Chloride pitting is the single most common reason stainless steel equipment fails in seawater, and the fastest way to judge whether an alloy will survive it is a number called PREN. Inconel 625 (UNS N06625) posts a PREN of roughly 51 - more than double that of 316L stainless steel and comfortably above every widely accepted threshold for full seawater immersion. This article shows exactly how that number is calculated, how 625 compares with every competing alloy class, what its critical pitting temperature (CPT) data means in practice, and where its real application limits lie - so that engineers, buyers, and specification writers can cite the numbers with confidence.

What Is Chloride Pitting, and Why Is It So Dangerous in Seawater?
Chloride pitting is a localized breakdown of an alloy's protective passive film by chloride ions, producing small, deep pits that can perforate equipment far faster than uniform corrosion ever would - and seawater is the most abundant natural source of the chloride ions that drive it.
Most corrosion-resistant alloys survive not because they are chemically inert, but because they spontaneously grow an ultra-thin, self-healing oxide layer - the passive film - that blocks further attack. In stagnant or low-oxygen water, chlorides (Cl⁻) attack that film through a distinctive mechanism:
- Film attack: the small chloride ion adsorbs onto the oxide surface and competes with oxygen at weak points - inclusions, scratches, MnS stringers, weld defects;
- Autocatalysis: once a microscopic breach opens, dissolved metal ions hydrolyze inside it, releasing H⁺ and dropping the local pH to values as low as 0–1, while chloride ions migrate inward to balance the charge;
- Propagation: the pit now contains its own concentrated hydrochloric acid, so it deepens at an accelerating rate even though the surrounding surface stays bright and intact.
This is what makes pitting uniquely dangerous. Total weight loss can be negligible - a few milligrams - while a pinhole penetrates a 5 mm pipe wall in months. Failures are hidden, sudden, and leak-before-warning. Seawater contains roughly 19,000–20,000 mg/L of chloride (about 3.5% total salinity), which is why material selection for marine service is dominated by one question: can this alloy resist chloride pitting - and for how long, at what temperature, and in what geometry?
What Is PREN, and How Is It Calculated?
PREN - the Pitting Resistance Equivalent Number - is a single-figure index that ranks an alloy's resistance to chloride pit initiation. The standard formula is PREN = %Cr + 3.3 × %Mo + 16 × %N.
The formula is empirical: it was developed by correlating alloy composition with measured critical pitting temperatures across the stainless steel family. Each element earns its coefficient for a specific, well-understood reason:
- Cr (coefficient 1.0): chromium is the backbone of the passive Cr₂O₃ film; more chromium means a thicker, more stable barrier that heals faster after damage.
- Mo (coefficient 3.3): molybdenum is the strongest single ally against chlorides. It slows film dissolution, speeds repassivation of incipient pits, and enriches the chemistry inside a pit so it cannot easily sustain the autocatalytic cycle. This is why Mo carries the 3.3 multiplier.
- N (coefficient 16): nitrogen dissolves into the alloy surface during repassivation, raises the local pH inside a developing pit, and acts synergistically with Mo. It is weighted most heavily at 16 per unit.
Two variants matter in practice. For tungsten-bearing alloys such as Hastelloy C-276, many engineers use the extended formula PREN = %Cr + 3.3 × %Mo + 16 × %N + 1.65 × %W. And it must be said plainly: PREN was calibrated on stainless steels. Applied to solid-solution nickel alloys it works well as a comparative ranking tool, but it does not capture everything - most importantly, it ignores the nickel matrix itself, which is far more tolerant of the acidic pit chemistry than an iron matrix is. A nickel alloy therefore tends to out-perform its PREN in real chloride service, not under-perform it.
What Is the PREN of Inconel 625?
Using the standard formula on ASTM B443 composition limits, Inconel 625's PREN is approximately 47–56, with a typical nominal value of about 51. That places it firmly in the top tier of commercially available chloride-resistant alloys.
Inconel 625 is specified under ASTM B443 (plate, sheet, strip) and B444/B446 (tube, bar) with the following controlling composition:
|
Element |
ASTM B443 limit (wt.%) |
Nominal (wt.%) |
Role in chloride resistance |
|
Nickel (Ni) |
≥58.0 (balance) |
~61 |
Matrix: resists acidic pit chemistry; immune to chloride stress corrosion cracking |
|
Chromium (Cr) |
20.0–23.0 |
21.5 |
Forms and stabilizes the passive oxide film |
|
Molybdenum (Mo) |
8.0–10.0 |
9.0 |
Primary pitting inhibitor; repassivation promoter |
|
Niobium + Tantalum (Nb+Ta) |
3.15–4.15 |
3.6 |
Solid-solution strengthening, weldability; not a PREN element |
|
Iron (Fe) |
≤5.0 |
~2.5 |
Residual; kept low |
|
Carbon (C) |
≤0.10 (Grade 1) |
~0.05 |
Kept low to avoid sensitization |
|
Nitrogen (N) |
trace (≤~0.05) |
<0.02 |
Negligible PREN contribution in Ni alloys |
The calculation is then straightforward, working from the specification limits:
|
Basis |
Calculation |
PREN |
|
Specification minimum |
20.0 + 3.3 × 8.0 + 0 |
= 46.4 |
|
Typical mill chemistry |
21.5 + 3.3 × 9.0 + ~0 |
≈ 51 |
|
Specification maximum |
23.0 + 3.3 × 10.0 + 0 |
= 56.0 |
Three honest qualifications belong in any rigorous discussion. First, nitrogen is present only as a trace residual in 625, so it adds at most a fraction of a point - unlike in super duplex steels, where nitrogen is a deliberate alloying addition worth several PREN points. Second, niobium - 625's signature element - is not counted in PREN at all, because Nb does not participate in the Cr–Mo passive-film chemistry the index measures; it is there for high-temperature strength and weld soundness. Third, 625 contains no tungsten, so the extended (W-bearing) PREN formula returns the same value. On any reasonable variant of the formula, Inconel 625 lands between roughly 47 and 56, and "about 51" is the defensible single number to cite.
How Does Inconel 625's PREN Compare with Other Corrosion-Resistant Alloys?
At PREN ≈ 51, Inconel 625 outperforms every stainless steel - including super duplex 2507 - and nearly every mainstream nickel alloy. Only molybdenum- and tungsten-rich grades such as Hastelloy C-276 rank higher.
|
Alloy (UNS) |
Cr (%) |
Mo (%) |
PREN (typical) |
Practical seawater verdict |
|
316L (S31603) |
17 |
2.1 |
≈ 24 |
Pits in ambient seawater - unsuitable for immersion |
|
Alloy 20 (N08020) |
20 |
2.5 |
≈ 29 |
Sulfuric acid specialist; not a seawater pitting alloy |
|
Alloy 825 (N08825) |
21.5 |
3.0 |
≈ 31 |
Good general corrosion alloy; marginal in stagnant seawater |
|
904L (N08904) |
21 |
4.5 |
≈ 36 |
Resists ambient seawater on smooth surfaces; crevice risk |
|
Duplex 2205 (S32205) |
22 |
3.2 |
≈ 35 |
Similar to 904L; better strength, crevice caution |
|
Super duplex 2507 (S32750) |
25 |
4.0 |
≈ 43 |
Widely used in ambient seawater; crevice/temperature limits apply |
|
Monel 400 (N04400) |
- |
- |
≈ 0* |
Excellent in flowing seawater by a different mechanism; pits when stagnant* |
|
Inconel 625 (N06625) |
21.5 |
9.0 |
≈ 51 |
Effectively immune to pitting across the natural seawater range |
|
Hastelloy C-276 (N10276) |
16 |
16 |
≈ 68 (≈74 with W) |
Top tier; specified for hot, concentrated chloride brines |
*Monel 400 deserves a footnote because its number is misleading: as a copper–nickel alloy with essentially no chromium or molybdenum, its PREN is near zero, yet it performs admirably in flowing seawater through a different protective mechanism. In stagnant seawater, however, Monel 400 is known to pit and is not recommended for creviced, slow-flow service. PREN ranks pit-initiation resistance within the Cr–Mo passive-film family of alloys; always read it alongside the alloy's own corrosion behavior.
The comparison also understates 625 in one respect worth citing: because PREN was calibrated on iron-based alloys, it cannot credit 625's ~58–61% nickel matrix, which resists the acidic pit chemistry that propagates pits in stainless steels. In field experience, Inconel 625 in natural seawater behaves even better than its PREN advantage over, say, 2507 would suggest - particularly once chlorides combine with H₂S, CO₂, or elevated temperature in oilfield service.
What PREN Thresholds Should Engineers Use for Seawater Service?
The working rules used across offshore and marine engineering are: PREN below ~32 is unsuitable for stagnant seawater; PREN ≥ 40 is the widely accepted threshold for reliable pitting resistance in ambient-temperature seawater including creviced joints; and PREN ≥ 45 provides margin for elevated-temperature or higher-chloride duty. Inconel 625, at ≈51, clears every threshold with room to spare.

These thresholds are rules of thumb distilled from decades of seawater exposure testing and offshore operating experience, not guarantees. Used correctly, they divide the alloy palette into clear bands:
- Below 32: 316L (PREN ≈ 24) fails this test outright - its well-documented pitting in ambient seawater is why it is confined to atmospheric or fully drained marine duties.
- 32–40: 317L, 904L, and duplex 2205 (PREN 33–36) survive smooth, ambient seawater but remain vulnerable at crevices, welds, and warm locations.
- 40–45: super duplex 2507 and super austenitics (PREN ~40–45) are the standard economical choice for ambient seawater valves, pipework, and fasteners where crevices are controlled.
- Above 45: Inconel 625 (≈51) is selected when pitting must be engineered out entirely, when crevices and elevated temperature cannot be avoided, or when chlorides coexist with sour gas (H₂S).
A rigorous specification never stops at the threshold. Temperature, chloride concentration, pH, flow velocity, crevice geometry, weld quality, and microbiologically influenced corrosion (MIC) all shift the real boundary. For design-critical service, the correct practice is to qualify the actual product form by test - ASTM G48 immersion or ASTM G150 electrochemical CPT - on material from the producing mill, with acceptance criteria written into the purchase order. This is exactly how JN Alloy supplies 625 into subsea and chemical duties: certified to ASTM/ASME specs, with G48/G150 and NACE MR0175 compliance documented at shipment.
What Is Inconel 625's Critical Pitting Temperature (CPT)?
Published CPT values for Inconel 625 cluster around 90–110°C depending on test method and product form - so far above the 0–40°C span of natural seawater that pit initiation on smooth 625 surfaces in seawater is not a realistic design concern.
The critical pitting temperature is the lowest temperature at which stable pits initiate on a metal surface under a defined test condition. Above the CPT, pitting becomes possible; below it, the alloy repassivates faster than a pit can stabilize. Two methods dominate: ASTM G48 (immersion in acidified 6% ferric chloride, an aggressive screening test) and ASTM G150 (electrochemical, which returns a precise, reproducible number). Typical reported values compare as follows:
|
Alloy |
PREN (typical) |
CPT, ASTM G150 (typical reported) |
CPT, ASTM G48 (typical reported) |
|
316L |
≈ 24 |
15–30°C |
10–20°C |
|
904L |
≈ 36 |
50–60°C |
40–50°C |
|
Super duplex 2507 |
≈ 43 |
80–95°C |
60–75°C |
|
Inconel 625 |
≈ 51 |
~100°C or above |
85–100°C |
|
Hastelloy C-276 |
≈ 68–74 |
~110°C or above |
95–110°C |
Exact values vary with surface finish, product form, and laboratory, so treat these as engineering ranges rather than constants. The design takeaways do not change: natural seawater - even tropical outfall water at 35–40°C - sits 50–70°C below 625's pit-initiation threshold. The more useful number for designers is the critical crevice temperature (CCT), which is always lower than the CPT because shielded crevice chemistry is more aggressive than a smooth surface. Published CCT values for 625 in ferric chloride testing cluster roughly 25–40°C below its CPT, i.e., in the ~55–75°C band - still comfortably above seawater temperatures, but the reason crevice control matters in hot chloride service.
What Are the Practical Application Limits of Inconel 625 in Seawater and Chloride Environments?
Across the entire natural seawater range (0–40°C), Inconel 625 has no practical pitting limit. Its real limits appear in three places: tight crevices in hot chloride service above roughly 60–70°C, hot concentrated low-pH brines where C-276-class alloys are the correct choice, and welded joints where molybdenum microsegregation or Laves phase can locally lower resistance.
Stated as an engineer would use them, the limits are:
- Pitting - no practical limit: pit initiation on smooth, properly annealed 625 surfaces is not a credible failure mode in natural seawater at any temperature the ocean reaches. Design confidence here is effectively total.
- Crevice corrosion - the real limit: crevices under gaskets, flange faces, deposits, and fouling are the limiting geometry. In hot chloride-bearing process streams (not ambient seawater), attack becomes possible above roughly 60–70°C; specify crevice-tight joint design and smooth finishes.
- Welds - manageable: weld metal can segregate molybdenum and form Nb-rich Laves phase, locally diluting pitting resistance. Qualified welding procedures (with 625 or 625 filler), controlled heat input, and post-weld solution anneal where practical restore the margin.
- Chemistry limits: hot, concentrated brines with low pH above ~100°C - acid-chloride scrubbers, certain FGD liquors - are C-276/C-22 territory; 625 is good but not the optimum.
- Economics - the honest limit: 625 carries a cost premium over super duplex. Where ambient seawater, controlled crevices, and no sour service
apply, 2507 often wins the economic case; 625 wins when its combination of top-tier chloride resistance, strength, H₂S tolerance, and weld-overlay capability is required in one alloy.
SCC - an advantage, not a limit: 625 is essentially immune to the chloride stress-corrosion cracking (Cl-SCC) that cracks austenitic stainless steels above ~50–60°C, a decisive advantage in hot chloride vapors and splash zones.
Where Is Inconel 625 Actually Used in Seawater and Marine Service?
Inconel 625 is the workhorse nickel alloy wherever chloride pitting resistance and high strength must coexist: subsea oil and gas hardware, weld overlay cladding on risers and pipeline components, seawater pump shafts and impellers, heat-exchanger and valve trim components, and marine fasteners and wireline equipment.

Subsea oil & gas: 625 weld overlay on carbon-steel riser joints, flowline spools, and subsea valves combines a corrosion-proof cladding with structural steel economy - the single largest marine use of the alloy. Weldability is itself a 625 superpower: it is the go-to filler metal (ERNiCrMo-3) for welding 625, C-276, 825, and dissimilar joints.
Seawater pumps and shafts: seawater lift pumps, injection pumps, and shafting exploit 625's combination of chloride immunity, cavitation resistance, and high shaft strength (annealed UTS roughly 830–1,000 MPa, well above C-276).
Sour + chloride wells: NACE MR0175/ISO 15156 lists 625 for sour service, so it is a default choice where reservoir chlorides, H₂S, and CO₂ occur together - a combination that disqualifies most stainless steels.
Marine exhaust and scrubbers: exposure bellows, exhaust components, and scrubber internals in hot, chloride-laden gas streams, where Cl-SCC rules out 300-series stainless.
Desalination and FGD: high-temperature sections of thermal desalination and flue gas desulfurization (FGD) systems, and seawater-cooled heat exchanger components in chemical and LNG plants.
What Standards and Tests Govern Inconel 625 in Chloride Service?
Product chemistry and form fall under ASTM B443 (plate/sheet/strip), B444 (tube), and B446 (bar), with ASME SB equivalents for code work; chloride performance is qualified by ASTM G48 and ASTM G150 testing; sour service is governed by NACE MR0175/ISO 15156; and offshore materials selection is guided by ISO 21457.
|
Standard |
What it governs |
Why it matters for chloride service |
|
ASTM B443 / ASME SB-443 |
Chemistry, mechanical properties of 625 plate, sheet, strip |
Fixes the Cr/Mo window that guarantees PREN ≥ ~46 |
|
ASTM B444 / B446 |
625 tube and bar |
Product forms for pipework, shafts, fasteners |
|
ASTM G48 (Methods A–F) |
Ferric-chloride immersion pitting/crevice screening |
Classic acceptance test; specify method and temperature in POs |
|
ASTM G150 |
Electrochemical CPT measurement |
Precise pit-initiation temperature for design margins |
|
NACE MR0175 / ISO 15156 |
Materials for H₂S-containing environments |
Qualifies 625 where chlorides and sour gas coexist |
|
ISO 21457 |
Offshore materials selection guidance |
Framework for seawater system alloy selection |
|
AWS A5.14 (ERNiCrMo-3) |
625 welding filler metal |
Ensures weld metal matches base-metal chloride resistance |
Procurement best practice: require mill test certificates reporting actual Cr and Mo (so the delivered PREN can be verified from the cert), plus G48 Method A at a stated temperature and NACE MR0175 compliance where applicable. A PREN computed from the actual certified chemistry - not the spec range - is the number your QA file should contain.
Inconel 625 vs. the Alternatives: How Should You Choose for Chloride Service?
Choose Inconel 625 when you need top-tier chloride resistance combined with high strength, sour-service capability, and weldability as a filler or overlay, all in one alloy. Choose super duplex 2507 when ambient seawater performance with controlled crevices is enough and cost dominates. Choose Hastelloy C-276 for hot, concentrated, low-pH chloride brines.
|
Service condition |
Recommended alloy |
Rationale |
|
Ambient seawater, smooth surfaces, budget-driven |
Super duplex 2507 / 904L |
PREN 36–43 adequate; far lower cost per kg |
|
Ambient seawater with crevices, fouling, or MIC risk |
Inconel 625 |
Crevice margin PREN ≈ 51 buys; no pit initiation observed |
|
Seawater + H₂S/CO₂ (sour) |
Inconel 625 |
NACE MR0175 listed; stainless grades mostly excluded |
|
Hot concentrated chloride brine, low pH, >100°C |
Hastelloy C-276 / C-22 |
PREN 68+ and W-bearing film chemistry |
|
Weld overlay / filler for dissimilar joints |
Inconel 625 (ERNiCrMo-3) |
Industry-standard cladding and filler alloy |
|
Flowing clean seawater, cost-critical |
Monel 400 or CuNi 90/10 |
Adequate in moving seawater at lower cost - avoid stagnant service |
One closing caution for the specification writer: never compare alloys on PREN alone across alloy families without reading the footnotes. PREN ranks initiation resistance; it does not price the nickel matrix, crevice geometry, weld condition, or cracking resistance - and those are precisely the dimensions on which Inconel 625 usually wins the argument.
Frequently Asked Questions
Approximately 51 on a nominal chemistry - and between 47 and 56 across the full ASTM B443 composition window (PREN = %Cr + 3.3 × %Mo + 16 × %N, with 21.5% Cr and 9% Mo typical).
Is a PREN of 51 good enough for seawater?
Yes, with a wide margin. The widely used acceptance threshold for reliable ambient-temperature seawater service, including crevices, is PREN ≥ 40; Inconel 625 clears it by roughly 11 points.
Why is niobium not included in the PREN calculation?
Niobium does not participate in the chromium–molybdenum passive-film chemistry that PREN measures. In 625 it is added for solid-solution strengthening and weldability, not pitting resistance.
Can Inconel 625 pit in seawater?
On smooth, properly annealed surfaces at natural seawater temperatures (0–40°C), pit initiation is not a realistic failure mode. Attack becomes conceivable only in tight crevices in hot chloride service, typically above about 60–70°C.
What is the critical pitting temperature (CPT) of Inconel 625?
Published values cluster around 90–110°C depending on test method (ASTM G150 electrochemical values typically at or above ~100°C; ASTM G48 immersion values roughly 85–100°C) - far above seawater temperatures.
How does Inconel 625 compare with 316L in seawater?
316L (PREN ≈ 24, CPT ≈ 15–30°C) pits and fails by perforation in ambient seawater; Inconel 625 (PREN ≈ 51, CPT ≈ 100°C) is effectively immune across the same range. They are not interchangeable in marine immersion service.
Inconel 625 or Hastelloy C-276 for chloride service - which is better?
Both are top-tier. C-276 (PREN ≈ 68–74 with tungsten) is superior in hot, concentrated, low-pH chloride brines; 625 offers higher strength, is the standard weld filler/overlay alloy, and is more economical where its resistance suffices.
Is Monel 400 better than Inconel 625 in seawater?
No - just different. Monel 400 excels in fast-flowing seawater through a copper-alloy mechanism but is known to pit in stagnant seawater and has a near-zero PREN. Inconel 625 resists pitting in both flowing and stagnant conditions.
Does welding reduce Inconel 625's pitting resistance?
It can, slightly, through molybdenum microsegregation and Laves-phase formation in the weld metal. Qualified procedures using matching ERNiCrMo-3 filler, controlled heat input, and solution annealing where practical keep the loss negligible.
What chloride concentration can Inconel 625 tolerate?
Natural seawater (~19,000–20,000 mg/L chloride) indefinitely at ambient temperature, and concentrated brines at moderate temperatures. The practical limits are set by temperature, pH, and crevice geometry rather than chloride concentration itself.
Is Inconel 625 resistant to chloride stress corrosion cracking?
Yes. Its nickel-rich, face-centered-cubic matrix is essentially immune to the transgranular chloride SCC that cracks austenitic stainless steels above roughly 50–60°C - a decisive advantage in hot chloride vapors and splash zones.
Does PREN predict crevice corrosion?
Not directly. Crevice corrosion initiates at lower temperatures than pitting; use the critical crevice temperature (CCT) instead. For 625, published CCT values are roughly 25–40°C below its CPT, i.e., about 55–75°C in ferric chloride tests.
What is the maximum seawater temperature for Inconel 625?
There is no practical pitting limit at natural seawater temperatures (even 40°C tropical water is ~60°C below 625's CPT). For hot chloride process streams, design against crevice attack above about 60–70°C.
Does Inconel 625 require cathodic protection in seawater?
Not for its own pitting resistance. Cathodic protection is sometimes applied system-wide, or to protect coupled carbon steel, but 625 hardware does not need it to resist seawater.
How is PREN calculated for duplex and super austenitic stainless steels?
With the same formula - %Cr + 3.3 × %Mo + 16 × %N - but nitrogen is a deliberate alloying addition in those grades (e.g., ~0.28% N in 2507 adds over 4 PREN points), whereas in 625 it is a negligible trace.
Which test verifies chloride pitting resistance - ASTM G48 or ASTM G150?
G48 (ferric chloride immersion) is the fast screening and acceptance test; G150 (electrochemical) delivers the precise critical pitting temperature used for design margins. Rigorous specifications use both.
Is Inconel 625 compliant with NACE MR0175 for sour service?
Yes - Inconel 625 is listed in NACE MR0175/ISO 15156 for use in H₂S-containing environments (in the appropriate conditions of use), which is why it dominates subsea hardware where chlorides and sour gas coexist.

