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MMO titanium anodes for on-site hypochlorite generation.

YIANTENG supplies Ru–Ir MMO titanium anodes in plate, mesh, rod and tube formats for prepared-brine electrochlorination cells. We match coating loading and active area to the customer’s brine concentration, target chlorine output, current density and duty cycle, and can reproduce replacement electrodes from drawings or samples. The stable titanium substrate and chlorine-evolution coating support controlled current distribution and project-specific service life.

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Grade 1 / 2

Titanium substrate

Ru–Ir MMO

Chlorine-evolution coating

Plate / mesh / rod / tube

Cell-matched electrode formats

Where on-site hypochlorite generation is used

Prepared-brine electrochlorination generates dilute sodium hypochlorite at the point of use and allows production to track actual disinfection demand. Typical duties include controlled residual disinfection in municipal drinking-water plants and distribution networks, final-effluent and reuse-water disinfection in wastewater facilities, and biofouling control in industrial cooling-water and process-water circuits. Electrode selection is governed by chloride concentration, target available-chlorine output, current density, water temperature, scaling tendency and duty cycle.

How electrochlorination produces hypochlorite

Prepared brine passes through a low-voltage electrolytic cell. Chloride is oxidized at the MMO anode, while water is reduced at the cathode. Chlorine then hydrolyses in water and forms hypochlorous acid/hypochlorite; the balance depends on pH and operating conditions.

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Chloride is activated

At the anode: 2Cl⁻ → Cl₂ + 2e⁻

Hydrogen is separated

At the cathode: 2H₂O + 2e⁻ → H₂ + 2OH⁻

Disinfectant is formed

Cl₂ + H₂O ⇌ HClO + H⁺ + Cl⁻, followed by the pH-dependent HClO/OCl⁻ equilibrium.

Why Ru–Ir MMO titanium is selected for electrochlorination

Unlike a consumable graphite body, an MMO anode separates the catalytic chlorine-evolution surface from the structural titanium substrate. This helps preserve electrode geometry, interelectrode spacing and current distribution while supporting compact, replaceable cell assemblies.

Engineering factorRu–Ir MMO titaniumGraphite
Active surfaceCatalytic Ru–Ir MMO layer designed for chlorine evolutionCarbon body participates in the anodic reaction and is consumed
Geometry in serviceTitanium carrier and active geometry remain comparatively stableDimensions and electrode gap change progressively with wear
Cell integrationPlate, mesh, rod and tube formats support compact cell layoutsBulkier sections and larger installation allowances may be required
Maintenance routeQualified recoating or electrode-assembly replacementConsumed graphite blocks require replacement

Why choose YIANTENG Ru–Ir MMO anodes

YIANTENG matches Ru–Ir coating formulation, oxide loading, titanium grade and exposed active area to brine chemistry, current density, cell geometry and operating cycle. The result is an electrode specification built around chlorine-production efficiency, coating integrity, predictable durability and the maintenance strategy of the generator.


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Efficient chlorine evolution

Typical acceptance values include a chlorine-evolution potential of ≤1.13 V and chlorine-evolution polarization of ≤40 mV, supporting stable anodic response when active area and current loading are correctly matched.

Uniform, well-bonded coating

Controlled surface preparation and thermal coating cycles target a coating-uniformity index of ≤15%. Where specified, reinforced mass-loss acceptance is ≤8 mg; coating adhesion and integrity are verified to the agreed project inspection method.

Verified accelerated durability

Accelerated-life acceptance is ≥40 h at 20,000 A/m² under the relevant HG/T 2471-2011 test method. Project coating loading is then selected for chloride level, operating current, duty cycle and target service life.

Polarity-reversal-ready design

Reversal-ready electrode structures and coating configurations are available for cells that periodically reverse polarity to manage scale. Reversal-life acceptance can be defined in 2.5% NaCl against the intended reversal frequency and operating cycle.

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