2026-06-18 14:38:02
Ruthenium-iridium oxide (RuO₂-IrO₂) is a metal oxide (MMO) coating used for chlorine precipitation during brine treatment. It features a low chlorine precipitation overpotential, reducing the energy consumption of active chlorine. RuO₂-IrO₂ coated electrodes are used in seawater electrolysis systems, swimming pool chlorination tanks, and drinking water electrolysis disinfection devices.
|
.Parameter |
Specification |
|
Coating composition |
RuO₂ : IrO₂ |
|
Coating thickness |
6 – 20 µm |
|
Operating temperature |
≤ 60 °C (continuous) |
|
Recommended current density |
100 – 800 A/m² |
|
Electrolyte compatibility |
NaCl, seawater, KCl, brackish water |
IrO₂-Ta₂O₅ coatings are designed for oxygen evolution environments with low or no chloride ion concentrations. The high tantalum content ensures the coating remains stable in acidic or neutral electrolytes, preventing anodic dissolution. Electrodes with IrO₂-Ta₂O₅ coatings are used in electrodeionization (EDI), electrodialysis (ED), and advanced oxidation process (AOP) reactors.
|
Parameter |
Specification |
|
Coating composition |
IrO₂ : Ta₂O₅ |
|
Coating thickness |
8 – 25 µm |
|
Operating temperature |
≤ 70 °C |
|
Recommended current density |
50 – 500 A/m² |
|
Electrolyte compatibility |
Sulfate, phosphate, carbonate, low-chloride solutions |
For applications requiring ozone or hydroxyl radical generation (such as advanced oxidation water treatment), titanium anodes coated with lead dioxide (PbO₂) or boron-doped diamond (BDD) are used. PGM-coated electrodes have a high oxygen evolution overpotential, generating ozone and hydroxyl radicals on the anode surface instead of releasing oxygen.
|
Parameter |
Specification |
|
Coating type |
PbO₂ / BDD / SnO₂-Sb₂O₃ |
|
Recommended current density |
100 – 2000 A/m² (BDD) |
|
Ozone generation efficiency |
5 – 15% current efficiency (electrolyte-dependent) |
|
Operating temperature |
≤ 50 °C |
|
Electrolyte compatibility |
Dilute sulfate, phosphate, low-conductivity water |
In water treatment, the performance of the anode depends not only on the coating system but also on the purity and microstructure of the titanium substrate.
|
Parameter |
Specification |
|
Substrate material |
Titanium Grade 1 or Grade 2 (ASTM B265) |
|
Titanium purity |
≥ 99.5% Ti |
|
Density |
4.51 g/cm³ |
|
Tensile strength |
240 – 345 MPa (Grade 1); 345 – 450 MPa (Grade 2) |
|
Corrosion resistance |
Resistant to Cl⁻, F⁻, O₃, H₂O₂, HClO at working pH |
|
Operating pH range |
0 – 14 (coating-dependent) |
|
Available forms |
Plate, mesh, rod, tube, wire, perforated sheet |
|
Standard mesh opening |
4 × 8 mm / 6 × 12 mm / custom |
|
Plate thickness |
1.0 – 5.0 mm |
|
Maximum operating voltage |
8 – 12 V (system-dependent) |
Titanium mesh, which ensures electrolyte circulation while maintaining electrode surface area, is widely used in flow-through electrochemical reactors. Plate and rod-shaped titanium meshes are used in static tank reactors and electrolyzers.
Unlike graphite anodes, which erode at rates of 1–3 kg per ton of chlorine produced, the electrode maintains its geometry throughout the operating life of the coating. Dimensional stability preserves the electrode gap in electrochemical cells, ensuring consistent current distribution and predictable reaction rates without process re-calibration.
MMO-coated electrodes in chlorine evolution service achieve 8–20 years of continuous operation before coating reactivation or recoating is required. The titanium substrate itself has an indefinite service life and can be recoated multiple times, reducing long-term material consumption compared to consumable electrode types.
The low chlorine evolution overpotential of RuO₂-IrO₂ coated electrodes — typically 40–60 mV lower than graphite at equivalent current density — translates directly into reduced cell voltage and lower power consumption per unit of disinfectant produced. In large-scale seawater electrolysis systems, this reduction represents measurable operating cost savings over multi-year periods.
These electrodes do not introduce metal ions into the treated water stream. Lead-based anodes used in older electrolytic chlorination systems release lead ions under anodic polarization. MMO-coated electrodes produce no dissolution products under normal operating conditions, which is critical for drinking water treatment compliance.
Many water treatment systems — including electrolytic scale prevention and electrocoagulation units — operate with periodic current reversal to prevent electrode fouling. Electrodes with appropriate MMO coatings tolerate polarity reversal without delamination or accelerated coating degradation, provided the reversal frequency and cathodic current density remain within specified limits.
When the active coating reaches end of life — indicated by rising cell voltage at constant current — the titanium substrate can be stripped, etched, and recoated. Recoating restores full electrode performance without replacing the structural titanium component, which represents the majority of the electrode material cost.
1: Electrolytic Chlorination and Sodium Hypochlorite Generation
The titanium anode is the electrode in a sodium hypochlorite (NaOCl) generator, producing disinfectant through the electrolysis of brine or dilute salt solutions. It is used in municipal drinking water treatment, wastewater disinfection, and cooling tower water management.
The RuO₂-IrO₂ coated electrode operates at a current density of 150–500 A/m² in a bipolar plate electrolytic cell. An electrochemical reaction on the anode surface generates chlorine gas, which hydrolyzes in the alkaline cathode electrolyte to form hypochlorite. In brine electrolysis, the electrode's lifespan is negatively correlated with the operating current density and the presence of fluorides or silica in the feed brine.
Coastal power stations, desalination plants, offshore platforms, and marine facilities use electrochemical systems with titanium anodes to produce active chlorine from seawater for biofouling control in intake pipelines and heat exchanger systems.
Seawater electrolysis cells use titanium plates or expanded mesh operated at 100–300 A/m² in flowing seawater. The high chloride content of seawater provides efficient chlorine generation without brine preparation. Electrodes in seawater service are typically coated with ruthenium-iridium oxide formulations optimized for high-chloride, low-temperature operation .
Electrocoagulation water treatment uses sacrificial iron or aluminum anodes for coagulant generation, but titanium serves as the inert counter-electrode substrate (cathode in standard polarity, anode during reversal) to maintain system geometry and avoid iron contamination in systems with polarity reversal cycles.
In combined systems, MMO-coated titanium anodes produce oxidants at the anode surface simultaneously with coagulant generation, treating industrial wastewater streams containing dyes, oils, heavy metals, and suspended solids. Applications include textile wastewater, food processing effluent, and surface finishing wastewater treatment.
Electrodeionization (EDI) and electrodialysis (ED) systems for ultrapure water production and desalination use titanium anodes to sustain the direct current field across ion exchange membranes. The anode chamber in EDI systems operates in oxygen evolution mode; IrO₂-Ta₂O₅ coated electrodes are specified for this service due to their stability in low-chloride, mildly acidic anode compartment conditions.
EDI systems for semiconductor-grade ultrapure water require electrodes that do not release trace metal ions under operating conditions, as contamination limits for ionic species in ultrapure water are below 1 µg/L.
Salt water chlorination (SWC) systems electrolyze low-concentration NaCl solutions, using titanium anode cells to generate hypochlorous acid in situ. The anodes in SWC units operate at relatively low current density (50–200 A/m²) and moderate temperature (25–35 °C), conditions that favor extended coating life.
Self-cleaning cells with automatic polarity reversal remove calcium carbonate scale from electrode surfaces in hard water regions, maintaining consistent chlorine output without manual descaling.
Electrochemical oxidation treats industrial wastewater streams where biological processes are inhibited by toxicity, salinity, or recalcitrant compound content. Applications include:
· Cyanide destruction: Anodic oxidation converts cyanide (CN⁻) to cyanate and then to nitrogen and CO₂ in metal finishing and mining wastewater.
· Chromate reduction systems: Titanium anodes in indirect electrochemical systems generate reducing agents or pH-control ions for hexavalent chromium precipitation.
· Ammonia removal: Electrochemical breakpoint chlorination using titanium anodes oxidizes ammonia nitrogen in landfill leachate and agricultural runoff.
· Color and COD reduction: MMO and BDD coated anodes degrade color bodies and reduce chemical oxygen demand (COD) in textile, paper mill, and pharmaceutical effluent.
When the coating reaches end of service life — typically indicated by cell voltage increase of 10–20% above initial operating value at constant current — the electrode is removed for evaluation. The recoating process involves:
1. Incoming inspection — visual assessment of substrate deformation, coating delamination, and dimensional check
2. Chemical stripping — removal of spent oxide coating using oxalic acid or HCl/HNO₃ solution
3. Surface preparation — abrasive blasting and acid etching to restore titanium substrate surface activity
4. MMO recoating — Thermal decomposition of fresh precursor solution in repetitive cyclic coatings
5. Quality verification — coating thickness (XRF), adhesion (peel test), and electrochemical activity confirmation
Recoating restores electrode performance to original specification. The substrate typically withstands 3–5 recoating cycles before substrate thinning from etching requires replacement.
Titanium anodes serve as the electrochemically active component across a broad range of water treatment Titanium anodes are electrochemically active components used in a variety of water treatment processes, from municipal drinking water disinfection to industrial wastewater treatment. The coating type, substrate form, and current density depend on the target electrochemical reaction, the water chemistry, and the required electrode lifespan for each application.
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