SMO 254

SMO 254 (UNS S31254) is a superaustenitic stainless steel with high molybdenum (6.0–6.5%), chromium (19.5–20.5%), and nitrogen content. Its PREN is typically 42-45. The alloy was developed for seawater and halide-containing media where conventional and high-alloy austenitic grades fall short.

1. Chemical Composition

The table below details the tightly controlled elemental composition of 254 SMO. Nitrogen and molybdenum are the primary strengthening and pitting-resistance agents.

Grade C Mn P S Si Cr Ni Mo N Cu Other
254SMO ≤ 0.020 ≤ 1.00 ≤ 0.030 ≤ 0.010 ≤ 0.80 19.50–20.50 17.50–18.50 6.00–6.50 0.18–0.25 0.50–1.00

Note: The narrow compositional window, especially for Mo (6.00–6.50%) and N (0.18–0.22%), is maintained to ensure consistent PREN between 42-45 and stable austenitic phase microstructure.

2. Mechanical Properties

The mechanical property values below are for 254 SMO in the solution-annealed condition as per ASTM and ASME requirements, applicable to seamless tube and pipe products.

Grade UNS Tensile Min, ksi (MPa) Yield Min, ksi (MPa) Elong. Min, %
S31254 ≥ 94 (650) ≥ 44 (300) ≥ 35 %

Note: 254 SMO has significantly higher yield strength than 904L or 316L because of nitrogen solid-solution strengthening. This allows reduced wall thickness at equivalent pressure ratings.

3. Equivalent Grade

The table maps 254 SMO across major international designation systems for use in engineering specifications, third-party inspection certificates, and global procurement documentation.

GRADE UNS GB JIS ISO DIN/EN GOST
ISC NEW
254SMO S31254 S31252 015Cr20Ni18Mo6CuN SUS312L X1CrNiMCuN20-18-7 1.4547 -

4. Key Technical Advantages

  • High PREN for Chloride Resistance: With a PREN [= %Cr + 3.3x%Mo + 16x%N] typically between 43 and 45, 254 SMO resists pitting initiation in seawater at temperatures up to 50-55°C and in chloride solutions where 316L, 317L, and 904L show active corrosion. It is the benchmark material for seawater service in this category.
  • Nitrogen-Enhanced Strength and Stability: The addition of nitrogen (0.18–0.22%) has a dual function. It provides solid-solution strengthening and a yield strength of roughly 50% above 316L. They also stabilize the austenitic phase, suppressing sigma phase formation during fabrication and elevated-temperature service.
  • Resistance to Stress Corrosion Cracking: The high nickel content (17.5–18.5%) combined with the austenitic structure provides 254 SMO high resistance to chloride-induced stress corrosion cracking (SCC). This failure affects lean austenitic grades at temperatures above 60°C.

Technical Note: 254 SMO requires welding with matching or overmatched filler metals (e.g., AWS ERNiCrMo-3 or ERNiCrMo-10) to preserve corrosion resistance in the weld metal. Standard 308/316 filler metals are not suitable. Post-weld heat treatment is generally not required due to the ultra-low carbon content. Solution annealing (1150–1200°C / water quench) may be beneficial after significant cold working to restore maximum corrosion resistance.

5. Common Manufacturing Standards

ASTM A312: Standard specification for seamless, welded, and heavily cold-worked austenitic stainless steel pipes. UNS S31254 is listed under the superaustenitic alloy group.

ASTM A213: Standard specification for seamless ferritic and austenitic alloy-steel boiler, superheater, and heat-exchanger tubes. S31254 is applicable for corrosion-sensitive heat exchanger service.

ASTM A269: Standard specification for seamless and welded austenitic stainless steel tubing for general service, applicable to S31254.

DIN EN 10216-5: Seamless steel tubes for pressure purposes, stainless steel (Grade 1.4547 equivalent).

GB/T 14976: Seamless stainless steel tubes for fluid transport, 015Cr20Ni18Mo6CuN designation.

Standards Comparison Table:

Standard ASTM EN/DIN JIS GB/T GOST
Seamless Pipe A312 S31254 EN 10216-5 (1.4547) GB/T 14976
Seamless Tube A213 S31254 EN 10216-5 (1.4547) GB/T 13296
Welded Tube A249 S31254 EN 10217-7 (1.4547) GB/T 12771

6. Primary Applications

  • Seawater Desalination: Multi-stage flash (MSF) and reverse osmosis (RO) plant piping, heat rejection tubes, and brine handling systems where continuous contact with high-salinity water at elevated temperatures demands PREN between 42-45.
  • Offshore Platform Process Piping: Topside process piping, sea chest inlet screens, and overboard systems on FPSOs and fixed offshore platforms where untreated seawater is the process medium.
  • Flue Gas Desulfurization: Absorber tower internals, spray nozzles, and recirculation pump casings in FGD systems handling hot, chloride-rich, sulfurous condensate at high flow velocities.
  • Marine Heat Exchangers: Shell-and-tube heat exchangers using seawater as the cooling medium, where tube pitting failure from warm seawater is the primary degradation concern.
  • Pulp Bleaching Circuits: Chlorine dioxide bleaching stages in kraft pulp mills where high-chloride bleach liquors at elevated temperatures are too aggressive for 317L or 904L.
Catalogue Phone E-mail Whatsapp