Free Wastewater Operator Exam Flashcards

A conventional plant often moves from preliminary treatment to primary clarification, secondary biological treatment, final clarification, disinfection, and solids handling. Each stage removes a different problem: debris, settleable solids, dissolved organics, biomass, pathogens, or sludge.

Preliminary treatment protects downstream equipment by removing large debris, rags, plastics, and grit. It is mainly equipment protection, not the main step for removing dissolved BOD.

A bar screen removes debris from the flow for disposal. A comminutor shreds solids and leaves the pieces in the wastewater, so it does not reduce solids loading the way screening does.

Grit removal lets heavy inorganic particles settle while keeping lighter organic solids in suspension. Poor grit control wears pumps, fills tanks, and can create odorous, organic-rich grit waste.

A primary clarifier removes settleable solids and floatable scum by gravity settling and skimming. Removing that load before aeration reduces downstream oxygen demand and sludge production.

A scum baffle keeps grease and floating material from escaping with clarifier effluent. Without it, floatables can foul downstream processes and raise effluent solids or BOD.

Flow equalization dampens peaks in flow or strength before downstream treatment. It helps biological and clarification processes see steadier loading instead of sudden shocks.

Activated sludge is an aerobic biological process where microorganisms in mixed liquor consume soluble and fine organic matter. Operators control the process by managing air, mixing, solids inventory, return sludge, and wasting.

MLSS is mixed liquor suspended solids: the suspended solids concentration in the aeration basin. It is a basic measure of biomass inventory, but it includes both active and inert material.

MLVSS estimates the volatile, more biologically active portion of mixed liquor solids. Operators often use MLVSS in F/M calculations because it better represents microorganisms than total MLSS alone.

High food-to-microorganism ratio means a relatively heavy food load for the available biomass. It often points to younger sludge, rapid growth, unstable settling, or white biological foam.

Low dissolved oxygen stresses aerobic biology and can reduce BOD removal, weaken floc, create odors, support filament problems, and cause ammonia breakthrough when nitrifiers are affected.

Mean cell residence time estimates how long solids stay in the activated sludge system. Longer sludge age favors slow-growing nitrifiers; excessive sludge age can create older-sludge symptoms and higher oxygen demand.

Increasing waste activated sludge removes biomass faster and lowers sludge age over time. WAS is the main long-term control for solids inventory and MCRT.

Return activated sludge moves settled biomass from the secondary clarifier back to aeration. Waste activated sludge removes biomass from the process. RAS shifts solids location quickly; WAS changes inventory and sludge age.

Sludge volume index relates 30-minute settled sludge volume to MLSS concentration. It is a settleability indicator: high SVI generally means bulky, poorly compacting sludge.

Bulking is poor settling or compaction, often reflected by high SVI. Rising sludge is solids floating after gas formation, commonly tied to denitrification or septic conditions in a clarifier.

Nitrification converts ammonia to nitrate under aerobic conditions. It needs adequate DO, alkalinity, temperature, and sufficient sludge age because nitrifying bacteria grow slowly.

Denitrification converts nitrate to nitrogen gas under anoxic conditions with available carbon. It removes nitrogen, but unwanted denitrification in a clarifier can make sludge rise.

Anaerobic zones lack dissolved oxygen and nitrate, anoxic zones lack dissolved oxygen but have nitrate, and aerobic zones have dissolved oxygen. Biological nutrient removal depends on keeping those environments distinct.

A secondary clarifier separates biological floc from treated water after aeration. Clear effluent, controlled sludge blanket, and reliable RAS removal are all signs the biological process and clarifier are working together.

If settleability is acceptable but the blanket is high, look beyond bulking. Hydraulic loading, inadequate RAS capacity, collector problems, or excessive solids inventory may be pushing the blanket upward.

Stabilization reduces the volatile, odorous, putrescible character of sludge before disposal or beneficial use. Digestion, lime stabilization, and similar processes make solids safer and easier to manage.

Thickening increases solids concentration before digestion or storage by removing some water. Dewatering removes much more water to produce a cake for hauling or disposal.

Chlorine residual is the measurable chlorine remaining after demand is satisfied and contact has occurred. Too little residual can mean poor disinfection; too much residual can violate discharge limits or harm aquatic life.

Dechlorination removes or neutralizes chlorine residual before discharge when the permit requires it. It protects receiving waters but must be controlled so disinfection is not defeated too early.

UV inactivates microorganisms with light rather than a chemical residual. Performance depends on clean lamps, proper intensity, exposure time, and wastewater clarity or UV transmittance.

Biochemical oxygen demand measures the oxygen microorganisms use while degrading biodegradable organic matter. High BOD means more oxygen demand on the treatment process or receiving stream.

Total suspended solids measures the particles retained on a filter. TSS is tied to clarifier performance, effluent permit compliance, and solids loading calculations.

Nitrification consumes alkalinity and can depress pH if buffering is low. Falling pH can then inhibit nitrifiers, so ammonia problems may be linked to alkalinity as well as air or sludge age.

Dissolved oxygen can change quickly after collection, so it is usually measured immediately in the field or online. A delayed bottle reading may not represent the process condition.

A composite sample better represents average conditions over time, such as daily BOD loading. A grab sample represents one moment and is common for parameters that change quickly or have short holding requirements.

Cooling and proper preservation slow chemical or biological changes after collection. Do not rinse a pre-preserved sample bottle unless the lab directs it, because rinsing can remove the preservative.

Chain of custody documents who collected, handled, transferred, and received a compliance sample. It protects the credibility of the result by showing the sample was not mixed up or tampered with.

A field duplicate checks precision across sampling and analysis for the same location and time. It is not a substitute for a blank, calibration record, or chain-of-custody form.

lb/day = concentration in mg/L x flow in MGD x 8.34. The 8.34 factor converts million gallons of water at that concentration into pounds per day.

Percent removal = (influent - effluent) / influent x 100. Use the same units for both concentrations and remember that lower effluent concentration means higher removal.

Detention time = volume / flow, with units matched. For example, MG divided by MGD gives days, then multiply by 24 to convert days to hours.

Chemical lb/day uses the same loading pattern as pollutants: dose in mg/L x flow in MGD x 8.34. The result is dry chemical pounds per day before adjusting for solution strength.

MCRT is approximated as solids in the system divided by solids leaving per day. Include wasting and effluent solids losses when the problem provides them.

SVI = 30-minute settled sludge volume in mL/L divided by MLSS in g/L. Convert MLSS from mg/L to g/L before dividing.

Cavitation occurs when pressure near the impeller drops low enough for vapor bubbles to form and collapse. Warning signs include noise, vibration, reduced flow, and impeller damage risk.

Blowers supply air, and diffusers transfer oxygen into mixed liquor. Fouled diffusers, leaking air lines, or blower problems can lower DO even if the biological demand has not changed.

Preventive maintenance is scheduled work done before failure: lubrication, inspection, calibration, cleaning, and exercising backup equipment. It reduces emergency outages and supports permit compliance.

SCADA alarms alert operators to abnormal conditions but do not replace field verification, calibration, or operating judgment. Cybersecurity and access control matter because remote systems can affect real plant equipment.

Before entry, test oxygen first, then combustible gases, then toxic gases such as hydrogen sulfide. Low oxygen can affect other sensor readings and is itself a life-threatening hazard.

LOTO provides positive isolation from electrical, mechanical, hydraulic, pneumatic, chemical, and stored-energy hazards before maintenance. A verbal warning or stopped switch is not enough.

Never mix sodium hypochlorite with acid cleaners. The reaction can release chlorine gas rapidly, creating a severe inhalation hazard.

If chlorine gas is suspected, move upwind and uphill while activating emergency procedures. Chlorine is heavier than air and can collect in low areas.

Permit compliance depends on accurate sampling, monitoring, reporting, and recordkeeping. Bypasses, upsets, missed samples, and limit exceedances must be handled according to the permit and agency notification requirements, not hidden or corrected after the fact.