904L vs 316L Stainless Steel Sulfuric Acid Resistance Showdown

Jun 05, 2026

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Anna Chen
Anna Chen
Junior R&D Scientist at Jinie Technology, focused on developing new materials and processes for stainless steel and nickel alloys. Passionate about innovation and sustainable manufacturing solutions.

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

 

.904L vs 316L Stainless Steel

 

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

 
Both grades are supplied in the solution-annealed and water-quenched condition, producing the maximum corrosion resistance and ductility. The table below presents minimum requirements and typical achieved values for plate and sheet products.
 
904L vs 316L Stainless Steel 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.

 

Applicable Standards and International Certifications

 

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

 

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