When sulfuric acid enters the equation, the choice of stainless steel grade is not merely a matter of preference - it can determine whether a plant runs reliably for twenty years or suffers a corrosion failure within twenty months. This article delivers a rigorous, data-driven comparison of 904L (UNS N08904 / EN 1.4539) and 316L (UNS S31603 / EN 1.4404), the two most commonly evaluated grades when engineers face acid-containing process environments
.
Bottom-Line Findings:
904L is demonstrably superior to 316L in sulfuric acid service across nearly every concentration and temperature range where 316L is even marginally viable.
316L is the cost-effective standard grade for general-purpose applications where sulfuric acid is absent or present only in trace quantities at ambient temperature.
For moderate-to-severe acid duty, the higher initial cost of 904L is consistently justified by dramatically lower corrosion rates, extended equipment life, and reduced unplanned downtime.
Understanding Sulfuric Acid Corrosion of Stainless Steels
Sulfuric acid (H₂SO₄) is the world's most widely produced industrial chemical, used in fertilizer manufacturing, metal pickling, petroleum refining, battery production, and dozens of other processes. Understanding why it is so corrosive to metals - and why alloy selection matters so much - is essential context for every engineer working in these industries.
Why H₂SO₄ Is Especially Corrosive
Sulfuric acid attacks metals through two primary mechanisms: direct acid attack (hydrogen evolution), which dominates at concentrations below approximately 40%, and a passive-film-dissolving mechanism at intermediate concentrations. At very high concentrations (above 93%), the acid becomes dehydrating and actually forms a protective layer on some alloys - but this is a narrow and highly temperature-sensitive window.
For practical engineering purposes, the most dangerous zone for stainless steels is the 5–70% concentration range at temperatures above 40°C. In this range, all standard austenitic grades including 316L experience rapid passive film breakdown, leading to accelerated general corrosion.
The Role of Alloying Elements
Three alloying elements are critical to H₂SO₄ resistance in austenitic stainless steels: molybdenum (Mo), nickel (Ni), and copper (Cu). Understanding their roles makes the 904L vs 316L performance gap immediately logical.
Molybdenum (Mo): Mo stabilises the passive film in reducing acid environments. 904L contains 4–5% Mo versus only 2–3% in 316L. This difference roughly doubles the passive film stability in sulfuric acid.
Nickel (Ni): Ni reduces the rate of active dissolution and shifts the alloy toward passivity in reducing media. 904L's 23–28% Ni content (versus 10–14% in 316L) is perhaps the single largest driver of its acid performance advantage.
Copper (Cu): The deliberate addition of 1–2% Cu in 904L is specifically engineered to reduce the corrosion rate in dilute-to-moderate H₂SO₄. 316L contains no copper. This is one of the most decisive compositional differences between the two grades.
Chemical Composition Comparison
The composition table below is the starting point for understanding every performance difference between these two grades. All values are per official material specifications.
Table 1: Chemical Composition - 316L vs 904L (All values in weight %)
|
Element |
316L Min |
316L Max |
904L Min |
904L Max |
Unit |
|
Chromium (Cr) |
16.0 |
18.0 |
19.0 |
23.0 |
% |
|
Nickel (Ni) |
10.0 |
14.0 |
23.0 |
28.0 |
% |
|
Molybdenum (Mo) |
2.0 |
3.0 |
4.0 |
5.0 |
% |
|
Copper (Cu) |
- |
- |
1.0 |
2.0 |
% |
|
Manganese (Mn) |
- |
2.00 |
- |
2.00 |
% |
|
Silicon (Si) |
- |
0.75 |
- |
1.00 |
% |
|
Carbon (C) |
- |
0.030 |
- |
0.020 |
% |
|
Nitrogen (N) |
- |
0.10 |
- |
0.10 |
% |
|
Sulfur (S) |
- |
0.030 |
- |
0.035 |
% |
|
Phosphorus (P) |
- |
0.045 |
- |
0.045 |
% |
|
Iron (Fe) |
Balance |
Balance |
Balance |
Balance |
- |
The Three Critical Compositional Differences
Nickel Differential (+13–14% more in 904L): Nickel is the single most important element for reducing active dissolution in reducing acids. The 13–14 percentage point gap in nickel content between 904L and 316L is responsible for a large portion of 904L's superior corrosion performance.
Molybdenum Differential (+2% more in 904L): An additional 2% molybdenum in 904L stabilises the passive film in acidic conditions. While this may appear modest, Mo's effect on passive film stability is non-linear and provides disproportionate benefit in concentrated acid environments.
Copper Addition (1–2% in 904L, absent in 316L): This is the most underappreciated difference. Copper directly reduces the rate of hydrogen evolution corrosion in sulfuric acid by acting as a cathodic inhibitor. 316L has no copper at all, and no amount of other alloying can compensate for its absence in sulfuric acid service.
Mechanical Properties Comparison
Table 2: Mechanical Properties - 316L vs 904L
|
Property |
316L Req. |
316L Typical |
904L Req. |
904L Typical |
|
Tensile Strength (MPa) |
≥485 |
~560 |
≥490 |
~540 |
|
0.2% Yield Strength (MPa) |
≥170 |
~220 |
≥220 |
~260 |
|
Elongation at Break (%) |
≥40 |
~50 |
≥35 |
~42 |
|
Hardness (HB) |
≤217 |
~150 |
≤200 |
~170 |
|
Impact Toughness (J, -196°C) |
Good |
~80–120 |
Very Good |
~100–140 |
|
Modulus of Elasticity (GPa) |
~193 |
193 |
~196 |
196 |
|
Density (g/cm³) |
7.99 |
7.99 |
8.00 |
8.00 |
904L offers slightly higher minimum yield strength than 316L, primarily because it contains more nickel and slightly more controlled nitrogen. Both grades provide excellent ductility and toughness at all temperatures including cryogenic conditions. For most chemical process applications, the mechanical property differences are secondary to corrosion performance in the material selection decision.
Sulfuric Acid Corrosion Rate Data: The Core Evidence
This section presents the most important data in this article. The corrosion rate comparison across a matrix of H₂SO₄ concentrations and temperatures is the definitive basis for material selection in acid service. All values are in millimetres per year (mm/y); a value below 0.1 mm/y is generally considered acceptable for long-term service.
Table 3: Corrosion Rates in Sulfuric Acid - 316L vs 904L (mm/year)
|
H₂SO₄ Conc. (wt%) |
Temp. (°C) |
316L Rate (mm/y) |
904L Rate (mm/y) |
Improvement Factor |
904L Suitability |
316L Suitability |
|
1–5 |
20 |
0.05–0.10 |
0.01–0.02 |
~5× |
Excellent |
Very Good |
|
1–5 |
60 |
0.20–0.50 |
0.03–0.08 |
~6× |
Excellent |
Acceptable |
|
5–20 |
20 |
0.50–1.50 |
0.05–0.15 |
~10× |
Very Good |
Marginal |
|
5–20 |
60 |
1.50–5.00 |
0.10–0.40 |
~12× |
Good |
Not Suitable |
|
20–40 |
20 |
3.00–8.00 |
0.20–0.80 |
~10× |
Good–Acceptable |
Not Suitable |
|
20–40 |
60 |
>10 |
0.50–2.00 |
>5× |
Marginal |
Not Suitable |
|
40–70 |
20 |
>10 |
0.80–3.00 |
>3× |
Marginal |
Not Suitable |
|
40–70 |
60 |
>>10 |
2.00–8.00 |
- |
Not Suitable |
Not Suitable |
|
70–90 |
20 |
>>10 |
>5.00 |
- |
Not Suitable |
Not Suitable |
|
90–98 |
20 |
>>10 |
>5.00 |
- |
Not Suitable |
Not Suitable |
Interpreting the Corrosion Rate Data
The data in Table 3 tells a clear, consistent story: 904L outperforms 316L by a factor of 5 to 12 times across the most industrially common sulfuric acid conditions (1–40% concentration, 20–60°C operating temperature). More importantly, for concentrations above 5% at temperatures above 40°C, 316L frequently exceeds the 1.0 mm/y threshold - making it functionally unsuitable, regardless of design allowances.
At concentrations above 40–70%, neither grade provides adequate resistance in long-term service. Engineers encountering concentrated sulfuric acid (above 70%) must evaluate specialist alloys such as Alloy 20 (UNS N08020), Hastelloy B-3 (UNS N10675), or high-silicon cast iron, which are specifically designed for concentrated H₂SO₄ service.
Multi-Environment Corrosion Resistance Comparison
Sulfuric acid is rarely the only corrosive species in an industrial process stream. The following table provides a broader view of how these two grades perform across all major corrosion mechanisms and acid types.
Table 4: Multi-Environment Corrosion Resistance - 316L vs 904L
|
Corrosion Mechanism / Environment |
904L Performance |
Rating |
316L Performance |
Rating |
|
Dilute H₂SO₄ (<10%, ambient) |
Excellent |
★★★★★ |
Good |
★★★☆☆ |
|
Dilute H₂SO₄ (<10%, 60°C) |
Very Good |
★★★★☆ |
Marginal |
★★☆☆☆ |
|
Conc. H₂SO₄ (40–70%, ambient) |
Marginal |
★★☆☆☆ |
Not Suitable |
★☆☆☆☆ |
|
Phosphoric Acid (H₃PO₄) |
Excellent |
★★★★★ |
Good |
★★★☆☆ |
|
Acetic Acid (CH₃COOH) |
Excellent |
★★★★★ |
Very Good |
★★★★☆ |
|
Hydrochloric Acid (HCl) |
Poor |
★★☆☆☆ |
Poor |
★☆☆☆☆ |
|
Chloride Pitting (Cl⁻ env.) |
Very Good |
★★★★☆ |
Good |
★★★☆☆ |
|
Crevice Corrosion (seawater) |
Good |
★★★☆☆ |
Marginal |
★★☆☆☆ |
|
Intergranular Corrosion |
Excellent |
★★★★★ |
Very Good |
★★★★☆ |
|
Stress Corrosion Cracking (SCC) |
Very Good |
★★★★☆ |
Marginal |
★★☆☆☆ |
|
Oxidising Acids (HNO₃) |
Good |
★★★☆☆ |
Very Good |
★★★★☆ |
Nitric Acid: The One Area Where 316L Has an Edge
Nitric acid (HNO₃) is an oxidising acid, and in oxidising acid environments, chromium content dominates the resistance mechanism. Both grades have similar chromium levels (16–18% in 316L; 19–23% in 904L), but 316L's lower molybdenum actually makes it slightly better suited to pure HNO₃ service because Mo can be detrimental in highly oxidising environments. However, this is a narrow exception - any process mixing HNO₃ with HCl or H₂SO₄ (mixed acids) immediately swings the advantage back to 904L.
Chloride Resistance: Pitting and Crevice Corrosion
The Pitting Resistance Equivalent Number (PREN) quantifies resistance to chloride-induced pitting. 904L achieves a PREN of approximately 32–36 versus 316L's 23–27. This gap is significant in any application where chloride ions co-exist with sulfuric acid - a common situation in industrial process streams, flue gas environments, and water treatment applications.
Physical and Thermal Properties
Table 5: Physical and Thermal Properties - 316L vs 904L
|
Property |
316L |
904L |
|
Melting Range (°C) |
1375–1400 |
1300–1390 |
|
Density (g/cm³) |
7.99 |
8.00 |
|
Thermal Conductivity (W/m·K, 20°C) |
13.4 |
12.0 |
|
Coeff. of Thermal Expansion (µm/m·°C) |
16.0 (20–100°C) |
15.3 (20–100°C) |
|
Specific Heat Capacity (J/kg·K) |
500 |
450 |
|
Electrical Resistivity (µΩ·m) |
0.74 |
0.95 |
|
Magnetic Permeability (annealed) |
~1.005 |
~1.003 |
|
Max Service Temp. – Oxidising (°C) |
~870 |
~1050 |
|
Max Service Temp. – Aqueous (°C) |
~300 |
~300 |
Both grades share broadly similar physical and thermal properties, as expected for austenitic alloys with comparable overall alloying levels. The slightly higher thermal expansion of 316L may be relevant in heat exchanger tube design but rarely drives material selection. Both grades are non-magnetic in the annealed condition, making them suitable for applications requiring low magnetic permeability (e.g., MRI facility construction, certain instrumentation).
Applicable Standards and International Certifications
Correct standard designation is essential for procurement, quality inspection, and regulatory compliance. The following table covers all major international designation systems for both grades.

Table 6: Standards and Designations - 316L vs 904L
|
Standard Body |
316L Designation |
904L Designation |
Scope / Notes |
|
ASTM |
S31603 |
N08904 |
Plate, Sheet, Strip, Bar, Pipe, Tube |
|
EN / DIN |
1.4404 |
1.4539 |
European product forms |
|
UNS |
S31603 |
N08904 |
Unified Numbering System |
|
ASME |
SA-240 / SA-312 |
SA-240 / SA-312 |
Pressure Vessels, Boilers, Piping |
|
ISO |
ISO 15156-3 |
ISO 15156-3 |
Sour-service (H₂S environments) |
|
NACE / AMPP |
MR0175 Compliant |
MR0175 Compliant |
Oil & gas corrosion service |
|
PED (EU) |
2014/68/EU |
2014/68/EU |
Pressure Equipment Directive |
|
FDA (food/pharma) |
Accepted |
Accepted |
Surface finish Ra ≤ 0.8 µm typical |
Both grades are fully covered under ASME, ASTM, and EN frameworks for pressure vessels, heat exchangers, and piping systems. For FDA-regulated pharmaceutical and food applications, both grades are accepted, with 316L being the near-universal default due to its established track record, lower cost, and extensive global supply chain.
Cost, Availability, and Fabrication
Material cost is often the most immediately visible decision factor, but lifecycle cost - which includes maintenance, replacement, and production downtime - almost always favours the higher-performance alloy in acid service. The following table presents the key commercial and fabrication parameters.
Table 7: Cost, Availability, and Fabrication - 316L vs 904L
|
Factor |
316L |
904L |
|
Relative Material Cost (Plate) |
Baseline (1.0×) |
~1.8–2.5× (higher Ni, Mo) |
|
Primary Cost Drivers |
Ni (10–14%), Mo (2–3%) |
Ni (23–28%), Mo (4–5%), Cu |
|
Global Availability |
Ubiquitous – all mill sizes |
Widely available – specialty |
|
Typical Lead Time (Plate) |
1–4 weeks |
3–8 weeks |
|
Weldability |
Excellent (ER316L filler) |
Very Good (ER385 filler) |
|
Machinability |
Good |
Good to Moderate |
|
Fabrication Complexity |
Low – easy to form/weld |
Moderate – standard austenitic |
|
Surface Finish Options |
All standard finishes |
All standard finishes |
|
Mill Certification (EN 10204) |
3.1 routinely available |
3.1 / 3.2 available |
Welding Guidelines
Correct filler metal selection is critical to maintaining corrosion resistance in the weld zone:
316L: AWS ER316L filler (or matching covered electrode E316L). Low heat input. No preheating required. Wide process window makes 316L the most easily fabricated stainless grade globally.
904L: AWS ER385 filler metal (or Avesta 904L / Sandvik 27.31.4.LCu type). Slightly tighter interpass temperature control recommended. Full solution anneal post-weld is not mandatory but is recommended for the most aggressive services. Purge with inert gas for pipe root passes.
Both grades: No preheating required. Use stainless-steel wire brushes and dedicated grinding wheels. Clean surfaces thoroughly to remove iron contamination and prevent free iron corrosion.
Application Selection Guide and Industry Case Studies
The following selection table provides engineers, procurement specialists, and plant managers with direct, evidence-based guidance on which grade to specify for given service conditions.
Table 8: Application and Industry Selection Guide - 316L vs 904L
|
Application / Environment |
316L |
904L |
Key Technical Rationale |
|
Dilute H₂SO₄ storage (<5%, ambient) |
Viable |
Preferred |
904L's Cu+Mo combination dramatically lowers corrosion rate |
|
H₂SO₄ piping systems (<20%, <60°C) |
Marginal |
Preferred |
316L corrosion rate exceeds 1 mm/y at these conditions |
|
H₂SO₄ neutralisation / scrubbing |
Viable |
Preferred |
Mixed acid/water streams favour 904L's broader resistance |
|
Phosphoric acid (H₃PO₄) processing |
Viable |
Preferred |
Both perform well; 904L superior at elevated temperatures |
|
Acetic acid process equipment |
Preferred |
Viable |
316L adequate at low temp.; saves cost vs 904L for mild duty |
|
Nitric acid (HNO₃) service |
Preferred |
Viable |
Oxidising acid favours Cr; 316L cost-effective here |
|
Pharmaceutical vessels & reactors |
Preferred |
Viable |
316L FDA-standard; 904L only if process requires it |
|
Food & beverage processing |
Preferred |
Viable |
316L meets all hygienic standards at far lower cost |
|
Seawater cooling / heat exchangers |
Marginal |
Preferred |
904L pitting resistance (PREN ~32) vs 316L's (~24) |
|
Fertiliser plant – sulphate streams |
Not Suitable |
Preferred |
Warm sulphate + chloride combination requires 904L |
|
Oil & gas production – sour service |
Viable |
Preferred |
904L higher Ni reduces risk of SCC in H₂S environments |
|
Cryogenic / LNG storage |
Preferred |
Viable |
316L widely qualified for LNG; 904L over-specified here |
|
General utility piping (non-acid) |
Preferred |
Viable |
316L offers equivalent performance at significant cost saving |
Summary: 316L vs 904L
The table below distills every dimension of this comparison into a single concise reference.
Table 10: Comprehensive Comparison Summary - 316L vs 904L
|
Dimension |
904L |
316L |
|
UNS / EN Designation |
N08904 / 1.4539 |
S31603 / 1.4404 |
|
Nickel Content |
23–28% (much higher) |
10–14% |
|
Molybdenum Content |
4–5% |
2–3% |
|
Copper Addition |
1–2% (acid resistance boost) |
None |
|
PREN Value |
~32–36 |
~23–27 |
|
H₂SO₄ Resistance |
Superior across concentrations |
Limited to dilute/ambient |
|
Corrosion Rate (<10% H₂SO₄) |
5–12× lower than 316L |
Baseline |
|
SCC Resistance |
Very Good (high Ni) |
Marginal |
|
Seawater Resistance |
Good |
Marginal |
|
Weldability |
Very Good |
Excellent |
|
Relative Material Cost |
~1.8–2.5× higher |
Baseline |
|
Global Availability |
Widely available (specialty) |
Ubiquitous |
|
Best Fit |
Acid / chemical duty |
General / food / pharma |


