Scaling Prevention
Antiscalants inhibit calcium carbonate, sulfate, and silica precipitation, allowing higher recovery and longer membrane life.
Customized chemical programs to prevent scaling, fouling, biofouling and to maximise membrane life and RO system efficiency.
Site‑specific feedwater evaluation and tailored RO chemistry programs. Typical response within 48 business hours.
RO systems require precise feedwater conditioning to avoid scaling, organic fouling, biofouling, and irreversible membrane damage. Cleanflo's approach combines lab‑backed feedwater analysis, tailored antiscalant and cleaning programs, and continuous monitoring to extend membrane life, reduce CIP frequency, and lower operating costs.
Antiscalants inhibit calcium carbonate, sulfate, and silica precipitation, allowing higher recovery and longer membrane life.
Dispersants and biocides keep organics, colloids, and microorganisms suspended and away from membrane surfaces.
Alkaline and acidic cleaners restore flux and salt rejection when fouling occurs, with protocols validated by membrane compatibility.
Cleanflo delivers prevention‑first RO programs: from feedwater characterisation to chemical selection, dosing, and performance tracking — all backed by our accredited laboratory.
Each untreated foulant leads to operational penalties: frequent cleaning, energy waste, premature membrane replacement.
Calcium carbonate, sulfate, silica scales reduce permeate flow, increase differential pressure, and shorten membrane life.
Humic acids, oils, silts form a cake layer, reducing flux and increasing cleaning frequency.
Microbial growth and EPS formation increase pressure drop and reduce salt rejection; can lead to permanent membrane damage.
Brown/black deposits cause irreversible membrane staining and require aggressive cleaning.
Oxidizers, incompatible cleaning chemicals, or physical abrasion permanently damage membrane performance.
Increased osmotic pressure raises energy demand; scaling risk limits recovery percentage.
Engineered formulations for every stage of RO operation — from pre‑treatment to CIP.
Purpose: Prevent precipitation of CaCO₃, CaSO₄, BaSO₄, SrSO₄, and silica scales.
Mechanism: Crystal distortion and dispersion at substoichiometric doses.
Monitoring: LSI, conductivity, calcium and silica residuals.
Benefit: Higher recovery, longer membrane life, reduced cleaning.
Purpose: Keep silt, clays, and organics suspended to prevent cake layer.
Mechanism: Anionic polymers impart particle repulsion.
Monitoring: SDI, turbidity.
Purpose: Control microbial growth; remove existing biofilm.
Types: Oxidizing (chlorine, bromine, chlorine dioxide) with DBNPA shock dosing; non‑oxidizing (isothiazolinones, glutaraldehyde).
Monitoring: ATP, residual biocide, microbial counts.
Purpose: Optimize pH to minimize scaling (e.g., silica above pH 8, carbonate below pH 7).
Benefits: Enhances antiscalant performance, stabilizes feedwater chemistry.
Alkaline cleaners: remove organics, biofilms, colloids.
Acid cleaners: dissolve inorganic scales (carbonates, sulfates).
Chelants: target iron/manganese.
CIP protocols validated with membrane compatibility.
Sequestrants (e.g., phosphonates, polymers) keep soluble iron in solution; pre‑oxidation strategies for particulate removal.
Prevent foaming in concentrate and permeate lines, especially during CIP operations.
Polymers and passivators to condition membranes and reduce irreversible fouling between CIP cycles.
A structured, six-step methodology ensures every chemical program is tailored to your site conditions.
Raw water sampling, lab tests: TDS, hardness, silica, alkalinity, iron, manganese, TOC, SDI, microbial load, turbidity.
Identify needs for multimedia filtration, softening, antiscalant, cartridge filtration, UV/chlorine control.
Antiscalant type, dosing point, target residual; CIP chemistry and schedule defined.
Validate antiscalant performance and CIP efficacy before full‑scale deployment.
Baseline flux, differential pressure, salt rejection, SDI; online meters (conductivity, pH).
Periodic sampling, CIP triggers, chemical tuning, performance reporting. KPIs: permeate flux (L/m²·hr), normalized salt rejection, recovery %, CIP frequency, SDI targets.
Chain‑of‑custody and accredited lab reporting (NABL where applicable).
SDI/SDI15, turbidity, TOC/DOC, UV254, ATP, microbial counts, ICP metals, silica by colorimetric/ICP.
Daily: online conductivity/flow. Weekly: SDI, permeate checks. Monthly: full lab panels (adjusted per site conditions).
Post‑cleaning flux recovery, salt rejection restoration; membrane autopsy if needed.
Antiscalant residuals: typically 2–6 ppm (dose confirmed by jar test).
CIP: alkaline cleaning at pH 11–12, acidic at pH 2–3; contact time 30–60 minutes, temperature 30–40°C.
pH ranges: acid dosing to reduce LSI, base dosing for silica control.
Membrane compatibility: always validate with manufacturer on oxidant exposure and cleaning chemicals.
Safety: PPE required (gloves, goggles, apron); neutralise cleaning waste before disposal; follow local discharge regulations.
Every RO application has unique feedwater chemistry demands — our programs are tailored accordingly.
From power plants to pharma — Cleanflo RO programs are trusted across critical industries.
High‑purity make‑up, stringent silica limits.
High‑purity RO, validation support.
Product water, process water reuse.
Coastal BWRO/SWRO, high recovery.
ZLD, recycling, concentrate management.
Typical improvements: CIP frequency reduced by 30–50%, system recovery increased by 5–10% points.
Fewer replacements, lower capex (typical life 3–7 years with proper chemistry).
Reduced chemical consumption, less downtime, lower opex.
Lower freshwater make‑up, reduced brine volume for disposal.
Consistent salt rejection, meeting product water specifications.
Sustained flux reduces pump energy consumption over time.
Silt Density Index measures colloidal fouling potential. SDI below 5 is recommended for RO feed; higher values require pre‑treatment.
When normalized pressure drop increases 10–15% or permeate flux drops 10–15%, or every 3–6 months as preventive maintenance.
Polyamide membranes are damaged by chlorine >0.1 ppm. Use non‑oxidizing biocides or remove oxidants with sodium bisulfite.
Monitor LSI, calcium and silica in reject stream; stable differential pressure indicates effective scale control.
Full feedwater analysis: TDS, hardness, alkalinity, silica, iron, manganese, TOC, SDI, microbial count.
Maintain soluble iron with sequestrants; pre‑oxidise and filter if particulate; acid CIP may be needed.
Discuss your feedwater challenges with our membrane specialists.
Our team will reach out to you as soon as possible.
Complete industrial water treatment programs backed by 45+ years of expertise.
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