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Stainless Steel for Chemical Processing

Chemical service cannot be selected from a generic corrosion chart alone. Concentration, contaminants, temperature, aeration, velocity and crevices can change performance completely. Final material approval remains with the project engineer.

Illustrative stainless steel reactor and chemical-process piping

Corrosion and Failure Mechanisms

  • Pitting and crevice corrosion in halide-bearing process streams
  • Stress-corrosion cracking under combined chloride, temperature and tensile stress
  • General corrosion in reducing acids outside an alloy's useful range
  • Preferential attack or phase imbalance after uncontrolled welding

Common Selection Risks

  • Selecting from chemical name without concentration, contaminants and temperature
  • Using a generic corrosion chart as a design guarantee
  • Mixing pipe, fitting, flange and weld-metal grades without one material specification

Recommended Stainless Steel Grades

Typical Supply Requirements

ProcessChemical identity, concentration and temperature
DesignPressure, thickness and corrosion allowance
ProductsPlate, pipe, fittings and flanges as one package
InspectionPMI, NDT and hydrotest as specified

Related Product Forms

What to Include in Your RFQ

Related Grade Comparisons

Frequently Asked Questions

When should 2205 replace 316L?

Use 2205 when chloride pitting or stress-corrosion cracking threatens 316L and its higher strength adds design value.

Is 904L always better than 2205?

No. 904L suits selected reducing acids; 2205 is stronger and often better in chloride service. Process conditions decide.

Why is PMI important?

Many grades look identical. Positive material identification helps prevent grade mix-ups before fabrication or shipment.

Technical content updated: 2026-07-29

Organizational author: Tsingshan (Shandong) Iron & Steel Co., Ltd..Review method, status and limitations.

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