WASH R&D Centre · Study series

A wastewater treatment works, unit by unit

An illustrated atlas of the municipal treatment works: the liquid train from screens to reuse, the internal recycles that make biological nutrient removal work, and the sludge line where half the real operating effort lives. Each unit is drawn as an exploded or x-ray view with its component schedule — the hardware a plant walk actually inspects. A companion to the WESS study guide, at the scale a municipality runs.

1

The waste in the water

Domestic wastewater is about 99.9% water. The works exists for the last gram per litre, and that gram is not one substance but half a dozen groups, each harmful in its own way and each removed by a different part of the plant. Knowing the groups is knowing why the works has the shape it has.

The gram in the litre, made visible
The gram in the litre, made visible. Raw sewage magnified: rag and grit sinking, a fat globule floating, dissolved organics, ammonium and phosphate ions, a bacterium, a virus, a helminth egg, suspended particles and salt ions — each labelled with its typical raw strength. Everything the works exists to separate from the 99.9%.
GroupTypical compoundsThe harmRemoved by
Gross solids, rags, grit (highly variable)Cellulose (paper, rags), plastics (PET, polypropylene), silica sand SiO₂Mechanical: wrapped pump shafts, blocked pipes, abraded impellers, digesters filling with sandScreens, grit chamber (§4)
Fats, oils, grease (50–100 mg/L)Triglycerides, free fatty acids (oleic, stearic), calcium soapsCoats diffusers and weirs, congeals in sewers, feeds stable scums and filamentous foamOil & grease separator (§4)
Organic matter (BOD ≈ 250–400, COD ≈ 500–800 mg/L)Carbohydrates (starch, sugars — glucose C₆H₁₂O₆), proteins and their amino acids, fats, urea; the texts’ CH₂O is shorthand for the mixtureOxygen theft: bacteria burning it in the river strip the dissolved oxygen fish and invertebrates live onPrimary settling + the biological reactors (§5–6)
Nitrogen (TKN ≈ 40–80 mg/L)Urea CO(NH₂)₂ (most of it), ammonium NH₄⁺ / free ammonia NH₃, protein-bound organic N; nitrite and nitrate only in traces on arrivalThree harms: un-ionised ammonia is directly toxic to fish; nitrifying it in the river costs 4.6 g O₂ per g N (more oxygen theft); and as nitrate it fertilises algae and renders water unfit for infantsNitrification then denitrification (§6)
Phosphorus (TP ≈ 6–12 mg/L)Orthophosphate PO₄³⁻ / HPO₄²⁻, detergent polyphosphates, organically bound PThe scarcest algal nutrient, so the one that controls blooms: a single gram grows roughly a hundred grams of algae — eutrophication runs on PChemical precipitation at settling; some biological uptake
Sulfur (SO₄²⁻ ≈ 30–100 mg/L + protein S)Sulphate SO₄²⁻ from supply water and detergents; sulfur-bearing amino acids (cysteine, methionine); sulphide HS⁻/H₂S wherever the flow goes septicHarmless as sulphate — lethal as sulphide: H₂S gas kills sewer workers, its re-oxidation on pipe crowns makes sulphuric acid that eats concrete, and the odour is the works’ public faceKept oxidised by aeration; managed, not removed (see the sulfur loop below)
Pathogens (E. coli 10⁶–10⁸ CFU/100 mL as indicator)Organisms, not compounds: bacteria (E. coli, Vibrio, Salmonella), enteric viruses (rota-, noro-), protozoan cysts (Giardia, Cryptosporidium), helminth eggs (Ascaris)Disease: the reason wastewater treatment exists at allSettling and membranes remove; disinfection kills (§8)
Suspended solids (TSS ≈ 200–400 mg/L)Organic detritus and cellulose fibres, clay and silt (aluminosilicates), the particulate share of everything aboveSmothers river beds, carries adsorbed organics and metals, and shields embedded pathogens from disinfectantSettling at both ends of the train, membranes (§5, 7)
Dissolved salts (TDS 500–1 200 mg/L)Na⁺, Cl⁻, SO₄²⁻, HCO₃⁻, Ca²⁺, Mg²⁺, K⁺Conservative: nothing in a conventional works touches them — the one group that passes through, and the reuse loop’s eventual limitNot removed (dilution, or membranes beyond UF)

The chemistry we are buying

Strip the plant to its purpose and it is a small set of reactions, chosen because each one converts a harmful species into a harmless one. The works is a place where those reactions are made to happen fast, in tanks, instead of slowly, in the river.

The harm the works pre-empts
The harm the works pre-empts. Downstream of an untreated outfall the river runs the same oxidation the aerobic reactor runs on purpose — on its own dissolved oxygen. The sag curve: clean water, degradation, the damage zone where only air-gulpers survive, and the slow recovery kilometres later.
The reaction we are pre-empting — oxygen theft in the river CHX2O+OX2→river bacteriaCOX2+HX2O\ce{CH2O + O2 ->[\text{river bacteria}] CO2 + H2O} The same oxidation the aerobic reactor runs deliberately (§6) happens for free in any river that receives raw sewage — and the oxygen it consumes is the river’s. A strong discharge drives dissolved oxygen through the sag that kills everything downstream of the outfall. The entire carbonaceous side of the works exists to run this reaction in a tank, on blown air, instead.
Nitrogen: from toxic to inert NHX3⇌NHX4X+\ce{NH3 <=> NH4+} NHX4X+→nitrifyNOX3X−→denitrifyNX2↑\ce{NH4+ ->[\text{nitrify}] NO3- ->[\text{denitrify}] N2 ^} Un-ionised ammonia (the NH₃ side of the equilibrium, favoured at high pH) is acutely toxic to fish at fractions of a mg/L. The works walks nitrogen down the whole chain: ammonium to nitrate (removing both toxicity and the 4.6 g/g oxygen debt), then nitrate to nitrogen gas — the same inert N₂ that is four-fifths of air. Section 6 gives both reactions in full.
The sulfur loop — septicity, odour and the acid that eats sewers SOX4X2−+2 CHX2O→no oxygen, no nitrateHSX−+2 COX2+HX2O+OHX−\ce{SO4^2- + 2CH2O ->[\text{no oxygen, no nitrate}] HS- + 2CO2 + H2O + OH-} HSX−+HX+⇌HX2S↑\ce{HS- + H+ <=> H2S ^} HX2S+2 OX2→ThiobacillusHX2SOX4\ce{H2S + 2O2 ->[\textit{Thiobacillus}] H2SO4} HSX−+2 OX2→SOX4X2−+HX+\ce{HS- + 2O2 -> SO4^2- + H+} Sulfur cycles rather than leaves. When sewage goes septic — long rising mains, deep septic tanks, any corner the redox tower’s bottom reaches — sulphate-reducing bacteria respire SO₄²⁻ and make sulphide. The equilibrium releases H₂S gas on the acid side of neutral: the rotten-egg odour, and at sewer-atmosphere concentrations a worker-killing toxin. On the damp crown of the pipe, Thiobacillus oxidises that gas to sulphuric acid, which dissolves the concrete — crown corrosion is how sewers are eaten from the inside. The works’ defence is the last reaction: keep the flow aerated and sulphide is oxidised harmlessly back to sulphate, which is why septicity control starts at the headworks, not at the complaint line.
Phosphorus: the reaction biology cannot do AlX3++POX4X3−→AlPOX4↓\ce{Al^3+ + PO4^3- -> AlPO4 v} FeX3++POX4X3−→FePOX4↓\ce{Fe^3+ + PO4^3- -> FePO4 v} Ordinary biomass is only ~1–2% phosphorus, so a biological train barely touches TP. Removal is bought chemically: alum or ferric dosed at settling precipitates phosphate as an insoluble salt into the sludge. Jar-test first — real sewage consumes coagulant on side reactions before this one.
Pathogens: oxidative kill HOCl+cell→inactivated\ce{HOCl + $\text{cell}$ -> $\text{inactivated}$} Hypochlorous acid oxidises through cell walls and proteins; UV instead wrecks DNA directly. Either way the barrier is §8 — and it only works on organisms the solids removal has left exposed.
Eutrophication in four panels
Eutrophication in four panels. Nutrients arrive, algae bloom and block the light, the bloom dies and its digestion strips the oxygen, and the pond ends green, anoxic and dead — with the multiplier that makes phosphorus the control knob: one gram grows about a hundred grams of algae.
The four pathogen classes to scale — virus, bacterium, protozoan cyst, helminth egg across three orders of magnitude — and the barrier that catches each: settling takes the heavy egg, the 0
The four pathogen classes to scale — virus, bacterium, protozoan cyst, helminth egg across three orders of magnitude — and the barrier that catches each: settling takes the heavy egg, the 0.05 µm membrane wall stops bacteria and cysts and most viruses, chlorine and UV finish what passes.
What "removed" means Almost nothing is destroyed. The screens fill skips; the settlers and the biology convert dissolved pollution into sludge; the precipitated phosphorus leaves in the same sludge; only nitrogen (as N₂) and carbon (as CO₂ and CH₄) actually leave as gas. Everything else is concentrated and carted away — which is why the sludge line of §9 is half the works, and why "treatment" is mostly the art of moving pollution from a large volume of water into a small volume of solids.
Who removes what
Who removes what. The section’s table drawn as a matrix: each contaminant group against the unit that captures or destroys it — and the dissolved-salts row empty end to end, because nothing in a conventional works touches them.
2

The works at a glance

A treatment works is two trains sharing one site. The liquid train runs left to right: physical protection (screens, grit, fats), balancing, primary settling, the biological reactors, final clarification, disinfection, and discharge or reuse. The sludge line runs underneath it: everything the liquid train removes — primary sludge and wasted biomass — is thickened, stabilised, dewatered and carted away. Two internal recycles stitch the trains together: the nitrified-liquor recycle (MLR) and return activated sludge (RAS) keep the biology supplied, while filtrate from dewatering returns its load to the head of works.

ScreenGritOil& greaseEQ tankPrimaryAnoxicAerobicSecondaryDisinfectReuse/ dischargeraw sewage by sewer — and septage by tanker from conservancy tanksMLR — nitrified liquor recycleRAS — return activated sludge (via RAS/WAS station)ThickenerDigesterDewateringCake off-siteprimary sludgeWASbiogasfiltrate and drying-bed drainage return to the head of works
The whole works in one line. Liquid train left to right with its two return streams — the MLR feeding nitrate back to the anoxic zone and the dashed RAS returning biomass — and the sludge line beneath: primary sludge and WAS to thickener, digester (yielding biogas), dewatering and cake off-site, with filtrate returning to the head of works. Every box below is drawn in full in the sections that follow.
3

Arrivals — by sewer and by tanker

Most of the load arrives by gravity sewer, but a works also serves everything the sewer network does not reach: conservancy tanks and septic systems whose contents arrive by vacuum tanker and are discharged at the headworks. The conservancy tank is the works’ off-site outpost — a sealed holding tank whose only treatment is quiet settling between collections. Its condition (and its emptying cadence) decides how septic, how strong, and how gritty the tankered load is when it hits the screens.

Conservancy tank, x-ray view
Conservancy tank, x-ray view. A sealed RCC holding tank in service: inlet, overflow and valved outlet, waterproofing strip between tank and base. What settles here between tanker visits arrives at the works as concentrated septage — the strongest, most variable feed the headworks sees.

How a septic tank actually works

The septic tank is the conservancy's discharging cousin, and it is a working treatment unit rather than a store. It is a flow-through vessel: every flush that enters pushes an equal volume out the far end, so the tank holds each day's flow for one to three days and no longer. What it does with those days is physics first, biology second.

The physics is self-organisation into three layers. Fats and greases float to a scum crust; settleable solids fall to a sludge blanket; between them sits a comparatively clear liquor zone. The inlet tee kills the incoming jet and delivers flow below the scum so nothing short-circuits across the surface; the outlet tee draws only from the clear middle, leaving both blankets behind. On that geometry alone the tank removes half to two-thirds of the suspended solids and a third of the BOD.

The biology happens in the blanket the physics builds. The settled sludge digests itself anaerobically — the same hydrolysis, fermentation and methanogenesis chain as the digester of §9, run cold and slow — destroying perhaps half of its own volume as gas. The bubbling lifts flecks of sludge that resettle, the urea arriving with the flow hydrolyses to ammonium, and sulphate reduction supplies the signature odour:

The septic chain — cold, slow, unmanaged digestion CO(NHX2)X2+3 HX2O→2 NHX4X++HCOX3X−+OHX−\ce{CO(NH2)2 + 3H2O -> 2NH4+ + HCO3- + OH-} settled organics→VFAs→CHX4+COX2\ce{$\text{settled organics}$ -> $\text{VFAs}$ -> CH4 + CO2} SOX4X2−+organics→HSX−+HX2S↑\ce{SO4^2- + $\text{organics}$ -> HS- + H2S ^} Urea to ammonium (why septic effluent is ammonium-rich), the digestion chain shrinking the blanket, and the sulphide that announces the process. Nothing here is aerobic: the tank ships its effluent OUT still anaerobic, still strong, still pathogen-laden.
The septic tank, working and failing
The septic tank, working and failing. Inlet tee below the scum, three self-organised layers, outlet tee drawing from the clear middle, effluent to the soakaway where soil biofilm runs the aerobic half — and the failure inset: blanket too high, solids over the outlet, soakaway blinded. The depth gauge at 30–40% is the desludge trigger.

That last point is the part most owners never hear: a septic tank does not make clean water. Its effluent is anaerobic, ammonium-rich and carries roughly half the original load; the actual treatment is the soakaway or drain field downstream, where the soil percolation bed runs the aerobic half of the job — an unpowered trickling filter of soil biofilm that oxidises the organics and ammonia and adsorbs what it cannot burn. The tank's real product is effluent clear enough not to clog that soil.

Which is also its fatal failure mode. The blanket and crust grow until they crowd the clear zone; solids then carry over the outlet and blind the soakaway, and a blinded soakaway is a rebuilt soakaway — the one component that does not recover with a pump-out. Hence the sludge-judge cadence: desludge at 30–40% blanket depth, before the geometry fails, not after the garden smells. Where there is no soakaway at all, the same vessel built sealed is the conservancy tank above, and the tanker to this works replaces the drain field.

4

Preliminary treatment — protecting everything downstream

Nothing biological happens here; preliminary treatment exists so that everything downstream can. Screens take the rags and plastics that would wrap a pump shaft; the grit chamber slows the flow until sand drops out before it can scour impellers and fill digesters; the oil-and-grease separator floats off what would otherwise coat diffusers and feed filamentous foam; and the equalisation tank flattens the morning peak into a feed the biology can ride. Each unit is cheap insurance against a specific, expensive downstream failure.

Screening / headworks
Screening / headworks. Coarse (20–50 mm) then fine (6–10 mm) bar screens with a raked monorail; screenings are washed, compacted and skipped. Everything the screens miss becomes somebody else’s blockage downstream.
Grit chamber
Grit chamber. Velocity drops to 0.2–0.3 m/s so sand and grit settle into the hopper while organics stay in suspension — protecting pumps and reactors from abrasion and keeping inert solids out of the digesters.
Oil / grease / scum separator
Oil / grease / scum separator. Three zones — gravity separation, coalescing media, clarified water — with skimmer arms taking the float and a sump taking the sinkers. Kitchen and industrial fat loads that defeat it reappear later as aeration-basin foam and settling trouble.
Equalisation tank
Equalisation tank. A mixed buffer (typically 2–8 h) that flattens hydraulic and organic shocks into a steady feed — the difference between a plant sized for the average day and one sized for its worst hour.
5

Primary settling — the cheapest treatment on site

An hour or two of quiet buys the removal of roughly half the suspended solids and a third of the BOD, at almost no operating cost: gravity does the work, a slow scraper collects the result. Primary sludge is the energy-rich half of the digester’s diet, so this tank is where the sludge line truly begins.

Primary settling tank
Primary settling tank. Feed well, scum baffle, rotating scraper into the conical hopper, outlet weir: the physical removal that halves the load the biology must carry, and the source of primary sludge for digestion.
6

The biological heart — anoxic, aerobic, and the anaerobic alternative

In a nutrient-removal works the anoxic and aerobic zones work as a pair. The aerobic basin does the heavy lifting — BOD oxidation and nitrification through a fine-bubble diffuser grid — and the anoxic zone upstream denitrifies, provided the MLR pipe keeps bringing it nitrate and the incoming sewage keeps bringing it carbon. The pairing is thermodynamic choreography: each zone holds its own redox regime, and the plumbing between them is as load-bearing as the biology. For strong wastes, an anaerobic reactor offers a different bargain — treatment that yields energy (biogas) instead of consuming it (aeration), at the price of slower, touchier biology.

Carbonaceous oxidation (aerobic) CHX2O+OX2→COX2+HX2O\ce{CH2O + O2 -> CO2 + H2O} The heterotrophs burning the organic load. CH₂O stands for generic organic matter; this reaction takes the first claim on whatever oxygen the diffusers supply.
Nitrification (aerobic) — two organisms in relay 2 NHX4X++3 OX2→2 NOX2X−+4 HX++2 HX2O\ce{2NH4+ + 3O2 -> 2NO2- + 4H+ + 2H2O} 2 NOX2X−+OX2→2 NOX3X−\ce{2NO2- + O2 -> 2NO3-} Ammonia oxidisers make nitrite and acid; nitrite oxidisers finish to nitrate. Together ≈ 4.6 mg O₂ per mg N, destroying ≈ 7.1 mg of alkalinity (as CaCO₃) per mg N.
Denitrification (anoxic) 5 CHX2O+4 NOX3X−+4 HX+→2 NX2+5 COX2+7 HX2O\ce{5CH2O + 4NO3- + 4H+ -> 2N2 + 5CO2 + 7H2O} Facultative heterotrophs respiring NITRATE in place of oxygen: the nitrate the aerobic zone made, plus the soluble carbon the raw influent brings, leave together as nitrogen gas. Needs roughly 4–5 g of soluble COD per g of NO₃-N, and returns about half of nitrification’s alkalinity.
Why oxygen in the anoxic zone is a fault Oxygen does not create nitrate — it stops nitrate being destroyed. The denitrifiers are facultative: offered both acceptors, they respire oxygen, because it yields more energy per electron than nitrate does. So dissolved oxygen above roughly 0.5 mg/L switches the whole population back to ordinary aerobic respiration, the carbon that should have reduced nitrate is burned with O₂ instead, and the nitrate rides through the zone untouched to the effluent. That is why the anoxic tank is stirred by a mixer rather than aerated, why the MLR diffuser distributes liquid and never air, and why an over-aerated aerobic zone poisons denitrification downstream through the oxygen dissolved in the recycle itself.
Anoxic reactor
Anoxic reactor. Mixed but never aerated: the mixer keeps biomass in suspension while the internal mixed-liquor recycle (MLR) pipe returns nitrified liquor from the aerobic zone. The MLR diffuser in the drawing is a liquid-distribution manifold on the tank floor — it spreads the returning liquor evenly so its nitrate meets the influent carbon across the whole zone rather than jetting a channel to the outlet. Despite sharing a name with the aerobic tank’s fine-bubble unit, it diffuses liquid, never air: the zone denitrifies only below about 0.5 mg/L dissolved oxygen, so entrained bubbles — or oxygen riding the recycle — switch the biology back to oxygen respiration and nitrate passes straight to the river.
Aerobic reactor
Aerobic reactor. A fine-bubble diffuser grid fed by the air-supply header, baffled against short-circuiting, with an effluent weir and a waste-sludge pipe. Aeration is usually the works’ single largest power draw — which is why its control earns so much attention.
Anaerobic reactor (UASB form)
Anaerobic reactor (UASB form). Influent rises through a granular sludge bed; biogas collects under the dome while the three-phase separator returns solids and passes clarified water on. The high-strength alternative: it makes energy rather than spending it, and hands a lighter load to the aerobic stage.
7

Separation and the return loop

Activated sludge only works because the biomass is caught and sent round again. The secondary settling tank separates the mixed liquor; the RAS/WAS pumping station returns most of it to the biology (RAS) and wastes the growth surplus (WAS) to the sludge line — the daily decision that sets sludge age, and with it nearly everything about how the plant behaves. A polishing clarifier gives the effluent a second, gentler settle where standards demand it.

Secondary settling tank
Secondary settling tank. Central drive, scraper arms, scum baffle, conical hopper: where the biology is separated from the water it treated. Sludge that will not settle here — bulking, rising, pin-floc — defeats the whole activated-sludge idea geometrically.
Clarifier
Clarifier. The polishing variant: perimeter weir, centre well, sloped floor to a sludge drawdown. Same physics as the secondary settler, applied once more to an already-clean stream.
RAS / WAS pumping station
RAS / WAS pumping station. Submersible pumps in a wet well, level transmitters, duty and standby: RAS returns continuously to the biology, WAS is wasted intermittently to thickening. The unglamorous machine most “biology” failures trace back to.
8

Disinfection and reuse

The last barrier is deliberately boring: a serpentine tank that buys twenty to sixty minutes of contact between effluent and disinfectant — chlorine dosed to hold a free residual, or a UV bank where by-products or dechlorination argue against chemicals. Beyond it, storage and pumping turn treated effluent from a discharge into a product: irrigation, process water, toilet flushing.

Chlorine speciation and demand ClX2+HX2O→HOCl+HX++ClX−\ce{Cl2 + H2O -> HOCl + H+ + Cl-} HOCl⇌HX++OClX−\ce{HOCl <=> H+ + OCl-} NHX4X++HOCl→NHX2Cl+HX2O+HX+\ce{NH4+ + HOCl -> NH2Cl + H2O + H+} Hypochlorous acid is the working biocide (pKa ≈ 7.5 — faster on the acid side of neutral). Ammonia and residual organics consume chlorine as chloramines BEFORE any free residual forms, which is why an upstream nitrification failure silently eats the disinfectant dose.
Disinfection / contact tank
Disinfection / contact tank. Baffle walls create plug flow and guarantee contact time; chemical dosing (or the UV alternative alongside) provides the kill; the outlet weir holds the level. The free residual measured here is the last number between the works and its receiving water.
Treated effluent storage / reuse tank
Treated effluent storage / reuse tank. Level-controlled storage with duty/standby pumps, flow metering and sampling — the unit that turns an outfall into a supply. Reuse applications range from irrigation and industrial process water to toilet flushing.
9

The sludge line — where half the operating effort lives

Everything the liquid train removes has to go somewhere, and moving watery sludge is mostly moving water. The line is a progression of concentration steps: the thickener roughly halves the volume by gravity; the digester stabilises the solids over weeks — destroying volatile matter, killing pathogens, and yielding biogas worth burning; dewatering presses the digested sludge to a spadeable cake; and drying beds do the same job with sun and sand where land is cheaper than machinery. Filtrate and drainage from every step return their load to the head of works — the works treats its own wastewater too.

Anaerobic digestion (sludge line, net) CHX3COOH→CHX4+COX2\ce{CH3COOH -> CH4 + CO2} 4 HX2+COX2→CHX4+2 HX2O\ce{4H2 + CO2 -> CH4 + 2H2O} Hydrolysis and fermentation break the sludge to volatile fatty acids and hydrogen; methanogens finish both routes to biogas — typically 60–70% CH₄. The digester runs the same chain as the anaerobic reactor, on the plant’s own residuals.
Sludge thickener
Sludge thickener. Gravity concentration (12–24 h) with slow rakes over a steep 60–70° cone: halves the volume the digester and dewatering must handle, at the cost of one more tank to keep un-septic.
Anaerobic sludge digester
Anaerobic sludge digester. Heated, mixed and insulated under a floating gas holder: 15–30 days that stabilise the sludge and yield biogas — the methanogenesis of the anaerobic reactor run as a process in its own right, on the plant’s own residuals.
Sludge dewatering — screw press
Sludge dewatering — screw press. Polymer-conditioned sludge squeezed along a screened screw against a back-pressure plate; cake to skip, transport or beds, filtrate back to the works. Cake dryness is set here, and trucking costs follow it.
Sludge drying beds
Sludge drying beds. Roofed cells over sand and gravel filters: drainage returns to the head of works while sun and airflow take the moisture. Layer thickness and scraping cadence are the entire operating manual.
10

Test yourself

  1. Grit chambers slow the flow to 0.2–0.3 m/s. Why that band — why not slower?
    Answer

    Slow enough for sand and dense inorganics to settle, fast enough that light organic solids stay in suspension and carry on to treatment. Slower, and the chamber starts doing the primary settler’s job — collecting putrescible sludge it was never designed to store.

  2. Which two streams meet in the anoxic zone, and what does each bring?
    Answer

    Incoming settled sewage brings soluble carbon (the electron donor); the MLR brings nitrate from the aerobic zone (the electron acceptor). Denitrification needs both in the same tank at the same time — which is why the recycle pipe is as important as the biology.

  3. WAS is a few percent of the RAS flow, yet it is called the most important control on the plant. Why?
    Answer

    Wasting sets sludge age — how long the average organism stays in the system. Sludge age determines whether slow-growing nitrifiers persist, how much oxygen the plant demands, and how the sludge settles. RAS keeps the biology in the tanks; WAS decides what that biology becomes.

  4. Why does the digester get primary sludge AND waste activated sludge, and which digests better?
    Answer

    Both need stabilising before disposal. Primary sludge digests better — it is raw, energy-rich organic matter. WAS is already biomass; its energy has largely been spent growing it, and its cell walls resist breakdown, so it yields less gas per tonne.

  5. Filtrate from dewatering returns to the head of works. What load does it carry, and when does that loop become a problem?
    Answer

    Digester filtrate is small in volume but rich in ammonia and phosphorus released during digestion. On a large works the return can add a fifth or more of the nitrogen load — arriving in slugs when dewatering runs — and an undersized biology feels it as unexplained effluent ammonia.