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Biofouling Control Companies
Biofouling monitoring and control, biocides, chlorine dioxide, UV, and membrane cleaning programs.
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Designing Biofouling Prevention Programs for Industrial Water Systems
Biofouling — the accumulation of biofilm (bacterial slime, fungi, algae, mussels) on heat exchangers, RO membranes, cooling tower fill, condensers, and pipework — degrades heat transfer coefficient 30–70%, increases pumping energy 10–30%, and shortens equipment life. Prevention strategies stack three layers: shock disinfection (chlorination to 1–5 mg/L free residual, monochloramine to 1–3 mg/L for higher pH cooling water, peracetic acid at 5–20 mg/L for chlorine-sensitive systems), continuous biocide dosing (DBNPA 5–25 mg/L, glutaraldehyde 50–200 mg/L, isothiazolinones at 1–10 mg/L), and dispersant programs to detach and flush biofilm.
Monitoring is the leverage point. ATP bioluminescence quantifies viable microbial load in under 60 seconds; biofilm coupon racks installed on side-streams measure accumulation gravimetrically and by FTIR; Legionella culture under ISO 11731 is mandatory for cooling towers under EU EN 16975 and ANSI/ASHRAE 188. Online ATP and oxidation-reduction-potential monitoring closes the loop on biocide dosing, replacing fixed-dose programs with demand-driven control that typically reduces chemical consumption 20–40%.
Macrofouling — zebra mussels, quagga mussels, Asian clams — affects intake structures in surface-water systems and is controlled by chlorination at 0.5–1 mg/L for 21–30 day mussel-mortality programs or thermal shock above 40°C for 30+ minutes. Aguato lists biofouling-prevention providers with proven references across cooling towers, RO desalination intakes, power-station condensers, and industrial recirculating systems.
Frequently Asked Questions
What biocide regime do I use for an open recirculating cooling tower?
Best practice combines a continuous halogen feed (free chlorine 0.2–0.5 mg/L or monochloramine 0.5–1 mg/L for pH above 8.5) with weekly shock dosing of a non-oxidizing biocide (isothiazolinone, glutaraldehyde, or DBNPA) at 50–100 mg/L for 4–8 hours. Add dispersant (polyacrylate or phosphonate at 5–15 mg/L) and rotate non-oxidizers quarterly to prevent resistant strains. Monitor ATP weekly and Legionella monthly.
How do I monitor biofilm in real time on an RO skid?
Install ATP test points on feed, mid-stage permeate, and concentrate to track viable microbial load. Place biofilm coupon racks on side-streams of each stage for monthly gravimetric and FTIR analysis. Track normalized differential pressure weekly — a 15% rise from baseline signals biofouling onset. Online DO, ORP, and chlorine residual probes close the feedback loop. Advanced sites use SAXS or quartz crystal microbalance for laboratory-grade kinetics.
What's the difference between biofouling and scaling?
Biofouling is biological — slimy, brown-to-green, soft, ATP-positive, removed by oxidation. Scaling is mineral — hard, white-to-gray, crystalline, removed by acid. Quick field tests: glutaraldehyde swab turns biofouling slick; 5% HCl dissolves scale. SEM/EDX of a coupon resolves the mix. Most RO and cooling failures involve both — biofouling traps precipitating ions, accelerating scale.
Are oxidizing biocides safe for RO membrane systems?
Polyamide RO membranes are damaged by free chlorine above 0.1 mg/L cumulative exposure (above 1,000 ppm-hours). Chlorination is typically applied upstream of sodium-bisulfite quench cartridges (SBS dosed at 1.5 to 3 times chlorine residual). Monochloramine is more membrane-tolerant (up to 0.5 mg/L continuous) but slower-acting. Non-oxidizing biocides (DBNPA, isothiazolinones) are preferred for direct membrane disinfection when biofouling resists oxidative shock.
Recurring biofouling on condenser tubes was reducing heat-transfer coefficient by 35% within 6 weeks of chemical dosing cycles. ATP counts regularly exceeded 5 million RLU/mL despite continuous chlorination at 0.3 mg/L free residual. Legionella culture results twice exceeded Ofwat risk threshold of 1,000 CFU/100mL in a 12-month period.
A biocide rotation programme replaced single-biocide continuous chlorination with alternating DBNPA shock dosing (75 mg/L, 4 hours, weekly) and glutaraldehyde (100 mg/L, 4 hours, fortnightly), supported by online ATP probes and ORP control on the chlorine dosing. Biofilm dispersant (polyacrylate at 10 mg/L continuous) and annual mechanical cleaning of fill pack were added.
ATP counts fell below 500,000 RLU/mL within 8 weeks and remained below 1 million RLU/mL for 18 months. Legionella culture stayed below 100 CFU/100mL. Heat-transfer efficiency recovered to design levels, saving an estimated GBP 280,000/year in fuel and GBP 65,000 in unplanned maintenance.
Questions to Ask Shortlisted Providers
- 1
What is your biocide rotation protocol and how do you verify efficacy against resistant strains?
Single-biocide programmes breed resistant biofilm communities within 6 to 12 months. Rotation with chemical class switching (oxidising, isothiazolinone, quaternary ammonium) is essential for sustained control.
- 2
Do you provide online ATP or ORP monitoring, and how is dosing feedback-controlled?
Fixed-dose biocide programmes waste chemical and underdose during high-load periods. Demand-driven dosing tied to ATP or ORP feedback reduces chemical spend 20 to 40% while maintaining tighter microbial control.
- 3
What is your Legionella monitoring protocol and how does it align with BS 8580-1 and HSE ACOP L8 obligations?
Cooling tower operators have a statutory Legionella control duty under ACOP L8. Vendors should define sampling frequency (monthly culture, weekly ATP), trigger levels, and corrective action thresholds explicitly.
- 4
How do you handle macrofouling risk from zebra or quagga mussels in surface-water intake systems?
Macrofouling by invasive mussels can block intake screens and condenser water-boxes within weeks. Vendors must specify chlorination duration and concentration for mussel mortality (0.5 mg/L for 21 days minimum).
- 5
What are your biocide discharge consents and Environment Agency reporting obligations for your proposed programme?
Biocide-containing blowdown discharging to controlled waters requires Trade Effluent Consent or Environmental Permit. Vendors should confirm compliance pathway before proposing any chemical regime.
What Drives Cost in This Category
Continuous halogen dosing costs GBP 15K to 60K/year per tower in chemical alone. Adding non-oxidiser shock doses and dispersants increases chemical cost 30 to 60% but reduces fouling-related downtime costs that typically exceed chemical savings.
Online ATP analysers cost GBP 15K to 40K per installation. Real-time Legionella monitors (PCR-based) cost GBP 50K to 120K. Both reduce statutory monitoring labour and enable demand-driven dosing that typically recoups capital in 2 to 3 years.
Annual fill pack cleaning costs GBP 8K to 30K per tower but is mandatory under ACOP L8. Skipping it leads to biofilm reservoir build-up that chemical programmes cannot overcome.
Monthly Legionella culture (ISO 11731) at GBP 80 to 150 per sample adds GBP 1K to 2K/year per tower. More frequent sampling during risk events or high ATP counts can triple laboratory expenditure.
Key Regulations & Standards
The Approved Code of Practice L8 and its Technical Guidance HSG274 Part 1 set out the legal duty for cooling tower Legionella risk assessment, written scheme, and routine monitoring. Non-compliance with ACOP creates a presumption of negligence in prosecution.
The British Standard defines the risk assessment methodology that must precede any biofouling control programme for cooling towers, hot and cold water systems, and spa pools. Assessors should be competent and ideally UKAS-accredited.
Blowdown from biocide-dosed cooling systems discharging to sewer requires Trade Effluent Consent from the local water company. Direct discharge to controlled waters requires an Environmental Permit from the Environment Agency.
All biocides used in water treatment must be authorised under BPR Product Type 11 (slimicides for cooling/process systems). Using unauthorised biocides is a criminal offence. WRAS approval is additionally required for potable water contact applications.







