2026-07-16 14:49:59
The vacuum level of surface condensers in power plants directly affects steam turbine output and power generation efficiency. Calcium and magnesium ions along with microorganisms in the circulating cooling water continuously deposit on heat exchanger tube walls, forming calcium carbonate scale layers and biofouling slime that reduce heat transfer coefficients and increase turbine back pressure. In severe cases, this forces units to operate at reduced load or even undergo unplanned shutdowns. Electrochemical water treatment technology removes hardness ions in situ through cathodic alkalization while synergistically inhibiting microbial attachment, with the titanium anode for cooling circulating water treatment serving as its core component.
Electrochemical Scale Prevention and Biofouling Control: Synergistic Mechanisms of In-Situ Crystallization and Active Chlorine
Traditional chemical scale inhibition and biocide dosing solutions require continuous addition of antiscalants and biocides, with chemical costs increasing as cycles of concentration rise and the burden of chemically-laden blowdown water disposal correspondingly intensifying. Electrochemical technology addresses both scaling and biofouling through two synergistic mechanisms by creating a controlled reaction environment within a circulating water side-stream unit.
In an electrolysis unit with the titanium anode at its core, the water reduction reaction on the cathode surface generates hydroxide ions, forming a localized high-pH micro-zone adjacent to the cathode. Within this micro-zone, bicarbonate ions convert to carbonate ions, prompting calcium and magnesium ions to preferentially crystallize and precipitate as calcium carbonate and magnesium hydroxide on the cathode surface, rather than depositing on condenser heat exchanger tube walls. Simultaneously, the titanium anode, when energized, utilizes the inherent chloride ions present in the circulating water to generate active chlorine species in situ. These species diffuse with the water flow throughout the condenser piping system, acting on microbial cell structures and helping to inhibit the attachment and growth of biofouling slime on tube walls. Periodic removal of cathode deposits through mechanical scraping or polarity reversal supports continuous online system operation without the need for shutdown cleaning. Actual scale prevention and biofouling control effectiveness vary depending on circulating water hardness, chloride ion concentration, cycles of concentration, and operating current density.
Performance varies based on specific operating conditions. Actual results depend on circulating water quality and operating parameters.

Anode Durability: Adapting to Long-Term Operation in High-Temperature Circulating Water
Power plant circulating cooling water operates at elevated temperatures, with significant salt accumulation and correspondingly rising chloride ion concentrations during high cycles of concentration operation. Anodes operating long-term in such high-temperature, high-salinity environments face the dual challenges of coating electrochemical activity decay and substrate corrosion. Additionally, organic matter and suspended solids in the circulating water may adsorb on the electrode surface, affecting active site accessibility.
The titanium anode for cooling circulating water treatment employs high-purity titanium as the substrate. The titanium substrate can form a dense passive film under anodic polarization conditions, providing structural stability for the electrode in chloride-containing high-temperature circulating water. The coating adopts an electrocatalytic active layer containing metal oxides such as IrO₂ and RuO₂. The IrO₂ component exhibits high electrochemical stability under both chlorine and oxygen evolution conditions, contributing to maintaining the catalytic activity of the coating during long-term operation. The coating and substrate achieve high bonding strength through optimized pretreatment processes, supporting the maintenance of structural integrity in high-flow, high-temperature circulating water. Through periodic polarity reversal, deposits on the electrode surface can be removed, maintaining chlorine and oxygen evolution efficiency. Actual working life varies depending on circulating water temperature, chloride ion concentration, hardness, and operating mode.
Engineering Value for the Power Generation Facilities Market
In the global power generation market, condenser vacuum maintenance is a critical factor affecting steam turbine efficiency and operational reliability. The engineering value of the titanium anode for cooling circulating water treatment in this market lies in integrating cathodic scale prevention and anodic biofouling control functions within a single electrochemical unit, supporting power plants in maintaining condenser heat exchange efficiency without heavy reliance on chemical agents.
Online electrochemical treatment solutions use electric current as the driving force, helping to reduce the continuous dosing of antiscalants and biocides and lowering chemical residues in blowdown water. These titanium anode products are built on high-purity titanium substrates and coated with metal oxide systems such as IrO₂ and RuO₂, and can be customized into plate, mesh, tubular, and other geometric configurations to suit circulating water side-stream treatment devices of different scales. It is recommended that power plant operators and industrial water treatment engineering firms conduct field condition testing of titanium anodes for cooling circulating water treatment based on their circulating water quality, cycles of concentration, and condenser operating parameters. By tracking indicators such as condenser vacuum variation trends, heat exchanger tube cleanliness factor, and long-term anode operating performance, the technical compatibility and comprehensive energy-saving benefits of the electrochemical treatment solution in specific power generation scenarios can be evaluated.
Important Note: The performance descriptions above are based on engineering experience under specific test conditions or internal test data. Differences may exist between laboratory results and actual operating conditions. Actual scale prevention and biofouling control effectiveness, working life, and the impact on condenser vacuum vary depending on circulating water quality, hardness, chloride ion concentration, temperature, cycles of concentration, operating parameters, and system design. This product is an industrial circulating water treatment equipment component, and its suitability for specific applications must be verified by the user according to actual operating conditions and relevant industry standards.
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