7.3 Water Treatment Residuals: Sludge, Backwash Water and Membrane Concentrate
Key Takeaways
Residuals include coagulant sludge, spent filter backwash, membrane backwash and concentrate, lime softening sludge, ion-exchange brine, and spent activated carbon.
Alum sludge production can be estimated as 8.34 × flow (MGD) × (0.44 × alum dose + raw suspended solids + other additives) in lb/day of dry solids.
Recycled filter backwash must return through the plant's full treatment train, ahead of the primary coagulant, under the Filter Backwash Recycling Rule.
Spent backwash discharged to surface water needs DEQ coverage, such as the 200-J NPDES general permit for filter backwash.
Residuals sent to a landfill must pass the paint filter liquids test, and discharges to a sanitary sewer need the receiving utility's approval.
Types of Residuals
| Residual | Source | Typical character |
|---|---|---|
| Coagulant (alum or ferric) sludge | Sedimentation basins, DAF float | Gelatinous; about 0.5-2 percent solids before thickening; hard to dewater |
| Spent filter backwash water (SFBW) | Media filter backwash and filter-to-waste | Large volume, low solids; contains concentrated particles and pathogens |
| Membrane residuals | MF/UF backwash and CIP wastes; NF/RO concentrate | Concentrate carries dissolved salts at several times feed levels; CIP waste may be acidic or caustic |
| Lime softening sludge | Softening clarifiers | Dense calcium carbonate; dewaters well |
| Ion-exchange brine | Regeneration | High chloride and hardness; disposal is often the hardest part of IX |
| Spent PAC and GAC | Adsorption | PAC leaves with the sludge; GAC is regenerated or replaced |
OHA's Table 51 even awards classification points for residuals handling. Examples are 5 points each for discharge to lagoons, land application or mechanical dewatering, and 10 for discharge to a raw water source.
Estimating Solids Production
A common estimate for alum coagulation is:
Doses are in mg/L. Raw-water suspended solids are often approximated as 1 to 2 times the raw turbidity in NTU.
Worked example. A 4.0 MGD plant doses 25 mg/L alum and adds 3 mg/L PAC. Raw suspended solids average 12 mg/L.
- 0.44 × 25 = 11 mg/L of alum floc
- Total = 11 + 12 + 3 = 26 mg/L of solids
- Dry solids = 8.34 × 4.0 × 26 = 867 lb/day
At 1 percent solids, that is about 867 ÷ (8.34 × 0.01) ≈ 10,400 gallons per day of sludge. Thickening to 4 percent cuts the volume by about 75 percent.
Backwash Water Management
- Equalization: backwash water arrives in short, large surges, so it goes to a washwater recovery basin or lagoon where solids settle and flow can be metered back slowly.
- Recycling: under the federal Filter Backwash Recycling Rule, conventional and direct filtration plants that recycle SFBW, thickener supernatant or dewatering liquids must return them through all treatment processes, at or before the point of primary coagulant addition. Recycle flow must be limited so it does not overload the plant, and the practice must be documented and reported.
- Discharge to surface water: sending backwash or settled supernatant to a stream is a point-source discharge needing DEQ coverage. DEQ's 200-J NPDES general permit covers filter backwash; other cases need an individual permit. Chlorine residual and solids must meet permit limits, which often means dechlorination and settling.
- Discharge to sanitary sewer: allowed only with the receiving utility's approval and pretreatment conditions. Large alum slugs can upset a small wastewater plant.
Thickening and Dewatering
- Gravity thickeners concentrate coagulant sludge, sometimes with polymer.
- Lagoons settle solids over months. They are periodically decanted, allowed to dry, and the solids removed. Freeze-thaw cycles in colder parts of Oregon help dewater alum sludge.
- Sand drying beds work for small plants in dry summer climates.
- Mechanical dewatering (belt presses, centrifuges, screw presses, plate-and-frame presses) produces cake from about 15 to over 35 percent solids, depending on the sludge and equipment.
Disposal Routes
- Landfill: the cake must pass the paint filter liquids test, meaning no free liquid drains through a standard paint filter in 5 minutes.
- Land application: alum and ferric residuals can be land-applied with approval. They bind phosphorus, so agronomic suitability matters.
- Beneficial use: lime residuals for agricultural liming; alum residuals for soil amendment or phosphorus control.
- Concentrate disposal (RO and NF): sewer discharge, surface discharge under permit, deep-well injection where allowed, or evaporation ponds. Concentrate often decides whether RO is practical at all.
Operating Tips
- Record sludge volumes, solids percentages and polymer use so you can spot changes in raw water or coagulant performance.
- Do not let recycle streams carry high turbidity or pathogens back to the head of the plant during upsets. Divert or hold them.
- Treat residual handling areas as part of plant security and spill planning. Lagoon berms, decant structures and chemical cleaning wastes all need inspection.
Worked Example: Thickening Volume Reduction
Thickening removes water, not solids, so the dry solids mass stays the same while the volume shrinks.
Example. A plant withdraws 50,000 gallons of alum sludge at 1.0 percent solids from its basins and gravity-thickens it to 4.0 percent.
- Dry solids = 50,000 gal × 8.34 lb/gal × 0.010 ≈ 4,170 lb
- Thickened volume = 50,000 gal × (1.0 ÷ 4.0) = 12,500 gallons
Quadrupling the solids concentration cuts the volume to one quarter. That shrinks the hauling, lagoon space or dewatering capacity the plant needs. The 37,500 gallons of separated water become supernatant, which goes back to the head of the plant under the recycle rules or out under a discharge permit.
Residuals Lagoon Operation
Many small and medium Oregon plants send coagulant sludge and backwash solids to lined lagoons or drying beds:
- Fill and decant: route flow to one cell while another settles. Decant clear supernatant from the surface, and do not draw down so far that settled solids resuspend.
- Rest and dry: take a full cell out of service so solids can drain and dry before removal. In colder parts of the state, freeze-thaw cycles break up gelatinous alum sludge so it drains far better after thawing.
- Remove and haul: track solids depth with a sludge judge. Plan removal before solids reduce settling volume and carry over into the decant.
- Records: log volumes sent to each cell, decant volumes and quality, and quantities hauled, with destinations, for permit and sanitary survey review.
Under the Filter Backwash Recycling Rule, where must a conventional plant return recycled spent filter backwash water?
Into the distribution system at a booster station with chlorine added
Through all treatment processes, at or before primary coagulant addition
Into the filter effluent channel, to save treatment capacity in the plant
Directly into the clearwell after disinfection, ahead of the high-service pumps
A 2.5 MGD plant doses 30 mg/L alum, and raw suspended solids average 10 mg/L with no other additives. Using the common estimate, how many pounds of dry solids does it produce per day?
about 1,450 lb/day
about 484 lb/day
about 834 lb/day
about 208 lb/day
A small Oregon filtration plant wants to discharge settled filter backwash supernatant to the creek below the plant. What does it need first?
A recycled water use plan approved by DEQ under OAR 340-055
DEQ NPDES coverage, such as the 200-J general permit, and its limits
Only a sign-off from OHA during the next scheduled sanitary survey
Nothing, because backwash water is already treated drinking water
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