Comparison
316 vs 317L Stainless Steel
All values are from ASTM A240/A240M and ASME SA-240. The molybdenum and nickel ranges are the only significant differences between the two grades, but those differences shift the PREN by approximately 4 points — enough to double the time-to-pitting in aggressive chloride environments.
| Property | 316 / 316L (UNS S31600/S31603) | 317L (UNS S31703) |
|---|---|---|
| Chromium (Cr) | 16.0 – 18.0% | 18.0 – 20.0% |
| Nickel (Ni) | 10.0 – 14.0% | 11.0 – 15.0% |
| Molybdenum (Mo) | 2.0 – 3.0% | 3.0 – 4.0% |
| Carbon (C) max | 0.08% (316) / 0.030% (316L) | 0.030% |
| Tensile Strength (min) | 515 MPa (316) / 485 MPa (316L) | 515 MPa |
| Yield Strength (min) | 205 MPa (316) / 170 MPa (316L) | 205 MPa |
| PREN Value | ~24 – 26 | ~28 – 30 |
| Density (g/cm³) | 8.0 | 8.0 |
| Common Fitting Specs | A182 F316/F316L, A403 WP316/WP316L | A182 F317L, A403 WP317L, A312 TP317L |
| Relative Material Cost | 1.30 – 1.48 (vs 304) | 1.45 – 1.65 (vs 304) |
The molybdenum content in 316 is 2.0–3.0%. In 317L, it is 3.0–4.0%. That single percentage point may seem minor, but the PREN formula multiplies Mo by 3.3. An increase from 2.5% Mo to 3.5% Mo adds 3.3 PREN points. Combined with the higher chromium (18–20% versus 16–18%) and nickel (11–15% versus 10–14%), the total PREN jump is from ~26 to ~30. In corrosion engineering, a 4-point PREN increase typically extends pitting initiation time by a factor of 3–5 in chloride environments.
The mechanism is straightforward: molybdenum incorporates into the passive oxide film as MoO₄²⁻ species. These molybdate ions adsorb onto active pit sites and inhibit the anodic dissolution reaction that propagates pitting. At 2.5% Mo, the molybdate coverage is sufficient for moderate chlorides. At 3.5% Mo, the coverage is dense enough to withstand chloride concentrations above 5,000 ppm at 60°C. We have seen 316L heat exchanger tubes fail by pitting within 18 months in a chemical plant recirculating loop at 4,200 ppm Cl⁻ and 55°C. Replacement with 317L tubes has now run 4 years with zero pitting.
The higher nickel in 317L (11–15% versus 10–14%) improves resistance to reducing acids such as sulfuric and hydrochloric acid. Nickel stabilizes the austenite phase and reduces the tendency for stress-corrosion cracking in chloride environments. In dilute sulfuric acid at 50°C, 316L shows measurable weight loss above 10% concentration. 317L extends that threshold to approximately 15% concentration. For FGD absorber slurries, which contain both sulfite/sulfate species and chlorides at 10,000–30,000 ppm, the combined Mo and Ni advantage makes 317L the standard grade.
In the corrosion-resistant austenitic family, there is a large jump from 316L (PREN ~26) to 904L (PREN ~34) or 254SMO (PREN ~42). 317L sits at PREN ~30, filling that gap at a much lower cost than either super-austenitic grade. For applications where 316L is marginal but 904L is overkill, 317L is the rational intermediate choice.
| Grade | PREN | Relative Cost (vs 304) | Typical Application |
|---|---|---|---|
| 316L | ~26 | 1.33 – 1.48 | General chemical, marine, food |
| 317L | ~30 | 1.45 – 1.65 | FGD, high-chloride chemical, pulp bleach |
| 904L | ~34 | 2.5 – 3.0 | Severe sulfuric acid, high-temp chlorides |
| 254SMO | ~42 | 4.0 – 5.5 | Seawater, sour gas, aggressive halides |
FGD systems scrub sulfur dioxide from coal-fired power plant exhaust using limestone slurry. The resulting absorber slurry contains calcium sulfite, calcium sulfate (gypsum), chlorides from coal combustion, and fluorides. Chloride concentrations in the slurry typically range from 10,000 to 50,000 ppm. The pH fluctuates between 4.5 and 6.5. This environment destroys 316L within 2–3 years in the absorber, recycle piping, and spray headers.
317L is the minimum acceptable grade for FGD absorber internals, outlet ducting, and slurry piping. The 3.0–4.0% Mo provides the molybdate inhibition needed to survive the chloride-sulfate combination. We have supplied ASTM A403 WP317L 90° elbows and A182 F317L slip-on flanges to three FGD retrofit projects in 2024. In each case, the EPC originally specified 316L and our corrosion engineers submitted a value-engineering change notice recommending 317L. All three were approved without dispute once the chloride levels were reviewed.
317L welds with ER317L filler, which matches the 3.0–4.0% Mo content. The weld pool is slightly more viscous than 316L, requiring 5–10% higher amperage for the same travel speed. Post-weld passivation is critical — the heat tint on 317L is more tenacious than on 316L because the higher Mo forms a thicker oxide scale. We use a nitric-hydrofluoric acid pickle followed by neutralization and a final nitric acid passivation. Without this two-step treatment, the heat-tinted zone can show preferential pitting initiation within 6 months in FGD service.
In 2024–2025, we received three separate inquiries that highlight the 316 versus 317L decision:
Our rule: when chloride exceeds 2,000 ppm and temperature exceeds 50°C, run a PREN check. If PREN < 28 is marginal for the design life, 317L is the next step up from 316L. If PREN > 32 is needed, skip 317L and go to duplex or super-austenitic.
Yes, fundamentally. 317L is an austenitic stainless steel with the same basic structure as 316L but with 3.0–4.0% Mo versus 2.0–3.0%, plus slightly higher Cr (18–20% versus 16–18%) and Ni (11–15% versus 10–14%). The carbon is capped at 0.030% like 316L. It is not a different alloy system — it is the same family with corrosion resistance dialed up one notch.
PREN = %Cr + 3.3 × %Mo + 16 × %N. For typical compositions: 316L PREN ≈ 24–26; 317L PREN ≈ 28–30. The 4-point gap translates to 3–5× longer pitting initiation time in chloride environments. As a rule of thumb, 317L can handle chloride concentrations roughly twice as high as 316L at the same temperature before pitting starts.
317L is marginal in raw seawater. Seawater chloride is approximately 19,000 ppm, and the PREN of ~30 is near the threshold for crevice corrosion in ambient seawater. For splash zones and slow-moving seawater, 317L may last 3–5 years before crevice corrosion initiates under gaskets or deposits. For reliable long-term seawater service, we recommend 254SMO (PREN ~42), 2507 super duplex (PREN ~42), or titanium. We have supplied 317L for seawater cooling systems with strict cathodic protection and 6-month inspection cycles, but it is not a fit-and-forget solution.
317L is the only common variant because the applications that need 317's corrosion resistance are almost always welded. A standard-carbon 317 (0.08% C max) would sensitize in the HAZ and lose its corrosion advantage. The mills therefore produce almost exclusively 317L. If you need higher carbon for creep strength, 321H or 347H are the appropriate grades, not a hypothetical 317H.
Based on HT PIPE 2025 procurement data, 317L pipe and fittings cost 10–15% more than 316L. The premium comes from the extra molybdenum (ferro-molybdenum has traded between $22 and $38 per kg over the last 12 months) and the higher nickel. For a 6" SCH40 seamless pipe, the 317L premium is approximately 12%. For forged flanges, it is closer to 15% because 317L has a narrower forging temperature window and higher die wear.
Use ER317L filler metal. It matches the 3.0–4.0% Mo content of the base metal. Do not use ER316L filler — the weld deposit will have only 2.0–3.0% Mo and will become the weak link in a chloride environment. Post-weld heat tint removal and passivation are mandatory for 317L in aggressive service. We use a two-step process: HF-HNO₃ pickle to remove scale, followed by a 20% HNO₃ passivation to restore the chromium-rich passive film.