11.1 Trickling Filters & Attached Growth Fundamentals
Key Takeaways
- A trickling filter is not a filter in the straining sense; it is an attached-growth bioreactor where wastewater trickles over media carrying a fixed biological slime layer.
- Sloughing is the normal periodic release of excess biofilm and appears as a temporary rise in effluent suspended solids that the secondary clarifier must capture.
- Recirculation dilutes strong influent, maintains continuous wetting during low flow, and helps control ponding and filter flies.
- Ponding indicates media plugging from excessive biofilm or debris and is corrected by increasing hydraulic loading, flooding the bed, or chlorinating the dosing water.
- Filter flies breed in a bed that stays dry between dosing intervals, so continuous wetting and periodic flooding are the primary controls.
11.1 Trickling Filters & Attached Growth Fundamentals
A trickling filter is a bed of media over which settled wastewater is distributed, allowing a biological slime layer (biofilm) growing on the media to remove organic matter as the water trickles past. The name is misleading — nothing is strained. It is a fixed-film or attached-growth bioreactor, in contrast to activated sludge, which is a suspended-growth process.
Fixed-film processes are common at smaller Arizona plants because they use far less energy than aeration, tolerate shock and intermittent loading, need less operator attention, and recover quickly from upsets.
The Biology
Wastewater flows over a biofilm attached to the media. Within that film:
- The outer aerobic layer contacts oxygen from air moving through the bed and does the organic removal.
- As the film thickens, oxygen cannot penetrate to the media surface, and the inner layer turns anaerobic.
- The anaerobic layer loses its grip on the media, and a patch of film detaches. This is sloughing.
Sloughing is normal and necessary. It removes excess biomass and is the process's equivalent of wasting sludge. It appears at the secondary clarifier as a temporary increase in effluent suspended solids, and heavy sloughing after a warm spell or a loading change can briefly degrade effluent quality. Excessive or wholesale sloughing, by contrast, signals a toxic load, a pH excursion, or a hydraulic surge.
Air movement through the bed is driven by natural draft from the temperature difference between the wastewater and the ambient air, and it reverses direction seasonally. Underdrains must stay clear and vents unobstructed; a plugged underdrain suffocates the bed. In cold weather natural draft weakens, which is one reason performance drops in winter — though in Arizona the more common problem is summer heat reducing oxygen solubility and driving odors.
Media
| Media | Specific surface area | Depth | Characteristics |
|---|---|---|---|
| Rock | Low (about 12 to 20 ft²/ft³) | Shallow, 3 to 8 ft | Heavy, prone to plugging, limited loading |
| Plastic (modular/cross-flow) | High (about 27 to 45+ ft²/ft³) | Deep, up to 20 to 40 ft | Light, high void ratio, resists plugging, allows high loading |
| Random plastic | Moderate to high | Variable | Dumped rather than stacked |
| Redwood/wood slat | Low | Moderate | Largely historical |
Plastic media transformed the process: its high void ratio permits far higher organic loading without ponding, and its light weight allows tall towers with a small footprint.
The Distributor
Most trickling filters use a rotary distributor: two or four arms with orifices, rotating on a center column.
- Rotation is normally driven by reaction force from the discharging jets (hydraulic drive); some are motor driven.
- Dosing rate, expressed in inches of liquid applied per pass of the distributor arm, controls how the bed is wetted. Higher instantaneous dosing with fewer passes flushes the media and controls flies and ponding.
- Routine maintenance: unplug orifices, check arm level, service the center column seal and bearing, and adjust the end gates that balance the arms.
Loading Calculations
Hydraulic Loading
Total flow applied includes recirculation.
Organic Loading
Worked example. A rock trickling filter is 80 ft in diameter and 6 ft deep. Primary effluent is 1.1 MGD at 140 mg/L BOD.
That figure places the unit in the high-rate range for a rock filter.
Recirculation Ratio
If influent is 1.0 MGD and 1.5 MGD is recirculated, the ratio is 1.5:1 and total applied flow is 2.5 MGD.
Why recirculate:
- Dilutes strong or toxic influent, protecting the biofilm
- Maintains continuous wetting at night and during low flow, which prevents the film from drying and prevents filter fly breeding
- Increases hydraulic flushing, controlling ponding
- Improves treatment by giving wastewater additional passes
- Returns dissolved oxygen to the applied flow
Classification by Loading
| Type | Organic loading (lb BOD/day/1,000 ft³) | Recirculation | Effluent |
|---|---|---|---|
| Low-rate (standard) | 5 to 25 | Little or none | Well nitrified, high quality |
| Intermediate | 15 to 30 | Some | Moderate |
| High-rate | 25 to 300 | Always | Less nitrification |
| Roughing | Over 100 | Yes | Pretreatment ahead of another process |
Low-rate filters nitrify well because the low organic loading lets slow-growing nitrifiers compete for space on the media. Heavily loaded filters are dominated by fast-growing heterotrophs and nitrify poorly — the same competition that governs sludge age in activated sludge.
Operating Problems
| Problem | Cause | Correction |
|---|---|---|
| Ponding | Media plugged by excess biofilm, debris, or media breakdown | Increase hydraulic loading or recirculation; flood the bed for 24 hours; chlorinate the dosing water; rake or replace media |
| Filter flies (Psychoda) | Bed dries between doses, allowing larvae to develop | Continuous wetting through recirculation; periodic flooding; higher instantaneous dosing rate; targeted chlorination |
| Odors | Anaerobic conditions from overloading or poor ventilation | Increase recirculation and ventilation; clear underdrains; reduce load |
| Heavy sloughing | Toxic load, pH shock, hydraulic surge, or seasonal change | Identify and control the source; clarifier must handle the solids |
| Poor effluent | Overloading, short-circuiting, distributor plugging | Verify loading, level the arms, clear orifices |
| Distributor stops | Plugged orifices, bearing or seal failure, debris | Clear orifices, service the center column |
[!IMPORTANT] Ponding and filter flies have the same primary fix from opposite directions: both are controlled by managing how the bed is wetted. Ponding needs flushing, and flies need the bed never to dry out. Increasing recirculation addresses both, which is why it is the first operational lever an operator reaches for.
A trickling filter 70 ft in diameter and 20 ft deep receives 1.5 MGD of primary effluent at 120 mg/L BOD. What is the organic loading rate?
An operator observes standing water on the surface of a rock trickling filter and, separately, a heavy population of filter flies around the structure. Which single operational change addresses both problems?
A low-rate trickling filter operating at 12 lb BOD/day/1,000 ft³ produces a well-nitrified effluent, while a high-rate filter at 90 lb BOD/day/1,000 ft³ at the same plant produces almost no nitrification. What explains the difference?