Safely decommissioning an old primary clarifier

A primary clarifier can remain in service for decades, quietly supporting solids removal while the rest of a wastewater treatment plant is modernized around it. Eventually, however, aging concrete, obsolete equipment, limited capacity, or a new treatment process can make retirement the safer and more practical option.

The following case study is based on a representative Los Angeles Basin wastewater facility. The project involved taking an old primary settling tank out of service while keeping treatment operations stable, protecting workers from confined-space hazards, and preparing the site for future process improvements.

Decommissioning was treated as a controlled engineering project rather than a demolition task. That distinction shaped every decision, from the first inspection to final backfill and documentation.

Why the clarifier had to go

The circular clarifier had been built in the 1960s and had reached the end of its useful operating life. Its concrete walls showed cracking and localized spalling, the mechanism bridge had experienced repeated corrosion repairs, and the collector drive required parts that were increasingly difficult to obtain. Operators also reported uneven sludge withdrawal and poor scum-skimming performance during high-flow periods.

The plant had enough hydraulic flexibility to remove the tank from service after minor process adjustments. A newer clarifier and improved screening system could handle the expected flow, but only if the remaining units were carefully balanced. The project team therefore evaluated structural condition, hydraulic capacity, odor control, electrical systems, underground piping, and future site use together.

The decision was approved after a condition assessment showed that continued operation would require substantial rehabilitation with limited long-term benefit. Retirement reduced operational risk and created space for a future equalization or solids-handling improvement.

Building a safe decommissioning basis

The first step was to develop a decommissioning basis of design. Engineers documented the tank geometry, influent and effluent channels, sludge piping, scum lines, wash-water connections, electrical feeds, chemical interfaces, and nearby buried utilities. Old record drawings were compared with field measurements because several modifications had been made without appearing in the original plans.

A hazard analysis covered biological exposure, hydrogen sulfide, methane, oxygen deficiency, residual sludge, unstable concrete, energized equipment, mobile cranes, falling objects, and unexpected flows. The clarifier was classified as a confined-space concern even though the tank was open to the atmosphere. Atmospheric conditions could change inside the tank, particularly near sludge deposits and enclosed pipe galleries.

The team also prepared a management-of-change package. It defined temporary operating conditions, alarm responses, bypass limits, shutdown authority, communication procedures, and restart criteria. Operators, maintenance staff, contractors, safety personnel, and the plant’s electrical and instrumentation specialists reviewed the package before field work began.

Preparing the plant and people

Isolation began with process verification rather than valve turning. Operators traced the clarifier’s flow path from the headworks through the distribution channel and confirmed which gates controlled neighboring units. Each isolation point was tagged, locked, and independently verified. Where a valve did not provide reliable positive isolation, the team installed a blind or physical separation.

The clarifier was drained in stages so that staff could observe changes in nearby channels and confirm that no unintended flow entered the basin. Remaining sludge was pumped to the solids-handling system under an approved waste profile. Washdown water was collected, sampled as required, and routed to a permitted treatment point instead of being discharged uncontrolled.

Before entry, workers completed confined-space training, rescue drills, respiratory-protection reviews, and task-specific briefings. A calibrated four-gas monitor was used for oxygen, hydrogen sulfide, carbon monoxide, and combustible gases. The entry plan required continuous monitoring, an attendant, retrieval equipment where appropriate, and a rescue capability independent of the entering crew.

The project team used daily pre-task meetings to address weather, crane movements, traffic separation, changing plant conditions, and simultaneous operations. This helped prevent a common failure mode in industrial demolition: treating each activity as isolated when several crews are working around the same structure.

Managing isolation, residuals, and demolition

After isolation, the mechanism bridge, drive assembly, scum baffle, weirs, access platforms, and electrical components were removed in a planned sequence. Reusable stainless-steel parts were separated from carbon steel and contaminated materials. Equipment was de-energized, drained, and inspected before cutting or lifting.

Residual sludge presented the greatest sanitation and exposure concern. Workers avoided dry scraping wherever possible, using pumping and low-pressure washdown to limit aerosols. Areas that could not be cleaned immediately were restricted and marked. Waste containers were covered, labeled, and removed from active work zones to reduce odor and contact hazards.

Structural demolition followed the engineer’s sequence. The upper wall and bridge supports were removed first, while the basin floor and selected wall sections were retained temporarily to control debris and protect adjacent piping. Saw cutting was preferred near active utilities because it produced more predictable loads than uncontrolled breaking. A lifting plan specified crane capacity, pick points, exclusion zones, wind limits, and spotter responsibilities.

Dust, noise, and vibration were monitored because the clarifier was close to operating treatment units. Concrete debris was tested and characterized before recycling or disposal. Once demolition ended, exposed pipe ends were capped, abandoned conduits were documented, drainage was checked, and the area was secured against unauthorized entry.

Comparing execution options

Three approaches were evaluated before construction. Full demolition offered the greatest future flexibility, while partial demolition reduced cost and disturbance. Leaving the empty tank in place required the least immediate work but preserved structural and maintenance liabilities.

Execution approach Primary benefit Main risk or limitation Suitable use
Full removal Maximum space and future flexibility Highest cost, noise, and utility exposure Sites needing a new structure or major reconfiguration
Partial demolition Balances cost and site access Remaining concrete may restrict future layouts Sites retaining a slab or converting the basin
Clean, isolate, and leave in place Lowest immediate disturbance Long-term inspection and liability remain Sites with limited funding or no near-term redevelopment

For this facility, partial demolition was selected. The floor and a controlled portion of the outer wall were retained after engineering review. This choice reduced vibration near a live effluent channel and provided a stable base for a future project, while removing the deteriorated bridge, internal equipment, upper wall sections, and accessible process piping.

The decision also reflected lifecycle cost. A cheaper first phase would have been less attractive if it required repeated inspections, odor control, or future removal of contaminated residuals. The selected approach created a documented, maintainable condition rather than simply stopping operation.

What the project taught the team

The most important lesson was that operating continuity must be designed into the demolition plan. The plant maintained treatment performance by adjusting flow distribution, increasing inspection frequency at active clarifiers, and establishing trigger points for reducing influent or pausing construction. These measures gave operators time to respond before a process upset became an emergency.

Documentation proved equally valuable. The closeout package included updated utility drawings, photographs of capped lines, waste manifests, atmospheric-monitoring records, equipment disposition, inspection reports, and the final area survey. Future teams will be able to distinguish abandoned systems from live infrastructure without relying on memory or outdated drawings.

The project also showed the value of professional knowledge-sharing. Case studies, facility tours, and technical presentations help water professionals compare approaches to confined-space work, residuals management, structural assessment, and process continuity. Relevant updates can be followed through the LABS of CWEA technical newsletters, which connect local practitioners with practical developments across the water environment field.

Recommendations for safer future projects

A successful clarifier retirement depends on disciplined preparation and clear ownership. The following practices should be built into the project from the earliest planning stage:

For water and wastewater professionals, the case reinforces a broader principle: decommissioning is part of asset management. A retired primary clarifier still affects safety, hydraulics, maintenance, environmental compliance, and future construction until the site is formally closed out.

LABS of CWEA supports the exchange of this kind of practical experience through education, workshops, facility tours, and professional events. Share project needs, training interests, or technical questions with contact LABS of CWEA and take part in strengthening safe, reliable water infrastructure across the Los Angeles Basin.