AQUChem

Scale & Corrosion Inhibitors for Cooling Water, Boiler & Closed-Loop Systems

11 active ingredients across 4 inhibitor families — phosphonates (HEDP/ATMP/PBTCA), copper/metal deactivators (BTA/TTA), anodic inhibitors (molybdate/nitrite), and cathodic inhibitors (zinc/phosphate).

Quick-Pick by System

System TypeScale RiskCorrosion RiskPrimary InhibitorCorrosion InhibitorMetal Deactivator
Open Recirculating Cooling Water (carbon steel)CaCO₃, CaSO₄General corrosionHEDP 10–30 ppmZinc phosphate 2–5 ppm Zn²⁺
Open Recirculating Cooling Water (copper alloys present)CaCO₃, CaSO₄Pitting + galvanicPBTCA 5–15 ppmZinc phosphate 1–3 ppm Zn²⁺BTA 1–3 ppm
Once-Through Cooling WaterCaCO₃ (mild)Low — short residenceHEDP 2–8 ppm
Low-Pressure Boiler (<10 bar)CaSO₄, silicaOxygen corrosionHEDP or ATMP 5–20 ppmSodium molybdate 50–200 ppm
Medium-Pressure Boiler (10–60 bar)Silica, magnetiteCO₂ + O₂ corrosionPhosphate alkalinity controlSodium sulfite or DEHA (oxygen scavenger)
Closed Cooling Loop (chiller circuit)Low — no evapGalvanic + creviceHPMA dispersant 50–100 ppmSodium nitrite 500–1500 ppm or molybdate 200–500 ppmBTA 10–30 ppm
District Heating / Hot Water LoopLowOxygen ingress corrosionSodium molybdate 200–500 ppm or nitriteBTA 5–20 ppm
Desalination Concentrate SystemCaSO₄, BaSO₄Low pH corrosionATMP 5–15 ppm + HEDP 5–10 ppm

All Grades (by chemistry class)

Phosphonate Scale Inhibitors — HEDP, ATMP, PBTCA, HPMA(4)

The workhorses of modern scale inhibition. Phosphonates chelate calcium and magnesium ions at the crystal nucleation stage (threshold effect), preventing CaCO₃ and CaSO₄ scale from forming at doses 100–1000× below stoichiometric. HEDP is the all-rounder; ATMP excels at silica and calcium phosphate inhibition; PBTCA provides combined scale + mild corrosion inhibition; HPMA (polymaleic acid) is a dispersant-grade polymer for particulate suspension.

Metal Deactivators — Benzotriazole (BTA), Tolyltriazole (TTA)(2)

Azole-type copper and copper-alloy corrosion inhibitors. BTA (benzotriazole) and TTA (tolyltriazole / methylbenzotriazole) form a chemisorbed monomolecular film on copper, brass, and bronze surfaces, reducing corrosion rate from ~200 μm/year to <5 μm/year. Essential in systems containing brass heat exchangers or copper tube condensers. TTA has slightly better thermal stability than BTA above 80°C.

Anodic Corrosion Inhibitors — Sodium Molybdate, Sodium Nitrite(2)

Anodic inhibitors passivate the metal surface by forming a stable protective oxide layer at anodic sites. Sodium molybdate (Na₂MoO₄) is the premium choice for closed-loop and mixed-metallurgy systems — non-toxic, synergistic with zinc and phosphate, effective 50–500 ppm range. Sodium nitrite is the workhorse for closed cooling loops at 500–2000 ppm but requires biocide co-dosing to prevent nitrite-consuming bacterial growth.

Cathodic / Mixed Inhibitors — Zinc Sulfate, Zinc Phosphate, Sodium Gluconate(3)

Zinc ions precipitate as Zn(OH)₂ at cathodic sites, suppressing cathodic reduction reactions and limiting general corrosion. Zinc phosphate combines the cathodic zinc mechanism with phosphate anodic passivation — the most widely used corrosion inhibitor for open cooling systems. Sodium gluconate acts as both a chelant and cathodic inhibitor, especially in hard-water high-pH systems where zinc would precipitate.

Imported Brand → China Equivalent

Equivalents are indicative; verify against TDS for project-critical applications.

International Brand / GradeChina EquivalentMajor Chinese Producers
Dow Dequest 2010 (HEDP 60%)HEDP 60% liquid (GB/T 15894)淄博万昌 (Wanchang), 郑州鑫恒, 广州昊诺
Dow Dequest 2006 (ATMP 50%)ATMP 50% liquid淄博万昌, 武汉远城, 郑州鑫恒
Dow Dequest 2066 (PBTCA 50%)PBTCA 50% liquid淄博万昌, 郑州鑫恒, 上海赛默
Albemarle Aquatreat AR-540 (HPMA)HPMA 50% dispersant polymer郑州鑫恒, 上海赛默, 广州昊诺
ICL BK-310 (BTA powder 99%)BTA 99% powder (GB/T 2978)武汉远城, 南通精化, 上海精美
Vanderbilt Cuvan 826 (TTA 50% liquid)TTA (MBT) 50% solution武汉远城, 南通精化, 广州昊诺
ICL Sodium Molybdate 39.5%Sodium Molybdate 39% liquid九江格兰特, 武汉远城, 郑州鑫恒
Chemours (DuPont) MOLY 2067 programMolybdate + BTA closed-loop program郑州鑫恒配方产品, AQUChem 预配方
Enthone Corrshield NT (zinc phosphate program)Zinc phosphate + HEDP open cooling program淄博万昌, AQUChem 预配方
Buckman Busan 11-M1 (sodium nitrite closed loop)Sodium Nitrite 40% inhibitor + BTAAQUChem 预配方

Frequently Asked Questions

HEDP vs ATMP vs PBTCA — which phosphonate should I use?

HEDP for general CaCO₃ scale in cooling water and low-pressure boilers; ATMP for high-silica or calcium phosphate scale; PBTCA when you want combined scale inhibition plus mild carbon-steel corrosion protection in a single molecule.

HEDP (1-hydroxyethylidene-1,1-diphosphonic acid) is the industry benchmark — broad-spectrum threshold inhibitor against CaCO₃, BaSO₄, and CaF₂, compatible with virtually all cations (Zn²⁺, Ca²⁺, Mg²⁺) up to 400 mg/L calcium hardness. ATMP (aminotrimethylene phosphonic acid) has 5 phosphonate groups vs HEDP's 2, giving stronger calcium binding — preferred when silica > 100 ppm or when dosing into high-phosphate biological treated effluent (ATMP resists precipitation better than HEDP in high-phosphate environments). PBTCA (2-phosphonobutane-1,2,4-tricarboxylic acid) has the best thermal stability (stable to 120°C vs HEDP's 70°C) and is used in high-temperature cooling and process systems where HEDP would hydrolyze. All three lose effectiveness above pH 9.5 as calcium precipitates them — formulate programs to maintain pH 7.5–9.0.

Zinc phosphate vs molybdate vs nitrite — which corrosion inhibitor for my system?

Zinc phosphate for open cooling towers with carbon steel (cost-effective, widely accepted); molybdate for closed loops and mixed-metallurgy systems (non-toxic, no environmental issues); sodium nitrite for closed hot-water loops where molybdate cost is prohibitive (but mandates biocide co-treatment to prevent Nitrobacter).

Zinc phosphate is a mixed-mode inhibitor combining cathodic zinc passivation with anodic phosphate film formation on carbon steel — one of the most cost-effective combinations at $0.5–1.5/m³ treated water. The downside is zinc environmental discharge limits (EU IED Directive: 0.3–1 mg/L Zn in discharge); plants with strict effluent limits may need to move to all-organic or molybdate programs. Sodium molybdate is 5–10× more expensive than zinc compounds but carries no environmental discharge constraints and performs well across carbon steel, stainless steel, aluminum, copper, and galvanized steel simultaneously — ideal for closed-loop mixed-metallurgy HVAC chiller circuits where one inhibitor must protect everything. Sodium nitrite at 500–1500 ppm gives excellent closed-loop protection (same passivation mechanism as molybdate) at 1/10th the cost of molybdate, but nitrite-consuming bacteria (Nitrobacter) convert it to nitrate over months, destroying the inhibitor — add 50–100 ppm DBNPA or glutaraldehyde biocide annually to control this.

What is cycles of concentration and how does it affect inhibitor dosing?

Cycles of concentration (COC) measures how much the dissolved salts have concentrated vs makeup water. Higher COC = less blowdown water = better water efficiency, but increases scale and corrosion risk. Inhibitor programs must be tuned to the target COC (typically 3–6 for most towers).

At COC = 4, calcium hardness in the tower water is 4× the makeup, chlorides and sulfates are 4×, and the Langelier Saturation Index (LSI) may exceed +2 (severe scaling tendency) if inhibitors are not fed. The standard approach is: (1) calculate target COC from blowdown economics and water cost; (2) model the tower water chemistry at that COC (calcium, M-alkalinity, TDS, silica); (3) select inhibitors to suppress the dominant scale risk (CaCO₃ if LSI > +1, CaSO₄ if SO₄ × Ca > 500,000, silica if Si > 150 ppm); (4) dose inhibitor at a rate proportional to makeup flow, not blowdown. Automatic conductivity controllers maintaining blowdown are the standard control mechanism — pair with a chemical feed pump on the makeup line for inhibitor proportional dosing. For COC > 6, run monthly deposit coupon analysis to verify performance.

What are the environmental and regulatory constraints on phosphonate and zinc discharge?

EU IED and many national regulations limit total phosphorus in cooling-tower blowdown to 1–2 mg/L P and zinc to 0.3–1 mg/L Zn. This drives shifts from zinc-phosphonate programs to zinc-free molybdate or all-organic polymer programs in environmentally sensitive sites.

Phosphonate discharge is regulated as 'total phosphorus' in most jurisdictions — at COC 5 with HEDP dose 15 ppm in makeup, blowdown phosphorus is ~75 ppm P, far exceeding 1–2 mg/L limits if discharged direct to sewer or waterway. Options: (1) route blowdown to wastewater treatment plant that removes phosphorus biologically/chemically; (2) switch to phosphonate-free corrosion inhibitor programs (molybdate + BTA + organic polymer); (3) use precipitation treatment (lime + coagulant) on blowdown before discharge. Zinc at 2–5 ppm in tower water results in 10–25 ppm Zn in blowdown at COC 5 — readily exceeds most effluent limits. Zinc-free programs using molybdate or organic inhibitor combinations are available from AQUChem for sites with strict Zn limits. REACH: HEDP, ATMP, and PBTCA are not SVHC-listed as of 2026; sodium molybdate is on the SVHC candidate list (Article 59 inquiry, not yet Annex XIV).

How do I monitor scale and corrosion inhibitor performance on-site?

Use corrosion coupons (mild steel + copper, 30-day exposure, target <5 mpy carbon steel / <1 mpy copper), deposit coupons, and monthly water analysis (calcium, M-alkalinity, silica, phosphonate residual, pH, conductivity, Zn if used).

The complete monitoring program for an industrial cooling tower: (1) Online: conductivity (COC control), pH, temperature, flow; (2) Weekly grab sample: calcium hardness, M-alkalinity, chloride, TDS, pH, turbidity; (3) Monthly lab analysis: silica, total phosphorus (or phosphonate residual by IC/ICP), zinc (if dosed), total bacteria plate count, Legionella (risk-based); (4) Quarterly: coupon rack removal and analysis — weigh coupon before/after to get mpy (mils per year) corrosion rate; visual inspection for pitting, biological fouling, or scale deposits; (5) Annual: heat exchanger tube inspection (eddy current or visual), deposit analysis by XRF to identify scale mineral type. Phosphonate residual testing: HEDP and ATMP are measured by IC (ion chromatography) at 0.5–20 ppm range; simpler colorimetric kits (ferrous sulfate titration) are available for field use but less accurate. Legionella sampling: mandatory in EU per Cooling Tower Directive and UK L8 HSE guidelines; minimum quarterly in high-risk systems.

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