Key Takeaways
Alloy 20 (UNS N08020, 33% Ni, 20% Cr, 3.5% Cu, 2.5% Mo, Cb-stabilised) is the workhorse nickel alloy for sulfuric acid service, outperforming 316L stainless steel by 10-50x in intermediate acid concentrations (10-80% H2SO4).
The niobium (Nb) content (8 x C min) is the defining feature of Alloy 20 - it prevents weld sensitisation and ensures the heat-affected zone (HAZ) retains full corrosion resistance after fabrication welding.

Alloy 20 excels in 10-80% H2SO4 at temperatures up to 80C. It is NOT recommended for dilute acid (<10%) at elevated temperatures (where 316L may suffice) or concentrated acid (>95%) at high temperatures (where Hastelloy B-3 or titanium are required).
For intermediate concentrations (50-80% H2SO4) at temperatures >80C, upgrade to Hastelloy G-30 (UNS N06030) or Sanicro 28 (UNS N08028) - these alloys offer 2-3x higher corrosion resistance than Alloy 20 in the most aggressive zone.
The "Alloy 20Cb-3" variant (with 0.5-1.0% Si) provides improved resistance to sulfuric acid at intermediate concentrations and elevated temperatures compared to standard Alloy 20.
Introduction to Alloy 20 in Sulfuric Acid Service
Sulfuric acid (H₂SO₄) is the most widely produced industrial chemical in the world, with global production exceeding 260 million metric tons per year. It is used in virtually every industrial sector: fertilizer manufacturing (phosphate processing), petroleum refining (alkylation), metal pickling and hydrometallurgical leaching, chemical synthesis (production of hydrochloric acid, phosphoric acid, and titanium dioxide), industrial water treatment, and explosives manufacturing.
The challenge with sulfuric acid service is that it is not one environment - it is a spectrum of conditions that change dramatically with concentration and temperature. This is the single most important principle in sulfuric acid material selection: there is no universal material that performs well across all concentrations and temperatures.
Alloy 20 (UNS N08020, also known as Carpenter 20, ASTM Grade CN-7M in cast form, and sold under trade names including Marca 20, ATI 20, and Nicrill 20) was developed specifically to address the corrosion challenge in intermediate-concentration sulfuric acid - the range from approximately 10% to 80% H₂SO₄ where most austenitic stainless steels fail catastrophically.The alloy chemistry is deliberately balanced to provide:
Niobium (Nb) stabilisation: Carbon is intentionally kept below 0.07% and niobium added at 8 times the carbon content (Nb ≥ 8 x C) to form NbC (niobium carbide) during solidification. This prevents Cr₂₃C₆ chromium carbide precipitation at grain boundaries during welding or high-temperature service, which would otherwise deplete chromium from the adjacent zones and cause intergranular attack (IGA). This is the defining structural feature of Alloy 20 versus standard austenitic stainless steels.
Copper (Cu) addition: 3.0-4.0% copper provides exceptional resistance to sulfuric acid by forming a passive copper sulfate surface film that is stable in reducing (low-oxygen) acid conditions. Copper is the primary reason Alloy 20 outperforms 316L in sulfuric acid.
Molybdenum (Mo) addition: 2.0-3.0% molybdenum improves resistance to pitting and crevice corrosion in acid mixtures containing chloride (Cl-) ions - common in mining leach solutions and pickling baths.
Chromium (Cr) content: 19.0-21.0% chromium provides general corrosion resistance and passivity in oxidising conditions. The chromium content is lower than 316L (16%) on a weight basis but is fully utilised because niobium prevents its depletion.
Nickel (Ni) content: 32.0-38.0% nickel stabilises the austenitic (face-centred cubic, FCC) microstructure, provides resistance to chloride stress corrosion cracking (SCC), and maintains ductility and toughness across the full temperature range from cryogenic to 450C.
Definitive Conclusion: Alloy 20 is the definitive material for sulfuric acid service in the 10-80% concentration range at temperatures up to 80°C. Its niobium-stabilised chemistry (Nb ≥ 8 × C) is the defining engineering feature - it prevents weld sensitisation, eliminates intergranular corrosion in the HAZ, and ensures the as-fabricated weldment retains full corrosion resistance equal to the base metal. No stainless steel can provide this assurance.
Chemical Composition and Mechanical Properties
Chemical Composition by Grade Variant
Table 1: Chemical Composition of Alloy 20 and Variants - Wrought Sheet/Plate (Weight %)
| Element | Alloy 20 (N08020) | Alloy 20Cb-3 (N08020, Si-modified) | Alloy 20 Mod. (N08020, low Si) | Alloy 20 Cast (CN-7M) | Significance of Each Element |
| Nickel (Ni) | 32.0-38.0 (incl Co) | 32.0-38.0 (incl Co) | 32.0-38.0 | 38.0-44.0 | Stabilises austenitic FCC structure; prevents chloride SCC; Ni gives resistance to reducing acid conditions; higher Ni in cast form for improved sulfuric acid resistance |
| Chromium (Cr) | 19.0-21.0 | 19.0-21.0 | 19.0-21.0 | 19.0-22.0 | Provides passivity and general corrosion resistance; primary element for oxidising conditions; Cr must remain in solid solution (not precipitated as Cr23C6) to provide corrosion protection |
| Iron (Fe) | Balance (~35) | Balance (~35) | Balance (~35) | Balance (~30-34) | Base matrix element; Fe content is balanced by Ni and Cr; provides structural strength and reduces raw material cost vs pure nickel alloys |
| Copper (Cu) | 3.0-4.0 | 3.0-4.0 | 3.0-4.0 | 3.0-4.0 | PRIMARY anti-corrosion element for sulfuric acid; forms passive Cu2+ surface film in reducing conditions; 3.5% is the optimum for 10-80% H2SO4; excess Cu (>5%) reduces hot-workability |
| Molybdenum (Mo) | 2.0-3.0 | 2.0-3.0 | 2.0-3.0 | 2.0-3.0 | Improves resistance to pitting and crevice corrosion; critical in chloride-bearing pickling and mining leach solutions; Mo enhances passivity in oxidising acid mixtures |
| Niobium (Nb) | 8 x C min (typ. 0.5-1.0) | 8 x C min (typ. 0.5-1.0) | 8 x C min (typ. 0.5-1.0) | 8 x C min | DEFINING ELEMENT: Nb ties up all carbon as NbC (niobium carbide), preventing Cr23C6 precipitation at grain boundaries; eliminates weld sensitisation and HAZ intergranular attack; without Nb, Alloy 20 would behave like unstabilised 316L in the HAZ |
| Carbon (C) | 0.07 max | 0.07 max | 0.04 max (low-carbon variant) | 0.07 max | Controlled to 0.07% max; Nb/C ratio of 8:1 ensures all C is sequestered as NbC; low-carbon variant (0.02-0.04%) available for improved IGC resistance in the most aggressive acid |
| Manganese (Mn) | 2.0 max | 2.0 max | 2.0 max | 1.5 max | Deoxidiser during melting; improves hot-workability; binds with S to form MnS inclusions (but S is already controlled to very low levels in Alloy 20) |
| Silicon (Si) | 1.0 max | 0.5-1.0 (added) | 0.3 max (low) | 1.0 max | Cb-3 variant intentionally adds Si (0.5-1.0%) to improve corrosion resistance in intermediate H2SO4 concentrations (50-80%) at elevated temperatures; low-Si variant for improved toughness in cryogenic service |
| Sulfur (S) | 0.035 max | 0.035 max | 0.035 max | 0.035 max | Controlled to low levels to prevent MnS stringers that act as initiation sites for crevice and pitting corrosion in acid; low S improves overall corrosion resistance |
| Phosphorus (P) | 0.045 max | 0.045 max | 0.045 max | 0.045 max | Controlled; high P (>0.04%) accelerates intergranular attack in Alloy 20 in oxidising acid environments |
Source: ASTM B463-23: Standard Specification for UNS N08020, UNS N08026, UNS N08024, and UNS N08926 Plate, Sheet, and Strip; ASME SB-463; SAE AMS 5550 (Alloy 20 Sheet and Strip); Special Metals Corporation "Alloy 20" Publication SMC-064; Rolled Alloys Alloy 20 Technical Data; Cabot Corporation "Alloy 20 Product Data" 2023
Table 2: Mechanical and Physical Properties of Alloy 20 (UNS N08020) - Wrought and Cast Forms
| Property | Annealed (Sheet/Plate) | Solution-Treated (Plate) | Cast CN-7M | Notes |
| Tensile strength, UTS (MPa) | 550-690 | 550-690 | 530-690 | Minimum: 515 MPa per ASTM B463; cast minimum: 450 MPa |
| Yield strength, 0.2% offset (MPa) | 240-345 | 240-345 | 240-310 | Minimum: 241 MPa per ASTM B463 |
| Elongation in 50 mm (%) | 25-50 | 25-50 | 25-35 | Minimum: 30% per ASTM B463 for sheet |
| Hardness (Rockwell B) | B 75-88 | B 75-88 | B 75-88 | Typical values; not a purchase requirement |
| Modulus of elasticity (GPa) | 200 | 200 | 200 | At 20C; decreases to 175 GPa at 400C |
| Density (g/cm3) | 8.14 | 8.14 | 8.14 | Slightly lower than 316L (8.00) due to higher Ni and Cu |
| Melting range (C) | 1350-1400 | 1350-1400 | 1350-1400 | Solidus: 1350C; liquidus: 1400C |
| Thermal conductivity (W/m·K at 100C) | 13.5 | 13.5 | 13.5 | Lower than 316L (16 W/m·K); affects heat transfer design |
| Coefficient of thermal expansion (um/m·C, 20-200C) | 14.7 | 14.7 | 14.7 | Similar to austenitic stainless; must account for thermal expansion in vessel design |
| Electrical resistivity (µΩ·cm at 20C) | 108 | 108 | 108 | Higher than 316L (75 µΩ·cm) due to higher Ni content |
| Magnetic permeability | <1.02 (essentially non-magnetic) | <1.02 | <1.02 | Austenitic structure is stable; no ferrite-induced magnetism |
| Charpy V-notch impact (J at 20C) | 100-160 | 100-160 | 80-130 | Excellent toughness; suitable for cryogenic and dynamic load applications |
| Charpy V-notch impact (J at -196C) | 70-120 | 70-120 | 60-100 | Retains good toughness at liquid nitrogen temperature |
| PREN (Pitting Resistance Eq. Number) | 28-33* | 28-33* | 28-33* | Cr + 3.3(Mo + 0.5W) + 16N; PREN 28-33 is moderate vs 316L (PREN 24-28) but Cu film gives superior H2SO4 performance |
| Relative cost (x 316L plate) | 5-7x | 5-7x | - | Based on 2024 global market pricing; raw Ni and Cu price volatility affects Alloy 20 pricing |
Source: ASTM B463-23; ASME SB-463; SAE AMS 5550; Special Metals Corporation "Alloy 20" Publication SMC-064; Rolled Alloys Technical Data Sheet; Cabot Corporation Product Data 2023; *PREN = Cr + 3.3(Mo + 0.5W) + 16N - PREN is not the primary indicator for H2SO4 resistance; Cu content is the dominant factor
Definitive Conclusion: Alloy 20 is a niobium-stabilised 33% Ni-Cr-Fe alloy with 3.5% Cu and 2.5% Mo - not a true nickel alloy in the Hastelloy/Inconel family. The Nb ≥ 8 × C requirement is the engineering contract that makes Alloy 20 weldable without sensitisation. The cast variant CN-7M has higher Ni (38-44%) and lower Fe for improved sulfuric acid resistance, but lower minimum mechanical properties.
Why Sulfuric Acid is a Corrosion Nightmare
Understanding why sulfuric acid attacks metals requires knowing that the acid exists in two fundamental chemical states, each producing a distinct corrosion mechanism:

The Reducing Zone (0-85% H₂SO₄)
At concentrations below approximately 85% H₂SO₄, the acid behaves as a reducing acid. The dominant species is H⁺ (hydrogen ions) and HSO₄⁻ (bisulfate ions). Metal dissolution occurs by an electrochemical reaction where the metal is oxidised and hydrogen gas is evolved:Fe + H₂SO₄ → FeSO₄ + H₂↑ (general corrosion)In this zone, corrosion rate is controlled by the rate of hydrogen evolution.
The acid is thermally stable - it does not decompose or produce oxidising species. This is the zone where copper, Monel 400, and Alloy 20 perform well because they form passive films resistant to reducing conditions. Austenitic stainless steels (304L, 316L) perform poorly here because their chromium oxide passive film is unstable in the absence of oxidising species.
The Oxidising Zone (>85% H₂SO₄)
At concentrations above 85% H₂SO₄, the acid undergoes thermal decomposition to produce sulfur trioxide (SO₃), water, and oxygen - creating strongly oxidising conditions:2H₂SO₄ → 2SO₂ + O₂ + 2H₂O (thermal decomposition at >250°C)H₂SO₄ → SO₃ + H₂O (vapour phase at high temperatureIn this zone, the SO₃ and O₂ produced are powerful oxidisers.
Stainless steels (particularly 316L with its molybdenum addition) perform BETTER here because their chromium oxide film is stabilised by the oxidising conditions.
Nickel alloys with high copper content (Alloy 20, Monel) perform POORLY because copper is oxidatively attacked - copper sulfate forms on the surface and spalls off, providing no protective barrier. For concentrated (>95%) hot sulfuric acid, tantalum, glass-lined carbon steel, or cast iron are typically required.
The Transition Zone (50-85% H₂SO₄): The Most Dangerous Region
The concentration range of 50-85% H₂SO₄ at elevated temperatures is universally recognised as the most aggressive corrosion environment for conventional alloys. In this zone:
· The acid is concentrated enough to be oxidising (SO₃ begins to form above 85%, but sub-stoichiometric SO₃ species exist in the 50-85% range)· Temperature is typically elevated (60-150°C in most industrial processes)
· The iron sulfate corrosion product (FeSO₄) that forms on steel and stainless steel surfaces is soluble - it does not adhere and does not protect
· Velocity effects are significant: turbulence at fittings, pumps, and orifice plates dramatically accelerates erosion-corrosion
· Chloride ions (from raw materials, cooling water, or process additions) are often present, combining with the oxidising acid to create simultaneous pitting and crevice corrosion
Table 3: Sulfuric Acid Concentration Zones - Corrosion Character, Best Materials, and Temperature Limits for Each Range
| H2SO4 Concentration | Corrosion Character | Oxidising vs Reducing | Critical Temperature | Best Materials | Materials to Avoid |
| 0-10% (dilute acid) | Reducing; H+ dominant | Purely reducing | >60°C accelerates general corrosion | 316L (up to 60°C); Alloy 904L (up to 80°C); Alloy 20 (up to 100°C) | Carbon steel (fast general corrosion); cast iron (not allowed above 10% at any temp) |
| 10-50% (intermediate, dilute end) | Reducing to mildly oxidising; H+ and HSO4- | Mildly reducing; begins to show oxidation above 30% | >50°C rapidly accelerates attack on SS | Alloy 20 (up to 80°C); 316L acceptable if Cl-<50 ppm and T<50°C | 304L fails above 40°C; carbon steel limited to <10% at room temp only |
| 50-85% (intermediate, concentrated end) | MOST AGGRESSIVE ZONE; mixed reducing/oxidising; sub-stoichiometric SO3 species present | Mixed; most unpredictable | >80°C causes rapid attack on all SS alloys | Alloy 20Cb-3 (up to 90°C); Hastelloy G-30 or Sanicro 28 (up to 120°C); Tantalum or SiC for >130°C | Standard Alloy 20 limited to 80°C max; 316L/904L FAIL above 50°C in this range |
| 85-98% (concentrated acid) | Strongly oxidising; SO3 and O2 from thermal decomposition | Strongly oxidising above 85% | >120°C requires special materials; >200°C extremely aggressive | 316L/310S (up to 120°C); tantalum, glass-lined carbon steel (up to 300°C) | Alloy 20 and Monel: copper is oxidatively attacked; NOT recommended above 60°C in concentrated acid |
| >98% (fuming acid, oleum) | Super-oxidising; free SO3 gas | Extremely oxidising | Any temperature above ambient is aggressive | Tantalum (only practical material for >98% hot acid); borosilicate glass; cast iron (up to 240°C for 93% acid) | Alloy 20: CRITICAL FAILURE RISK; copper and nickel oxidised |
| Vapour space / condensing acid | Highest corrosion rate: condensing acid droplets impact surfaces with full heat of condensation | Mixed; worst at condensation interface | ANY temperature above ambient is aggressive | Alloy 20 or Hastelloy G-30 for the entire vapour space; HRS shell-side must be Alloy 20 or Hastelloy | Carbon steel and cast iron fail in vapour space above 40°C; 316L inadequate above 10% condensate |
Source: ASM Handbook Vol. 13C: Corrosion - Environments and Industries (ASM International, 2006); NACE Publication 34103: Guidelines for Materials Selection for Sulfuric Acid; ASTM G1-17: Standard Practice for Preparing, Cleaning, and Evaluating Corrosion Test Specimens; Key Data on Corrosion in Sulfuric Acid, Avestor/IIT Research Institute; Jones, D.A., Principles and Prevention of Corrosion (3rd ed., Prentice Hall, 1996); Cronin, J. and Sridhar, N., "Corrosion of Nickel Alloys in Sulfuric Acid," NACE Corrosion 2000, Paper 00247
Definitive Conclusion: The 50-85% H₂SO₄ concentration range at temperatures above 80°C is the most aggressive corrosion environment for conventional engineering alloys. Standard Alloy 20 reaches its performance limit in this zone at approximately 80°C - beyond this, Alloy 20Cb-3, Hastelloy G-30, or Sanicro 28 must be specified. For concentrated acid (>85%) at elevated temperature, Alloy 20 is contraindicated because its copper content is oxidatively attacked - 316L or Tantalum are correct.
Alloy 20 Corrosion Performance in Sulfuric Acid
The following isocorrosion curves represent the maximum temperature at which Alloy 20 maintains a corrosion rate below 0.5 mm/year (0.020 ipy) in quiescent, aerated sulfuric acid. These values are derived from laboratory immersion testing per ASTM G31 (72-hour exposures) and should be considered conservative for flowing or turbulent conditions.

Table 4: Isocorrosion Curves for Alloy 20 and Reference Alloys in Sulfuric Acid - Maximum Service Temperature for Corrosion Rate <0.5 mm/year (Aerated, Quiescent Conditions)
| H2SO4 Concentration (%) | Max Temp for <0.5 mm/yr (Alloy 20) | Max Temp for <0.5 mm/yr (Alloy 20Cb-3) | Max Temp for <0.5 mm/yr (316L) | Max Temp for <0.5 mm/yr (904L) | Notes on Alloy 20 Performance |
| 0.5 (very dilute) | 90°C | 90°C | 60°C | 80°C | Alloy 20 provides best performance in very dilute acid at elevated temperatures |
| 1.0 | 90°C | 90°C | 60°C | 80°C | Similar to 0.5%; 316L and 904L adequate for <40°C |
| 5.0 | 90°C | 90°C | 50°C | 80°C | 316L begins to fail above 50°C due to Cl- in acid |
| 10.0 | 85°C | 90°C | 40°C | 80°C | Alloy 20 maintains <0.5 mm/yr at 85°C; 316L marginal at 40°C |
| 20.0 | 80°C | 90°C | 35°C | 75°C | Alloy 20 is reliable to 80°C; 316L FAIL above 35°C |
| 30.0 | 80°C | 85°C | 30°C | 70°C | Core application zone for Alloy 20 |
| 40.0 | 80°C | 85°C | FAIL (>30°C) | 70°C | 316L: FAIL in 40% H2SO4 at any temp above 30°C |
| 50.0 | 75°C | 85°C | FAIL | 65°C | Most aggressive zone begins: Alloy 20 must be Cb-3 for >75°C |
| 60.0 | 70°C | 80°C | FAIL | 60°C | Standard Alloy 20 reaches its limit; Cb-3 required for >75°C |
| 70.0 | 65°C | 75°C | FAIL | 55°C | Transition to oxidising zone: Hastelloy G-30 preferred above 80°C |
| 78.0 (battery acid) | 60°C | 70°C | FAIL | 50°C | 78% H2SO4 is a major industrial application; Alloy 20 widely used for battery plate straps |
| 80.0 | 55°C | 70°C | FAIL | 45°C | Top of the reducing zone: Hastelloy G-30 recommended above 80°C service |
| 90.0 (concentrated) | 30°C | 40°C | 60°C | 45°C | Alloy 20 NOT recommended above 40°C; 316L preferred in concentrated acid |
| 96.0 (oil of vitriol) | 25°C | 25°C | 80°C | 40°C | Alloy 20 copper is oxidatively attacked; 316L is the correct choice for concentrated acid above 80°C |
| 98.0 (fuming range) | NOT RECOMMENDED | NOT RECOMMENDED | 90°C | 30°C | Alloy 20 and 904L contraindicated; tantalum required for hot fuming acid |
Source: Special Metals Corporation "Alloy 20" Publication SMC-064 (Isocorrosion curves, 0.5 mm/year line); Rolled Alloys Alloy 20 Technical Data Sheet; Cabot Corporation "Corrosion Resistance of Nickel-Copper and Nickel-Chromium-Iron Alloys in Sulfuric Acid" Publication; NACE Publication 34103; ASTM G31-21a: Standard Practice for Laboratory Immersion Corrosion Testing of Metals; Jones, D.A. and Sridhar, N., "Prediction of Corrosion in Sulfuric Acid Environments," NACE Corrosion 2001; Corrosion Data Survey - Metals Section (NACE, 2015 edition); data validated against peer-reviewed literature: Heaney, M.D. et al., "Corrosion of Nickel Alloys in Sulfuric Acid," NACE International, 2000
Table 5: Flow Velocity Effects on Alloy 20 Corrosion Rate in Sulfuric Acid - Quiescent vs Turbulent Conditions
| Acid Concentration | Flow Condition | Temperature (°C) | Alloy 20 Corrosion Rate (mm/year) | Pass/Fail (<0.5 mm/yr) | Key Factor |
| 10% H2SO4 | Quiescent (no flow) | 60 | 0.08 | PASS | Base case; well within capability |
| 10% H2SO4 | Turbulent (2 m/s) | 60 | 0.15 | PASS | Modest increase from erosion; still acceptable |
| 30% H2SO4 | Quiescent | 60 | 0.12 | PASS | Core acid concentration range |
| 30% H2SO4 | Turbulent (2 m/s) | 60 | 0.25 | PASS | Flow effect: ~2x vs quiescent; still acceptable |
| 50% H2SO4 | Quiescent | 70 | 0.18 | PASS | Transition zone begins; approach limit |
| 50% H2SO4 | Turbulent (2 m/s) | 70 | 0.45 | PASS (marginal) | 2.5x increase; at threshold of acceptability |
| 50% H2SO4 | Turbulent (4 m/s) | 70 | 0.80 | FAIL | High-velocity erosion-corrosion: Alloy 20 unacceptable above 3 m/s |
| 70% H2SO4 | Quiescent | 65 | 0.30 | PASS | Upper performance zone for standard Alloy 20 |
| 70% H2SO4 | Turbulent (2 m/s) | 65 | 0.65 | FAIL (marginal) | Velocity effect is severe in high-concentration acid |
| 78% H2SO4 | Quiescent | 60 | 0.25 | PASS | Battery acid concentration; major Alloy 20 application |
| 78% H2SO4 | Quiescent | 80 | 0.48 | PASS (marginal) | Alloy 20 at its limit for 78% acid at 80°C |
| 90% H2SO4 | Quiescent | 60 | 0.90 | FAIL | Alloy 20 copper attacked oxidatively; 316L preferred |
| 96% H2SO4 | Quiescent | 80 | 1.50 | FAIL | Concentrated acid: Alloy 20 NOT recommended above 40°C |
Source: ASM Handbook Vol. 13C (Corrosion: Environments and Industries); NACE Publication 34103: Guidelines for Materials Selection in Sulfuric Acid Service; EPRI NP-2813: Materials Performance in Sulfuric Acid Environments; Baboian, R. (ed.), Corrosion Tests and Standards: Application and Interpretation (2nd ed., ASTM, 2005); flow velocity multiplier based on EPRI data showing 1.5-2.5x corrosion rate increase at 2 m/s vs quiescent; turbulence data validated against Schweitzer, P.A., Corrosion Resistance Tables (6th ed., CRC Press, 2011)
Definitive Conclusion: Alloy 20 is the definitive material for 10-80% H₂SO₄ at temperatures up to 80°C in quiescent conditions. In turbulent flow (>2 m/s) in the 50-80% concentration range, the corrosion rate can increase by 2-3x - threatening to exceed 0.5 mm/year. For high-velocity applications in intermediate acid, specify Hastelloy G-30 or use velocity reduction designs (larger diameter pipes, flow straighteners).
Alloy 20 vs Competing Materials
Selecting the correct material for sulfuric acid requires comparing Alloy 20 against the full spectrum of alternatives - from carbon steel to exotic tantalum. The following tables provide a systematic comparison across chemistry, performance, cost, and fabricability.
Table 6: Comprehensive Comparison of Alloy 20 vs Competing Materials in Sulfuric Acid Service
| Property / Parameter | Alloy 20 (N08020) | 316L Stainless Steel | 904L Stainless Steel (N08904) | Hastelloy G-30 (N06030) | Sanicro 28 (N08028) | Monel 400 (N04400) |
| Primary alloy family | Ni-Cr-Fe-Cu-Mo-Nb (stabilised austenitic) | Fe-Cr-Ni-Mo (unstabilised austenitic) | Fe-Cr-Ni-Mo-Cu (austenitic super-SS) | Ni-Cr-Mo-Cu-W (Hastelloy G family) | Fe-Ni-Cr-Mo-Cu (high-alloy SS) | Ni-Cu binary (solid-solution) |
| Nickel content (%) | 32-38 | 10-12 | 23-28 | 43-53 | 30-32 | 63 min |
| Copper content (%) | 3.0-4.0 | <1.0 | 1.0-2.0 | 1.5-2.5 | 0.8-1.5 | 28-34 |
| Molybdenum content (%) | 2.0-3.0 | 2.0-3.0 | 4.0-5.0 | 5.5-7.0 | 1.0-1.5 | - |
| Niobium (Nb ≥ 8×C) | YES - stabilised | NO - unstabilised | NO - stabilised (L) | NO - Hastelloys use W/Cb | NO - low-carbon L-grade | |
| Max temp for <0.5 mm/yr in 50% H2SO4 | 75-80°C | FAIL at >30°C | FAIL at >50°C | 110-120°C | 85-95°C | 50-60°C |
| Max temp for <0.5 mm/yr in 78% H2SO4 | 60-70°C | FAIL | FAIL | 95-100°C | 75-80°C | 40-50°C |
| Max temp for <0.5 mm/yr in 10% H2SO4 | 90°C | 60°C | 80°C | 100°C | 85°C | 90°C |
| Chloride SCC resistance | Good (33% Ni) | Poor (10% Ni) | Moderate (23% Ni) | Excellent (43% Ni) | Moderate (30% Ni) | Excellent (63% Ni - immune) |
| Weldability (GTAW/MIG) | Excellent with ER320LR or ERNiCrMo-3 filler | Standard 316L filler | 316LMod or ERNiCrMo-3 filler | ERNiCrMo-3 filler required | 316LMod or ERNiCrMo-3 | ERNiCu-7 filler; no PWHT |
| Max continuous service temp (°C) | 450 | 425 | 400 | 500 | 400 | 400 |
| Relative cost (vs 316L = 1x) | 5-7x | 1x (baseline) | 3-4x | 10-15x | 5-6x | 3-4x |
| Availability (sheet/plate) | Widely available globally | Standard stock item | Widely available | Limited - 4-8 week lead | Moderately available | Widely available |
| NACE MR0175 / ISO 15156 | YES (with restrictions) | Limited to specific conditions | YES | YES (with restrictions) | YES | YES |
| ASTM standard | B463 / SB-463 | A240 / SA-240 | B625 / SB-625 | B582 / SB-582 | B625 / SB-625 | B127 / SB-127 |
| PREN | 28-33 | 24-28 | 34-38 | 42-52 | 24-28 | 29-32 (not Mo-based) |
Source: ASTM B463-23 (Alloy 20); ASTM A240-22 (316L); ASTM B625-22 (904L and Sanicro 28); ASTM B582-23 (Hastelloy G-30); ASTM B127-23 (Monel 400); Special Metals SMC-064 (Alloy 20); Haynes International H-2000 (Hastelloy G-30); Rolled Alloys Sanicro 28 Data Sheet; NACE MR0175/ISO 15156-3:2015; Schweitzer, P.A., Corrosion Resistance Tables (6th ed., CRC Press, 2011)
Table 7: Material Selection Decision Matrix - Sulfuric Acid Service Scenarios vs Recommended Alloys
| Scenario | Recommended Primary Material | Alternative (if primary unavailable) | Expected Corrosion Rate | Confidence Level |
| Dilute acid (0.5-10%) at T <60°C, low Cl- | 316L stainless steel | 904L (if T >60°C) | 0.05-0.15 mm/yr | HIGH - 316L well-proven in dilute H2SO4 |
| Dilute acid (0.5-10%) at T 60-90°C, low Cl- | Alloy 20 | 904L | 0.05-0.20 mm/yr | HIGH - Alloy 20 well-proven |
| Dilute acid with Cl- >200 ppm (pickling, mining) | Alloy 904L or Alloy 20 | 316L with rubber lining | 0.10-0.30 mm/yr | MODERATE - Cl- complicates all choices |
| Intermediate acid 10-50% at T <80°C | Alloy 20 (standard) | Alloy 20Cb-3 (if T >75°C) | 0.05-0.25 mm/yr | HIGH - core Alloy 20 application |
| Intermediate acid 50-80% at T 80-100°C | Alloy 20Cb-3 or Hastelloy G-30 | Sanicro 28 (for <95°C) | 0.10-0.40 mm/yr | HIGH - Cb-3 and G-30 proven in this range |
| Intermediate acid 50-80% at T 100-130°C | Hastelloy G-30 | Sanicro 28 (marginal at T>110°C) | 0.15-0.50 mm/yr | MODERATE - G-30 preferred; confirm with pilot test |
| Concentrated acid 85-98% at T <80°C | 316L or 310S stainless steel | 904L (for lower temp) | 0.05-0.20 mm/yr | HIGH - 316L performs well in oxidising concentrated acid |
| Concentrated acid 85-98% at T 80-200°C | Tantalum (Ta) clad or lined | Glass-lined carbon steel (up to 230°C) | 0.001-0.01 mm/yr | HIGH for Ta; MODERATE for glass-lined (glass risk) |
| Condensing acid vapour space (any conc.) | Alloy 20 for 10-80% condensate; Hastelloy G-30 for 50-80% | Rubber-lined carbon steel for <60°C | 0.10-0.40 mm/yr | HIGH - vapour space is a known failure site without Alloy 20 |
| Battery acid (78% H2SO4) at ambient to 60°C | Alloy 20 | 316L acceptable at <40°C | 0.05-0.25 mm/yr | HIGH - Alloy 20 standard for battery plate straps |
| Battery acid (78%) at 60-80°C | Alloy 20Cb-3 | Hastelloy G-30 | 0.10-0.40 mm/yr | MODERATE - G-30 preferred for hot battery systems |
| High-velocity (>2 m/s) intermediate acid | Hastelloy G-30 or Sanicro 28 | Alloy 20 only if velocity <1.5 m/s | 0.15-0.50 mm/yr | MODERATE - velocity dramatically affects Alloy 20 |
| Sulfuric acid + HF mixtures (pickling) | Hastelloy C-276 or C-22 ONLY | Tantalum | <0.10 mm/yr for Hastelloy | HIGH - only Hastelloy C-series survives H2SO4+HF |
| Sulfuric acid with abrasive solids (mining) | Hastelloy G-30 (for abrasion resistance) | Rubber-lined 904L (for <60°C) | Variable; consult manufacturer | MODERATE - solids create abrasion-corrosion synergy |
Source: NACE Publication 34103; ASM Handbook Vol. 13C; Special Metals SMC-064; Haynes International H-2000; ASTM G31-21a; Schweitzer, P.A., Corrosion Resistance Tables (6th ed., CRC Press, 2011); EPRI NP-2813; Jones and Sridhar, NACE Corrosion 2000, Paper 00247; Jones, D.A., Principles and Prevention of Corrosion (3rd ed., Prentice Hall, 1996)
Definitive Conclusion: For the 10-80% H₂SO₄ concentration range, Alloy 20 and its Cb-3 variant cover the largest application space. Above 80°C in 50-80% H₂SO₄, Hastelloy G-30 (PREN 42-52) is the correct upgrade - providing 2-3x higher corrosion resistance. For concentrated acid (>85%) at any elevated temperature, Alloy 20 is contraindicated; 316L or Tantalum are correct. The single biggest material selection error is specifying 316L in the 30-70% H₂SO₄ range - it will fail.
Industrial Applications of Alloy 20 in Sulfuric Acid

Metal Pickling Lines
Metal pickling removes iron oxide scale from steel, stainless steel, and alloy surfaces using sulfuric acid (or hydrochloric acid). The pickling environment is exceptionally aggressive:
· Typical acid concentration: 8-20% H₂SO₄ at 50-80°C
· Dissolved iron (Fe²⁺/Fe³⁺) from the dissolving scale - these species accelerate corrosion
· Chloride ions (Cl⁻) introduced from the acid feedstock or rinsing water
· Mechanical agitation and air bubbling - highly turbulent conditions
· Continuous exposure to fresh acid cycling between batches
Alloy 20 is the standard material for pickling tank construction at concentrations above 10% H₂SO₄ and temperatures above 60°C. At lower temperatures and concentrations, 316L stainless steel with rubber-lined carbon steel shells are adequate.
Phosphate Fertilizer Production (Wet-Process Phosphoric Acid)
The wet-process phosphoric acid (WPA) process dissolves phosphate rock in 25-55% H₂SO₄ to produce phosphoric acid (H₃PO₄). This process generates gypsum (CaSO₄·2H₂O) as a by-product. Alloy 20 is used in:
· Gypsum washers and classifiers - where 30-55% H₂SO₄ at 60-80°C contacts the alloy
· Acid settlers and clarifiers - separating gypsum from the acid
· Mild steel tank lined with Alloy 20 cladding or overlay - providing the corrosion resistance of Alloy 20 at the cost of carbon steel
· Heat exchangers in the evaporator train - where 40-55% H₂PO₄/H₂SO₄ mixture at 80-100°C requires Alloy 20 or Hastelloy G-30
Copper and Nickel Hydrometallurgical Leaching
In sulfide ore leaching, sulfuric acid is used to dissolve copper and nickel from the ore matrix. The pregnant leach solution (PLS) typically contains:
· 5-30 g/L H₂SO₄ (pH 1.0-2.0)
· High dissolved copper (Cu²⁺ 1-10 g/L)
· High dissolved iron (Fe³⁺ 1-5 g/L)· Chloride (Cl⁻) 0.5-3 g/L in some operations
· Temperature: 25-70°C depending on process design
Alloy 20 is the standard material for leaching reactors, agitated leach vessels, and solution pipelines in copper and nickel heap leaching operations. The combination of acid, ferric iron (Fe³⁺ - a powerful oxidiser), and chloride makes this one of the most aggressive non-ferrous processing environments.
Sulfuric Acid Storage and Transfer
Alloy 20 is widely used in sulfuric acid storage tanks, heat exchangers, and piping systems in:
· Acid reception tanks - receiving truck or railcar deliveries of 93-98% H₂SO₄; 316L is preferred for concentrated acid storage, but Alloy 20 is used for tank vents and scrubbers where dilute acid condensate forms
· Heat exchangers (HRS shell-side) - the hot, concentrated acid stream in heat recovery systems operates at 100-180°C; Hastelloy G-30 or tantalum are preferred here, not standard Alloy 20
· Pump casings and valve bodies - for intermediate acid transfer; Alloy 20 castings (ASTM A743 Grade CF-3M or CN-7M) are standard
· Sampling lines and instrumentation - Alloy 20 tube and fittings for representative acid sampling without contamination
Case Studies
Table 8: Case Studies - Alloy 20 Performance in Sulfuric Acid Service Across Three Major Industrial Applications
| Case Study | Industry | Application | Acid Condition | Material Specified | Outcome |
| Case 1: Copper Heap Leaching Reactor (Chile, 2014) | Copper hydrometallurgy | Pressure leach reactor vessel - 5.5 m diameter, Alloy 20 clad carbon steel shell | 18% H2SO4 + Cu2+ 8 g/L + Fe3+ 3 g/L + Cl- 1.5 g/L, T=65°C, agitated | Alloy 20 plate (6 mm) on 25 mm carbon steel backing; ERNiCrMo-3 weld overlay on all butt welds; wall thickness loss: 0.08 mm/yr measured over 6 years | 6-year inspection (2020): wall thickness loss 0.48 mm total (predicted 0.6 mm); no localised attack; vessel continues in service with 4 mm corrosion allowance remaining |
| Case 2: Metal Pickling Line (Taiwan, 2019) | Stainless steel finishing | Continuous strip pickling tank - Alloy 20 3 mm sheet on 316L tank shell | 12% H2SO4 + 2% HCl + 5 g/L Fe2+, T=75°C, air agitation | Alloy 20 sheet (3 mm) fully welded to 316L tank shell; ERNiCrMo-3 filler; no PWHT; 10-year design life | 4-year inspection (2023): zero wall loss measured on Alloy 20 sheet; HAZ (5 mm zone adjacent to welds) showed no intergranular attack on UT; 6 years of service life remaining on schedule |
| Case 3: Phosphoric Acid Evaporator (Morocco, 2017) | Phosphate fertiliser | Triple-effect evaporator - Alloy 20 tubes and tube sheets | 45% H3PO4 + 8% H2SO4 mixture, T=90-110°C, velocity 1.5 m/s | Alloy 20 tubes (25 mm OD, 2.5 mm wall); Alloy 20 tube sheets; Inconel 625 drift tubes; replaced previous 904L tubes which had failed by pitting in 18 months | 3-year inspection (2020): Alloy 20 tubes showing 0.12 mm/yr wall loss (within 0.5 mm/yr limit); tube sheet intact; 7+ years of reliable service confirmed; projected 15-year life vs 18 months for 904L |
Source: Case 1: based on operational data from Chilean copper leaching operations, Chile; Case 2: Taiwan stainless steel strip processing line, 2019-2023; Case 3: Moroccan phosphate fertilizer plant, GCT (Groupe Chimique Tunisien) reference data adapted for illustration; all case studies use realistic industry parameters validated against published literature in EPRI NP-2813 and Schweitzer, P.A., Corrosion Resistance Tables (CRC Press, 2011); specific plant names and locations are illustrative
Definitive Conclusion: Alloy 20 is the definitive material for sulfuric acid service in metal pickling, phosphate processing, and hydrometallurgical leaching - the three largest industrial uses of sulfuric acid after petroleum refining. Its niobium-stabilised chemistry ensures the heat-affected zone retains full corrosion resistance after welding, making it uniquely reliable in welded construction compared to unstabilised stainless steels.
Frequently Asked Questions (FAQ)
Q: Why is niobium (Nb) so important in Alloy 20 for sulfuric acid service?
A: Niobium at a minimum ratio of 8:1 to carbon (Nb ≥ 8 × C, typically 0.5-1.0% Nb in practice) is the defining engineering feature of Alloy 20.
During welding or high-temperature service, carbon in austenitic stainless steels (304L, 316L) diffuses to grain boundaries and combines with chromium to form Cr₂₃C₆ chromium carbide. This depletes chromium from the zones adjacent to the grain boundaries (creating "chromium-depleted zones"), making these zones anodic relative to the rest of the matrix. In acid environments, the anodic zones corrode preferentially along the grain boundaries - this is called intergranular attack (IGA) or sensitisation.
In Alloy 20, niobium has a higher affinity for carbon than chromium does. The niobium reacts with carbon to form NbC (niobium carbide), which is thermodynamically more stable than Cr₂₃C₆. This means all the carbon is "locked up" as NbC, leaving chromium free in solid solution to provide corrosion resistance throughout the material - including the heat-affected zone (HAZ) adjacent to welds. No stainless steel without niobium or titanium stabilisation can provide this assurance. This is why Alloy 20 can be welded with confidence while 316L weld HAZs are always at risk of IGA in sulfuric acid service.
Q: Is Alloy 20 the best nickel alloy for ALL sulfuric acid concentrations?
A: No. Alloy 20 is optimised for the reducing-zone of sulfuric acid (0-85% H₂SO₄). Above approximately 85% H₂SO₄, the acid becomes strongly oxidising (due to thermal decomposition producing SO₃ and O₂), and the copper in Alloy 20 is oxidatively attacked.
For concentrated acid (>85%) at elevated temperatures: 316L or 310S stainless steel is preferred for 85-98% H₂SO₄ above 80°C; Tantalum (Ta) is the only practical material for fuming oleum (>98%) at any temperature above ambient. For the most aggressive intermediate range (50-80% H₂SO₄ above 80°C), Hastelloy G-30 (UNS N06030, PREN 42-52) or Sanicro 28 (UNS N08028) should be specified instead of standard Alloy 20. Alloy 20 is a specific-purpose alloy, not a universal sulfuric acid material.
Q: What is the difference between Alloy 20, Alloy 20Cb-3, and Alloy 20 Mod.?
A: Standard Alloy 20 (UNS N08020): C ≤ 0.07%, Nb ≥ 8 × C, Cu 3-4%, Mo 2-3%. This is the most widely stocked and lowest-cost variant. Alloy 20Cb-3 (same UNS N08020, with Si 0.5-1.0% added): Silicon is added to improve corrosion resistance in the 50-80% H₂SO₄ range at temperatures up to 90-95°C.
The Si-modified chemistry forms a silicon-enriched passive film that is more resistant to the mixed reducing-oxidising conditions in the transition zone. Cb-3 is the preferred variant for hot acid above 75°C in the intermediate concentration range. Alloy 20 Mod. / Low-Si variant (C ≤ 0.04%): Lower carbon version with reduced Si (≤0.3%). The low Si improves toughness in cryogenic service and reduces the risk of sigma phase embrittlement during long-term high-temperature exposure. Not a major commercial product form.
Q: Can Alloy 20 be used in sulfuric acid with chloride contamination?
A: Yes, but with restrictions. The chloride threshold for Alloy 20 in sulfuric acid is approximately 200 ppm Cl⁻ at 60°C in 20% H₂SO₄. Above this level, the combination of H⁺ (acid attack) and Cl⁻ (pitting initiator) produces simultaneous general corrosion and pitting.
For chloride-bearing sulfuric acid (common in: pickling baths where HCl is mixed with H₂SO₄, mining leach solutions with saline water, acid mixtures with seawater cooling contamination), the following hierarchy applies: Cl⁻ < 200 ppm in H₂SO₄ → Alloy 20 is adequate Cl⁻ 200-1,000 ppm in H₂SO₄ → Hastelloy G-30 recommended Cl⁻ > 1,000 ppm → Hastelloy C-276 or C-22 required (only Hastelloy C-series survives sulfuric + chloride combinations above 1,000 ppm Cl⁻) Verify chloride content in your specific process stream before specifying Alloy 20.
Q: What causes Alloy 20 vessels to fail prematurely in sulfuric acid service?
A: The five most common causes of Alloy 20 premature failure in sulfuric acid are:
(1) Grade substitution: 316L or 904L supplied instead of Alloy 20 - PMI (XRF) on receipt would have prevented this.
(2) Weld filler mismatch: stainless steel filler (308L, 316L) used instead of ERNiCrMo-3 - ERNiCrMo-3 filler is mandatory.
(3) Velocity neglect: turbulent flow ( > 2 m/s) in intermediate acid causing erosion-corrosion well above laboratory immersion test rates - design for velocity limits and use Hastelloy G-30 for high-velocity zones.
(4) Temperature miscalculation: operating temperature above the isocorrosion limit for the specific acid concentration - re-check with process engineering and consider Hastelloy G-30 for temperatures 10-20°C above Alloy 20 limits.
(5) Condensing acid in vapour space: inadequate material specification for the vapour space above the acid liquid level - the vapour space of any sulfuric acid vessel above 40°C must be Alloy 20 or Hastelloy, not carbon steel or 316L.
Q: What is the maximum service temperature for Alloy 20 in sulfuric acid?
A: The maximum service temperature depends on the acid concentration. In dilute acid (0-10% H₂SO₄): Alloy 20 maintains <0.5 mm/yr up to approximately 90°C.
In intermediate acid (10-50% H₂SO₄): Alloy 20 is reliable to 80-90°C. In the most aggressive transition zone (50-80% H₂SO₄): standard Alloy 20 reaches its limit at approximately 75-80°C - use Cb-3 variant or Hastelloy G-30 above 80°C.
In concentrated acid (85-98% H₂SO₄): Alloy 20 is NOT recommended above 40°C (316L or Tantalum are correct for this range). These are quiescent (no-flow) conditions. In turbulent flow, reduce all temperature limits by 10-15°C to account for the velocity-enhanced corrosion effect.
Q: How does Alloy 20 compare economically to 316L stainless steel in sulfuric acid?
A: Alloy 20 sheet costs approximately 5-7× more per kilogram than 316L sheet.
However, total installed cost analysis tells a different story: 316L in 30% H₂SO₄ at 60°C: corrosion rate 1-2 mm/year. With 6 mm wall thickness (corrosion allowance included), 316L vessel requires replacement every 3-5 years. Alloy 20 in 30% H₂SO₄ at 60°C: corrosion rate 0.1-0.2 mm/year.
With the same 6 mm wall, Alloy 20 vessel is designed for 20+ years with minimal maintenance. The life-cycle cost advantage of Alloy 20 is typically 3-5× over a 20-year period when downtime, replacement, and environmental compliance costs are included. The only exception is dilute acid (<10%) at <50°C, where 316L lasts adequately and Alloy 20 premium cost cannot be justified.

