Titanium equipment supplier Baoji City Changsheng Titanium Co.,Ltd

Corrosion and Protection in Chlor-Alkali Production

1. Main corrosive substances in chlor-alkali production
1.1.Caustic Soda
Caustic soda, as a key raw material and product in chlor-alkali production, is present throughout the entire production line. This includes caustic injection and production in the electrolysis workshop, concentration and storage in the evaporation tank area, pH adjustment of brine in the brine workshop, and chlorine absorption in the chlorine-hydrogen treatment workshop. Caustic soda itself is highly corrosive and directly impacts the performance of production equipment, potentially affecting the production process and leading to safety incidents. During the concentration process of liquid caustic soda, corrosion of production facilities becomes more severe, especially for certain metal equipment. If effective anti-corrosion measures are not implemented, it can result in serious safety production accidents.

1.2.Chlorine
Chlorine is one of the key products in the chlor-alkali production phase and a significant factor contributing to the corrosion of production facilities. Chlorine is highly reactive and has strong oxidizing properties, particularly when the water content exceeds a certain level. Moist chlorine, mixed with HCl and HClO, can easily corrode a variety of metal materials. Numerous experiments have shown that the corrosiveness of chlorine is closely related to temperature — generally, the higher the temperature, the stronger the corrosiveness. The moisture level in the air also significantly affects chlorine’s corrosiveness; lower air humidity typically results in weaker corrosive effects. Chlorine usually reacts with water first, producing more corrosive substances that further react with metals like nickel and iron. Only a few metal elements can resist its corrosiveness. Another situation arises when the water content in chlorine is less than 0.5%, producing dry chlorine, which can react with titanium to form unstable TiCl4, a substance prone to explosion.

1.3 Hydrochloric Acid
Hydrochloric acid is one of the key products in chlor-alkali production, known for its extremely reactive chemical properties and strong corrosiveness. It can react with most metals, leading to significant corrosion of production equipment. The corrosive effect of hydrochloric acid differs in the presence or absence of oxygen. For example, in an oxygen-free environment, it reacts strongly with iron but does not corrode copper. However, in an oxygen-rich environment, both iron and copper can suffer severe corrosion. Hydrochloric acid reacts with reactive metals, and through these reactions with metal elements in the equipment, it causes the equipment to be corroded and eroded.

2. Corrosion Protection Measures in Chlor-Alkali Production
2.1 Common Anti-Corrosion Strategies for Caustic Soda
In environments with normal temperatures, alkaline solutions with a concentration of less than 30% can form an oxide protective film on the surface of carbon steel, resulting in minimal corrosion. However, the corrosion resistance of carbon steel often varies with changes in the concentration of the alkaline solution and environmental temperature. The higher the temperature or concentration, the weaker its corrosion resistance becomes. Specifically, when the concentration of caustic soda exceeds 30%, the oxide protective film on the surface of the carbon steel is damaged, exposing the metal to the alkaline solution and causing severe corrosion. For instance, iron ions react with sodium hydroxide to form soluble Na₂FeO₂, which can continue to corrode the metal and lead to significant equipment damage. When the solution temperature exceeds 80°C, the combination of high temperature, high concentration alkaline solution, and external stress often leads to corrosion at welding points, causing cracks that are difficult to repair by welding. Therefore, it is essential to select appropriate anti-corrosion materials based on the actual concentration and temperature conditions of the caustic soda solution.

The chromium in austenitic stainless steel undergoes oxidation reactions with corrosive substances, forming a protective film on the surface of the steel that provides corrosion resistance. In a 40% sodium hydroxide solution at 100°C, the corrosion rate of austenitic stainless steel is less than 0.05 mm/a. Low-carbon stainless steels, such as SUS304 and SUS310S, have low yield strength but high flexibility. When the concentration of sodium hydroxide is around 30% and the temperature is approximately 90°C, these low-carbon stainless steels exhibit good resistance to stress corrosion. As a result, ultra-low carbon austenitic stainless steels are often chosen for non-standard equipment or piping.

Catholyte circulation tanks and caustic outlets are exposed not only to high-temperature, highly alkaline substances but also to electrical currents. For these facilities or surrounding pipes, nickel or carbon steel is often used as lining material. When the sodium hydroxide concentration exceeds 50% and the temperature is above 85°C, nickel materials are typically used. To reduce the alkali embrittlement of carbon steel, strict material control is essential. Additionally, heat treatment is frequently applied to weld joints, and weld joint inspections are enhanced to reduce the impact of external forces.

2.2 Common Corrosion Protection Strategies for Chlorine
The chlorine gas generated from the electrolysis of brine typically has a temperature between 75°C and 85°C and contains a large amount of water vapor, making it moist chlorine. Moist chlorine has strong oxidizing properties and can react with metals like iron and copper, leading to severe corrosion of production equipment. To address this issue, corrosion protection measures must be strengthened, such as using titanium or fiberglass materials for moist chlorine pipelines. Titanium is a highly reactive material, but at room temperature, it forms an oxide protective film on its surface that can resist the corrosion of moist chlorine, hypochlorous acid, and other oxidizing acids. Titanium also has good electrical resistance, can withstand high current densities, and maintains stable geometric properties, which effectively extends the service life of production facilities.

In the current chlor-alkali industry, especially during the process of removing moisture from moist chlorine or during cooling, titanium pipes are used to resist chlorine corrosion. Additionally, many other devices, such as anolyte storage tanks, dechlorination towers, scrubbing towers, and coolers, are also made from titanium. At room temperature, titanium can resist hydrochloric acid corrosion at concentrations below 10%, and at 50°C, it can resist 3% hydrochloric acid corrosion. Therefore, when selecting titanium materials for chlorate decomposition, it is essential to carefully control the concentration of hydrochloric acid

Since titanium reacts strongly with dry chlorine, potentially causing severe fire accidents, titanium equipment cannot be used with dry chlorine. To ensure the proper application of titanium materials, the water content in chlorine should be kept above 1.5%. Carbon steel, on the other hand, exhibits strong stability in dry chlorine environments below 90°C, making it suitable for use in materials for chlorine compressors and some pipelines that transport dry chlorine after cooling. It is important to strictly control the temperature below 90°C.

In facilities where dry chlorine and circulating water are used for heat exchange, protective coatings are typically applied to the surface of the pipes to prevent corrosion caused by chloride ions (Cl−) in the circulating water, thereby enhancing corrosion resistance. Additionally, rubber is a commonly used anti-corrosion material, often used as a lining in metal equipment, due to its excellent impermeability and corrosion-resistant properties.

2.3.Common Corrosion Prevention Measures for Acids

Hydrochloric acid is highly corrosive and reacts chemically with active metals, often causing severe damage to production equipment. Equipment in contact with hydrochloric acid typically uses carbon steel lined with hard rubber to enhance its corrosion resistance. For hydrochloric acid with strict requirements on calcium and magnesium content, rubber with low calcium and magnesium content should be used for the lining. Given hydrochloric acid’s strong permeability, crystallization issues often arise at certain temperatures, leading to cracks in the lining. Therefore, regular inspections of rubber linings are necessary. If significant damage is detected, repairs should be made promptly to prevent pipeline ruptures that could disrupt production. In some processes with low flow rates and pressures, CPVC (Chlorinated Polyvinyl Chloride) material can be used for pipelines to provide convenient maintenance and management while resisting hydrochloric acid corrosion.

Fiberglass-reinforced plastic (FRP) has excellent physical flexibility and good corrosion resistance, making it easy to process and shape. It is often used as a lining for pipelines to protect against hydrochloric acid corrosion. Fluoroplastics, known for their strong corrosion resistance and high-temperature endurance, are also effective as liners, though their high production costs and difficulty in forming make them less commonly used. Impermeable graphite offers excellent resistance to hydrochloric acid corrosion and can withstand temperatures of 2000-3000°C, as well as 400°C in oxidative environments. As a result, graphite is often used in hydrochloric acid synthesis processes.

In chlor-alkali production, other acidic corrosives like sulfuric acid and hypochlorous acid can also cause corrosion to metal equipment. PVC (Polyvinyl Chloride) is highly corrosion-resistant and can withstand corrosion from dilute nitric or sulfuric acids. However, PVC’s thermal resistance is weak, typically only functioning under temperatures of up to 65°C, and its flexibility is poor, making it prone to deformation. From a cost and lifespan perspective, carbon steel is commonly used for concentrated sulfuric acid transport pipelines. Hypochlorous acid pipelines often use PVC or CPVC materials, while low-temperature hydrochloric acid pipelines also frequently use CPVC. For short-distance transport, PE (Polyethylene) pipes supported by pipe racks are suitable, while high-temperature hydrochloric acid pipelines require steel-lined PTFE (Polytetrafluoroethylene) or steel-lined PO (Polyolefin) materials.

Considering the environmental impact of acidic substances, their transportation usually occurs in sealed environments with minimal leakage to prevent environmental damage.

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