Alloy System
Fe-Ni-Cr + Mo, Cu, N
Strengthening
Solid Solution + N
Service Temp
−196 to 550 °C
What is Alloy 31? Alloy 31 (UNS N08031), also known as Nicrofer 3127 hMo, is a nitrogen-alloyed iron-nickel-chromium-molybdenum superaustenitic alloy developed by VDM Metals in 1990 to fill the performance gap between highly alloyed austenitic stainless steels and nickel-based alloys. Its chemistry combines 30–32% nickel for chloride stress-corrosion cracking resistance, 26–28% chromium for oxidizing acid protection, 6–7% molybdenum for pitting resistance, 1.0–1.4% copper for sulfuric acid passivation, and a deliberate 0.15–0.25% nitrogen addition that stabilizes the austenitic structure while sharply increasing pitting resistance (PREN ≈ 52). This balanced composition makes Alloy 31 — nicknamed “The Superior All-Rounder” — the optimal material for high-concentration sulfuric acid, seawater coolers, FGD systems, and severe chloride pitting service where Alloy 20 and 904L are insufficient but C-276 cost is not justified. HT PIPE supplies Alloy 31 in plates, seamless pipes, welded pipes, forged fittings, flanges, and round bars with full EN 10204 3.1 certification and ASTM G28 intergranular corrosion testing.
Chromium (Cr) ★
26.0 – 28.0%
Oxidizing acid + PREN driver
Molybdenum (Mo) ★
6.0 – 7.0%
Pitting & crevice resistance
Nitrogen (N) ★
0.15 – 0.25%
Austenite stabilizer + PREN
Copper (Cu) ★
1.0 – 1.4%
H₂SO₄ passivation
Alloy 31: The Superior All-Rounder
Alloy 31 (UNS N08031, DIN 1.4562) was introduced in 1990 by VDM Metals as Nicrofer 3127 hMo — an evolution of the earlier Nicrofer 3127 LC with higher molybdenum and a deliberate nitrogen addition. The alloy occupies a strategic position between highly alloyed austenitic stainless steels (904L, 254 SMO) and full nickel-based alloys (C-276, C-2000). Its iron-base composition with 30–32% Ni, 26–28% Cr, 6–7% Mo, 1.0–1.4% Cu, and 0.15–0.25% N delivers pitting resistance (PREN ≈ 52) approaching nickel alloys at 60–70% of the cost.
The nitrogen addition is the critical innovation. Nitrogen stabilizes the austenitic structure, allowing higher Cr and Mo contents without forming harmful intermetallic phases (sigma, chi) that plague older superaustenitics. Nitrogen also dramatically increases pitting resistance — in the PREN formula, nitrogen carries a coefficient of 16, far higher than Mo (3.3) or Cr (1.0). The result is an alloy that matches nickel-alloy corrosion performance in many environments while maintaining excellent fabricability and a pressure-vessel certification envelope of −196°C to 550°C (VdTÜV 509).
Compared to Alloy 20, Alloy 31 trades higher Cr, Mo, and nitrogen for superior high-concentration sulfuric acid and seawater pitting performance. Compared to 904L, the higher Mo + N pushes PREN from 36 to 52, enabling service in chloride environments that destroy 904L. Compared to Hastelloy C-276, Alloy 31 sacrifices some pure HCl and mixed-acid capability for a 30–40% cost reduction — making it the engineering optimum for FGD, seawater, phosphoric acid, and chlorine dioxide service.
Five Defining Advantages of Alloy 31
1. Sulfuric Acid Excellence
Outperforms Alloy 20 and 904L in high-concentration H₂SO₄ — copper enables passivation, Cr and Mo extend the passive range into concentrated and hot acid.
2. Severe Pitting Immunity
6–7% Mo + 0.15–0.25% N delivers PREN ≈ 52 — approaching C-276 (66) and far above 904L (36). CPT > 90°C in ASTM G48.
3. All-Round Corrosion Resistance
Handles reducing acids, oxidizing acids (boiling 67% HNO₃), alkaline and acidic halides, and chlorine dioxide — a true multi-environment alloy.
4. Wide Temperature Range
VdTÜV 509 pressure-vessel certified from −196°C to 550°C; ASME to 800°F (427°C). Impact ≥140 J/cm² at −196°C.
5. Weldable & Fabricable
Nitrogen-stabilized austenite preserves weldability and toughness. Weld with over-alloyed filler FM 59 (ERNiCrMo-13). Standard austenitic fabrication equipment applies.
Chemical Composition — ASTM B625 UNS N08031
The Fe-Ni-Cr-Mo-Cu-N chemistry defines Alloy 31’s position as a nitrogen-alloyed superaustenitic bridging stainless and nickel alloys. The very low carbon (0.015% max) plus nitrogen stabilization minimizes sensitization risk; the 6–7% Mo + nitrogen combination drives pitting resistance to nickel-alloy levels:
| Element |
Min (%) |
Max (%) |
Role |
| Iron (Fe) |
Balance |
— |
Base element — iron-base composition reduces cost vs. full nickel alloys while nitrogen stabilizes austenite. |
| Nickel (Ni) ★ |
30.0 |
32.0 |
SCC resistance + austenite stabilizer. Prevents chloride stress-corrosion cracking. Works with nitrogen to stabilize austenite at high Cr/Mo content. |
| Chromium (Cr) ★ |
26.0 |
28.0 |
Oxidizing acid + PREN driver. Forms protective Cr₂O₃ film. 26–28% Cr enables resistance to boiling 67% HNO₃ and oxidizing chloride environments. |
| Molybdenum (Mo) ★ |
6.0 |
7.0 |
Pitting & crevice resistance driver. Higher Mo than 904L (4.5%) and Alloy 20 (2–3%). Critical for seawater, FGD, and chloride pitting service. |
| Nitrogen (N) ★ |
0.15 |
0.25 |
Key alloying innovation. Stabilizes austenite (permits high Cr + Mo without sigma phase), boosts PREN (coefficient 16), increases solid-solution strength, improves weldability. |
| Copper (Cu) ★ |
1.0 |
1.4 |
H₂SO₄ passivation catalyst. Self-polarizes surface in sulfuric acid, shifting corrosion potential into passive range. Lower Cu than Alloy 20 (3–4%) — balance shifted toward Cr/Mo/N. |
| Manganese (Mn) |
— |
2.0 |
Deoxidizer; improves hot workability. Auxiliary austenite stabilizer. |
| Silicon (Si) |
— |
0.3 |
Deoxidizer during melting. Kept low to avoid sigma-phase promotion. |
| Carbon (C) |
— |
0.015 |
Ultra-low carbon — below L-grade threshold. Combined with nitrogen stabilization, minimizes sensitization risk in welded fabrications. |
| Phosphorus (P) |
— |
0.020 |
Impurity — controlled to prevent temper embrittlement and weld hot cracking. |
| Sulfur (S) |
— |
0.010 |
Impurity — tightly controlled for weldability and pitting resistance. |
★ Starred elements define Alloy 31’s corrosion performance — Cr, Mo, N, Ni, and Cu are the five functional pillars
PREN (Pitting Resistance Equivalent Number): PREN = %Cr + 3.3 × %Mo + 16 × %N = 27 + 3.3 × 6.5 + 16 × 0.2 ≈
52 (nominal). This places Alloy 31 well above 316L (~25),
Alloy 20 (~28), and 904L (~36), and approaches the super-austenitic 254 SMO (~46) and nickel alloys C-276 (~66) and C-2000 (~75). The high PREN reflects Alloy 31’s design focus on severe chloride pitting and crevice corrosion — seawater, FGD, and acidic halide service. For pure HCl or mixed reducing acids where C-276 and C-2000 retain an edge, validate by immersion testing.
Mechanical Properties — Room Temperature (Solution Annealed)
Alloy 31 is a solid-solution strengthened austenitic alloy. The 0.15–0.25% nitrogen addition provides significant solid-solution strengthening — yield strength is notably higher than 316L and 904L. Properties are stable in the solution-annealed condition. The alloy retains excellent toughness down to cryogenic temperatures, with impact energy ≥140 J/cm² at −196°C.
| Condition |
UTS (MPa) |
YS (MPa) |
Elongation (%) |
Hardness |
| Solution Annealed (ASTM B625) |
≥650 |
≥277 |
≥40 |
≤220 HB |
| Typical (20°C) |
~720 |
~340 |
~45 |
~190 HB |
Impact Toughness (Charpy V-Notch)
| Temperature |
Impact Energy |
Unit |
| Room temperature (20°C) |
≥185 |
J/cm² |
| Cryogenic (−196°C) |
≥140 |
J/cm² |
Elastic Constants & Physical Constants (Annealed at 20°C)
| Elastic / Physical Constant |
Value |
Unit |
| Modulus of Elasticity (Tension, E) |
~200 |
GPa (29.0 × 10³ ksi) |
| Shear Modulus (G) |
~78 |
GPa |
| Poisson’s Ratio (ν) |
0.29 |
— |
Physical Properties — UNS N08031
Alloy 31’s physical properties are comparable to other high-alloy austenitic stainless steels. The density (8.05 g/cm³) reflects the iron-base composition with substantial Ni, Cr, and Mo additions. The alloy is essentially non-magnetic in all conditions — the nitrogen-stabilized austenite is highly stable and does not transform under cold work.
| Property |
Value |
Unit |
| Density |
8.05 |
g/cm³ (0.290 lb/in³) |
| Melting Range |
1330 – 1370 |
°C (2426 – 2498 °F) |
| Specific Heat (at 20°C) |
~500 |
J/kg·K |
| Electrical Resistivity (at 20°C) |
1.04 |
μΩ·m |
| Coeff. of Thermal Expansion (20–100°C) |
~14.0 |
μm/m·°C |
| Magnetic Permeability |
~1.001 |
Non-magnetic |
Heat Treatment Procedures
Alloy 31 requires solution annealing to dissolve precipitates formed during hot or cold working and to restore full corrosion resistance and ductility. The ultra-low carbon content plus nitrogen stabilization reduce sensitization risk in welded fabrications, but solution annealing after cold work is recommended for severe service:
Step 1 — Solution Anneal
1150 – 1200 °C + Rapid WQ
Hold time ~30 min per 25 mm section thickness. Mandatory water quench. Dissolves carbides, nitrides, and any sigma/chi phase; restores full corrosion resistance.
Step 2 — Stress Relief (optional)
Avoid 600–1000 °C Range
Stress relief in the precipitation range promotes sigma and chi phases. If dimensional stability is required, use brief treatment below 500°C.
Step 3 — Post-Weld
As-Welded or Solution Anneal
Most applications accept as-welded service with over-alloyed FM 59 filler. For severe corrosion service (FGD, seawater), full solution anneal + pickling recommended.
CRITICAL NOTES:
Do not dwell in 600–1000°C range — high Mo + Cr promotes sigma (σ) and chi (χ) intermetallic precipitation, depleting the matrix of Cr/Mo and reducing corrosion resistance. Rapid cooling through this range is essential.
Mandatory water quench from solution temperature — air cooling is too slow for the high Mo content and will permit intermetallic precipitation.
Hot working range: 1150–1230°C. Do not allow material to fall below 1000°C before finishing. Solution anneal after hot working to restore properties and corrosion resistance.
Corrosion Resistance — The Superior All-Rounder
Alloy 31 was engineered to deliver nickel-alloy-level corrosion performance from an iron-base composition. The 26–28% Cr / 6–7% Mo / 0.15–0.25% N / 1.0–1.4% Cu combination produces a uniquely balanced corrosion profile: exceptional in high-concentration sulfuric acid, exceptional in oxidizing nitric acid, exceptional in chloride pitting and crevice corrosion, and durable in alkaline and acidic halide environments. This breadth of capability is what earns the alloy its “all-rounder” positioning.
Sulfuric Acid (H₂SO₄) ★ — DEFINING STRENGTH
Alloy 31’s signature capability — superior to Alloy 20 and 904L. The 1.0–1.4% copper addition self-polarizes the alloy surface in sulfuric acid (similar mechanism to Alloy 20 but lower Cu content), while the higher Cr (26–28%) and Mo (6–7%) extend the passive range into concentrated and hotter acid. In 50% H₂SO₄ at 80°C, Alloy 31 achieves corrosion rates below 0.05 mm/yr — matching C-276 performance at lower cost. This makes it the preferred material for high-concentration sulfuric acid service where Alloy 20 reaches its limit.
Phosphoric Acid (H₃PO₄) — Wet-Process Service
Excellent resistance to wet-process phosphoric acid. The high Cr and Mo content handles the chloride, fluoride, and sulfate contaminants typical of wet-process acid, while the alloy resists both general corrosion and erosion-corrosion in evaporators and heat exchangers. Used extensively in phosphoric acid concentrators and superphosphoric acid service.
Nitric Acid (HNO₃) — Boiling 67% Service
Excellent resistance, including to boiling 67% nitric acid (Huey test conditions). The 26–28% chromium content forms a stable Cr₂O₃ passive film that resists oxidizing acid attack. Corrosion rate in boiling 67% HNO₃ is approximately 0.03 mm/yr — superior to Alloy 20 (0.15), 904L (0.10), and even C-276 (0.30, due to Mo-bearing transpassive dissolution). This makes Alloy 31 a strong candidate for mixed nitric/sulfuric acid environments.
Chloride Pitting & Crevice Corrosion ★
Outstanding resistance. PREN ≈ 52 places Alloy 31 between 254 SMO and C-276. Critical pitting temperature (CPT) in ASTM G48 exceeds 90°C — far above 316L (~15°C), Alloy 20 (~35°C), and 904L (~50°C). This is the key capability that qualifies Alloy 31 for seawater coolers, FGD absorbers, and other chloride-rich service where pitting is the governing failure mode. The nitrogen contribution is decisive — removing nitrogen from the formula drops PREN by ~3 points.
Alkaline & Acidic Halides, Chlorine Dioxide
Excellent resistance in alkaline halide and acidic halide environments, and outstanding performance in chlorine dioxide (ClO₂) bleaching service — the dominant failure environment in pulp and paper bleach plants. The combination of high Cr, Mo, and N resists the aggressive oxidizing chloride conditions that destroy 316L and 904L bleach plant equipment.
Chloride Stress-Corrosion Cracking (SCC)
The 30–32% nickel content provides immunity to chloride SCC — the failure mode that limits 316L service life above 60°C in chloride environments. Combined with the high PREN, this makes Alloy 31 suitable for seawater and brackish water service at temperatures where 316L, 317L, and even 904L fail by SCC or pitting.
Intergranular Corrosion (IGC)
Passes ASTM G28 Method A in the solution-annealed condition. The ultra-low carbon (0.015% max) reduces sensitization risk, while nitrogen stabilization further limits chromium carbide precipitation. Welded fabrications retain good IGC resistance when proper low-heat-input procedures are followed. For severe service, post-weld solution anneal + pickling restores full IGC resistance.
Corrosion Rate Comparison — Alloy 31 vs Alloy 20 vs 904L vs C-276
| Environment |
Alloy 31 |
Alloy 20 |
904L |
C-276 |
| 50% H₂SO₄ at 80°C (mm/yr) |
<0.05 |
0.08 |
0.15 |
<0.05 |
| Boiling 67% HNO₃ (mm/yr) |
0.03 |
0.15 |
0.10 |
0.30 |
| G48 Pitting CPT (°C) |
>90 |
35 |
50 |
>95 |
| 10% HCl at 50°C (mm/yr) |
0.20 |
0.50 |
0.80 |
0.08 |
| Relative Cost Index |
4.0× |
2.0× |
3.0× |
5.0× |
Green = excellent; Red = unacceptable. Values are typical — actual performance depends on specific process chemistry, aeration, velocity, and contaminants. Note C-276’s poorer performance in boiling HNO₃ (Mo transpassive dissolution) vs Alloy 31’s Cr-driven resistance.
Grade Selection Guide — Alloy 31 Positioning
Alloy 31 is positioned as “The Superior All-Rounder” — the optimal choice when service conditions exceed the capability of Alloy 20 and 904L but the cost of C-276 is not justified. It delivers near-nickel-alloy pitting and sulfuric acid resistance at 60–70% of C-276 cost:
| Alloy |
H₂SO₄ Resistance |
Pitting Resistance |
Weldability |
Relative Cost |
| 316L |
★★ |
★★ |
★★★★★ |
$ |
| Alloy 20 |
★★★★ |
★★★ |
★★★★ |
$$ |
| 904L |
★★★★ |
★★★★ |
★★★★ |
$$$ |
| Alloy 31 |
★★★★★ |
★★★★★ |
★★★★ |
$$$$ |
| C-276 |
★★★★★ |
★★★★★ |
★★★★★ |
$$$$$ |
Alloy 31 Positioning: “The Superior All-Rounder”
Choose Alloy 31 when the corrosion environment exceeds Alloy 20 and 904L capability (high-concentration sulfuric acid, severe chloride pitting, seawater, FGD, chlorine dioxide) but the cost of
C-276 is not justified. Choose 316L for mild service where cost is critical. Choose
Alloy 20 for moderate sulfuric acid service. Upgrade to
C-276 or
C-2000 for pure HCl, mixed reducing acids, or the most aggressive environments where iron-base alloys reach their limit.
Key Applications
Alloy 31 is the workhorse material for FGD systems, seawater-cooled heat exchangers, pulp-and-paper bleach plants, and high-concentration sulfuric acid service where 316L, 317L, and 904L fail prematurely and C-276 cost is difficult to justify. Its balanced chemistry and broad corrosion capability make it the default upgrade specification when service conditions push beyond standard austenitic stainless steels:
| Application |
Components & Conditions |
| Flue Gas Desulfurization (FGD) ★ |
Absorber towers, inlet ducts, mist eliminators, and quenches in coal-fired power plant FGD systems. Handles SO₂-laden chloride-rich acidic environments where 316L/317L and 904L fail by pitting and crevice corrosion. |
| Pulp & Paper Bleach Plants |
Chlorine dioxide (ClO₂) bleaching equipment — towers, washers, piping, and storage tanks. The high Cr/Mo/N combination resists the aggressive oxidizing chloride environment that destroys 904L and duplex stainless. |
| Fine Chemicals & Organic Acid Synthesis |
Reactor vessels, heat exchangers, and piping handling organic acids, esters, and mixed acid catalysts. Especially suited to processes combining oxidizing and reducing conditions. |
| Wet-Process Phosphoric Acid |
Evaporators, heat exchangers, pumps, and piping in phosphoric acid concentrators. Handles H₃PO₄ with chloride, fluoride, and sulfate contaminants; resists both corrosion and erosion-corrosion. |
| Seawater / Brackish Water Heat Exchangers ★ |
Plate and tubular heat exchangers, cooling systems, and piping in coastal plants, LNG facilities, and offshore platforms. PREN ≈ 52 resists seawater pitting and crevice corrosion at elevated temperatures. |
| HPAL (High-Pressure Acid Leach) — Nickel/Cobalt Ore |
Autoclaves, flash vessels, and piping for high-pressure sulfuric acid leaching of laterite ores. Handles 80–100% H₂SO₄ at 250°C and high chloride content. |
| Oil & Gas Sour Service |
Downhole tubing, process piping, and pressure vessels in sour gas service. NACE MR0175 / ISO 15156 Level VI certified for acidic gas environments containing H₂S, CO₂, and chlorides. |
| Waste Acid Recovery & Salt Evaporation |
Spent acid regenerators, acid concentrators, and salt evaporators/crystallizers. Handles mixed chloride/sulfate acidic brines at elevated temperatures. |
Applicable Standards & Specifications
| Standard |
Product Form / Scope |
Notes |
| ASTM B622 / ASME SB-622 |
Seamless Pipe & Tube |
Primary seamless pipe spec. UNS N08031. |
| ASTM B619 / B626 |
Welded Pipe & Tube |
Welded pipe and tube products |
| ASTM B625 / ASME SB-625 |
Plate, Sheet, Strip |
Primary flat-product spec. Pressure vessel plate. |
| ASTM B581 / ASME SB-581 |
Wire |
Ni-Cr-Fe-Mo wire for fasteners and mesh |
| ASTM B649 / ASME SB-649 |
Bar — Fe-Ni-Cr-Mo-Cu-N alloy |
Primary bar product spec. UNS N08031. |
| ASTM B564 / ASME SB-564 |
Nickel Alloy Forgings (Flanges, Fittings) |
Pressure vessel and piping service |
| ASTM B366 / ASME SB-366 |
Wrought Welded Fittings |
Butt-weld and socket-weld fittings |
| ASTM A240 / A480 |
Flat-Rolled Stainless & Heat-Resisting Plate |
General flat-product specifications |
| VdTÜV 509 |
German Pressure Vessel Approval |
Certified −196°C to 550°C pressure vessel service |
| NACE MR0175 / ISO 15156 |
Sour Oil & Gas Service — Level VI |
Acidic gas (H₂S) service certification |
| ASME Section VIII |
Pressure Vessel Construction |
Code case to 800°F (427°C) |
| DIN 1.4562 / NS1404 |
X1NiCrMoCu32-28-7 — European / Chinese Werkstoff |
European (1.4562) and Chinese (NS1404) equivalents |
Available Product Forms from HT PIPE
We supply Alloy 31 in solution-annealed + water-quenched condition with EN 10204 3.1 certification on every shipment. ASTM G28 Method A intergranular corrosion testing per heat is standard for severe-service applications. Welding filler metal FM 59 (2.4607 / UNS N06059, ERNiCrMo-13) is available for fabrications. Contact us for project quotations and current stock.
| Product Form |
Specification & Range |
| Seamless Pipes & Tubes |
½″–12″ NB, Sch 10S–Sch 80S. ASTM B622 UNS N08031. Solution annealed + WQ. |
| Plates & Sheets |
0.5–50 mm thickness. ASTM B625 UNS N08031. Solution annealed + WQ. Custom cut-to-size available. |
| Welded Pipes |
ASTM B619/B626 UNS N08031. Full range of sizes. As-welded or solution annealed per requirement. |
| Forged Fittings |
ASTM B366 UNS N08031. Butt-weld and socket-weld. Elbows, tees, reducers, caps, stub ends. |
| Flanges |
ASTM B564 UNS N08031. 150#–1500#. Weld neck, blind, slip-on, lap joint, long weld neck, orifice. |
| Round Bars |
6–300 mm diameter. ASTM B649 UNS N08031. Hot-finished and cold-drawn. Solution annealed. |
| Welding Consumables |
FM 59 (2.4607 / UNS N06059) — ERNiCrMo-13. Over-alloyed filler metal for Alloy 31 weldments. Wire and rod forms. |
HT PIPE Project Experience — Alloy 31
Case Study: Flue Gas Desulfurization (FGD) Absorber Tower — 8 Tons Alloy 31 Plate & Pipe Fittings
HT PIPE supplied 8 tons of Alloy 31 plate (ASTM B625, 6–25 mm) and seamless pipe fittings (ASTM B622, DN50–DN200) to a Southeast Asian coal-fired power plant for a seawater-cooled flue gas desulfurization system. The system handles:
SO₂-laden flue gas quenched and absorbed in seawater;
Chloride concentration ~20,000 ppm Cl− from the seawater scrubbing medium;
Acidic chloride environment at 60–80°C with intermittent excursions;
Crevices at mist eliminator supports and weld zones — pitting and crevice corrosion governing failure modes;
Material selection justification: 316L and 317L had failed within 2 years in a sister plant due to chloride pitting and crevice corrosion. 904L was rejected as inadequate for the high-concentration sulfuric acid zones in the absorber sump (corrosion rate >0.5 mm/yr predicted). C-276 was considered but rejected as cost-prohibitive for an 8-ton scope. Alloy 31 was selected as the optimal balance — PREN ≈ 52 and 6–7% Mo + nitrogen deliver the required pitting resistance, while the 1.0–1.4% copper addition improves sulfuric acid passivation in the sump region.
Delivery: Full EN 10204 3.1 certification with ASTM G28 Method A intergranular corrosion testing on all 6 heats (max 0.3 mm/yr achieved). Solution-annealed at 1150–1180°C + mandatory water quench per Step 1 procedure with furnace chart records. Pickled and passivated surface finish. Delivered in 12 weeks from order. Plant has operated 5+ years with zero corrosion incidents reported.
For additional project references matching your specific process chemistry — FGD, seawater cooling, phosphoric acid, HPAL, pulp and paper — contact our technical sales team. We can provide anonymized case studies and material selection recommendations for your corrosion environment.
Frequently Asked Questions — Alloy 31
Q1: What is the difference between Alloy 31 and Alloy 20?
Alloy 31 is a substantially higher-grade alloy than Alloy 20. It carries higher Cr (26–28% vs 19–21%), higher Mo (6–7% vs 2–3%), and adds nitrogen (0.15–0.25%). PREN rises from ~28 in Alloy 20 to ~52 in Alloy 31 — a dramatic increase in pitting resistance. Alloy 31 is clearly superior in high-concentration sulfuric acid, seawater, and severe chloride pitting environments. The trade-off is approximately 2× the cost of Alloy 20. Choose Alloy 20 for moderate sulfuric acid service where cost matters; upgrade to Alloy 31 when the environment involves high-concentration H₂SO₄, seawater, FGD, or severe pitting service.
Q2: Can Alloy 31 replace C-276?
In many applications, yes. Alloy 31 delivers close-to-C-276 corrosion resistance from an iron-base composition at approximately 60–70% of C-276 cost. PREN is 52 vs C-276’s 66. For high-concentration sulfuric acid, phosphoric acid, seawater, and chlorine dioxide service, Alloy 31 is the more economical choice. However, for pure hydrochloric acid, mixed reducing acids, and boiling reducing-acid environments, C-276 retains a clear performance advantage. We recommend laboratory immersion coupon testing in your specific process chemistry before specifying Alloy 31 as a C-276 replacement in borderline service.
Q3: What role does nitrogen play in Alloy 31?
Nitrogen (0.15–0.25%) is the defining alloying innovation in Alloy 31. It serves four critical functions: (1) boosts pitting resistance — in the PREN formula, nitrogen carries a coefficient of 16, far higher than Mo (3.3) or Cr (1.0); (2) stabilizes the austenitic structure, allowing the high Cr (26–28%) and Mo (6–7%) contents without forming harmful sigma or chi intermetallic phases; (3) increases solid-solution strength, raising yield strength above 316L and 904L; (4) improves weldability by stabilizing austenite against ferrite formation in the weld metal. Nitrogen is what enables Alloy 31 to approach nickel-alloy corrosion performance from an iron-base composition.
Q4: Is Alloy 31 suitable for cryogenic applications?
Yes. Alloy 31 is VdTÜV 509 certified for pressure vessel service from −196°C to 550°C. Charpy V-notch impact energy remains ≥140 J/cm² at −196°C — excellent cryogenic toughness. This qualifies the alloy for LNG, deep-cryogenic processing, arctic engineering, and other sub-zero applications. The nitrogen-stabilized austenitic structure does not undergo ductile-to-brittle transition at cryogenic temperatures, unlike ferritic or duplex stainless steels. For cryogenic pressure vessels, ensure post-weld solution anneal + pickling to restore full toughness in the heat-affected zone.
Q5: What are the welding considerations for Alloy 31?
Use the over-alloyed filler metal FM 59 (2.4607 / UNS N06059, ERNiCrMo-13) to ensure weld metal corrosion resistance matches or exceeds the base metal. Key welding parameters: (1) low heat input (0.5–1.5 kJ/mm) to limit grain growth and segregation; (2) interpass temperature ≤150°C to avoid precipitation; (3) thorough cleaning of weld preparations — remove all oxides, oils, and contamination; (4) post-weld acid pickling and passivation to restore the protective Cr₂O₃ film in the heat-affected zone. Because nitrogen is present, avoid prolonged dwell in the 600–1000°C range to prevent nitride and intermetallic precipitation. Most chemical process applications accept as-welded service; for severe corrosion service (FGD, seawater), full post-weld solution anneal + pickling is recommended.
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Plates, Seamless Pipes, Welded Pipes, Forged Fittings, Flanges, Round Bars — ASTM B622/B625/B649 Certified
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