids retention time
Also called sludge age: the mass of solids in the aeration basin divided by the mass of solids leaving the system per day, expressed in days.
Food-to-microorganism ratio
Pounds of BOD applied per day divided by pounds of mixed liquor suspended solids under aeration. It indicates organic loading relative to the biomass available.
Sludge volume index
Settled sludge volume in mL/L after 30 minutes times 1,000, divided by MLSS in mg/L. Values near 80 to 150 indicate good settling.
Return activated sludge rate
The RAS flow needed to maintain basin MLSS, calculated as influent flow times MLSS divided by (RAS concentration minus MLSS), with consistent units.
Secondary clarifier loading
Solids loading rate equals (influent flow plus return flow) times MLSS, divided by clarifier surface area. Excess loading causes solids carryover in the effluent.
Nitrification oxygen demand
Oxidizing ammonia to nitrate consumes about 4.57 mg of oxygen per mg of nitrogen. This demand adds to aeration requirements beyond carbonaceous BOD.
Secondary treatment limits
Common regulatory limits are 30 mg/L BOD and 30 mg/L total suspended solids, with at least 85 percent removal of both, based on monthly averages.
Hydraulic detention time
Tank volume divided by flow rate, expressed in hours or days. It describes how long wastewater remains in a treatment unit at a given flow.
Manning's equation
Velocity equals (1.486/n) times hydraulic radius to the two-thirds power times slope to the one-half power in US customary units, where n is roughness.
Self-cleansing velocity
A minimum gravity sewer velocity of about 2 feet per second at design flow. Below it, grit and solids settle and can cause blockages.
Maximum sewer velocity
Gravity sewers are usually designed to keep velocity at or below about 10 feet per second to limit abrasion, scour, and release of hydrogen sulfide.
Infiltration versus inflow
Infiltration is groundwater entering through pipe defects and joints. Inflow is direct stormwater entry through connections such as roof drains, sumps, and manhole covers.
Surcharging
A condition where flow exceeds gravity pipe capacity, causing the hydraulic grade line to rise above the pipe crown and potentially back up into basements.
Confined space atmosphere
Entry requires testing for oxygen (19.5 to 23.5 percent), flammable gas, and hydrogen sulfide before entry and continuously during occupancy, with ventilation as needed.