25 March 2026· 15 min read· Calculator Corrosion Science Stainless Steel Duplex

PREN Calculator — Pitting Resistance Equivalent Number for Stainless Steels and Nickel Alloys

The Pitting Resistance Equivalent Number (PREN) is the primary quantitative tool for ranking the resistance of stainless steels, duplex alloys, and nickel alloys to chloride-induced pitting and crevice corrosion. It converts alloy composition into a single index that engineers use for material selection, service environment qualification, and design specification. This calculator computes PREN, PRENw (including tungsten), and provides critical pitting temperature estimates, service environment ratings, and a side-by-side batch comparison mode for up to eight alloys. A complete graduate-level treatment of pitting corrosion electrochemistry, passive film theory, and the physical basis of each coefficient follows.

Key Takeaways

  • PREN = %Cr + 3.3×%Mo + 16×%N. Each coefficient reflects the relative effectiveness of the element in stabilising the passive film against chloride attack.
  • PRENw = %Cr + 3.3×(%Mo + 0.5×%W) + 16×%N. Required for super duplex and other W-bearing grades (Ferralium 255, SAF 2507W) — standard PREN underestimates pitting resistance without this correction.
  • Seawater ambient service requires PREN ≥ 32–34; warm seawater (>35°C) requires PREN ≥ 40. Grade 316L (PREN ~25) is entirely unsuitable for unprotected seawater immersion.
  • Critical pitting temperature (CPT) correlates approximately with PREN: CPT (°C) ≈ PREN − 20 for austenitic grades in 6% FeCl₃ — a useful screening estimate, not a substitute for ASTM G48 testing.
  • Crevice corrosion temperature is typically 20–30°C lower than the CPT for the same alloy, making crevice geometry the most dangerous scenario for any grade near its service limit.
  • PREN applies to wrought, solution-annealed material. Weld HAZ, sensitised microstructure, sigma phase, and surface contamination (iron contamination, grinding damage) all reduce effective pitting resistance regardless of calculated PREN.

PREN / PRENw Calculator

3 modes: single alloy • grade presets • batch comparison • CPT & CCT estimates

Single Alloy
Grade Presets
Batch Comparison
Required for PRENw. Leave 0 if not present.
Used for PRENMn (duplex research variant)
Please enter at least %Cr to calculate PREN.
PREN scale — pitting resistance service envelope
0102030405060+
Alloy Comparison Table
#AlloyCr%Mo%N%W%PRENPRENwCPT est.Rating
No alloys added. Calculate then click “Add to Comparison”.
Pitting Corrosion Mechanism Bulk solution (neutral/alkaline) O₂ O₂ O₂ O₂ Cl⁻ Cl⁻ Cl⁻ Film breakdown (Cl⁻ attack) Passive film (Cr₂O> + MoO₃) PIT Fe→Fe²⁺+2e⁻ pH ↓ (acid) Cl⁻ ↑ (migrate) O₂ depletion O₂+2H₂O +4e⁻→4OH⁻ Cathodic Cathodic Higher PREN → more robust passive film Cr: forms Cr₂O₃ — primary passive film Mo: enriches film as MoO₃, blocks active sites N: dissolves as NH₄⁺ in pit, raises local pH PREN = %Cr + 3.3×%Mo + 16×%N Anodic Polarisation Curve log Current Density → Potential E (vs ref.) E𝔌𝔬𝔬 Eₚ𝑹𝔬𝑡 Eₚ𝑖𝑡 Eₚ𝑖𝑡 (hi PREN) Eₚ𝑖𝑡 (304L) Eₚ𝑖𝑡 (2507) Eₚ𝑹𝔬𝑡 Active dissolution Passive region (low iₚₐₛₛ) Pitting / transpassive ΔEₚ𝑖𝑡 from ΔPREN Low PREN (304L ~19) High PREN (2507 ~42)
Figure 1. Left: pitting corrosion mechanism at a passive film breakdown site. Chloride ions penetrate the Cr₂O₃-based passive film; inside the developing pit, metal dissolution (Fe → Fe²⁺ + 2e⁻) acidifies the local environment, chloride migrates in for charge neutrality, and oxygen depletion prevents repassivation — a self-sustaining autocatalytic cycle. Mo and N additions to the alloy enrich the passive film and raise the local pit pH, suppressing pit initiation. Right: schematic anodic polarisation curve. Higher PREN shifts the pitting potential Epit to more noble (positive) values, making pitting initiation harder. Eprot is the protection potential below which existing pits repassivate. © metallurgyzone.com

The Physical Basis of the PREN Formula

The PREN formula is empirical — derived by Sedriks, Truman, and others from regression analysis of critical pitting temperature (CPT) data on large numbers of alloy compositions — but each term has a sound physical and electrochemical basis.

Chromium (Coefficient 1.0): The Passive Film Former

Chromium is the foundation of stainless steel corrosion resistance. Above approximately 10.5% Cr, the spontaneous formation of a stable, self-healing Cr₂O₃-rich passive film on the steel surface provides the primary barrier against corrosion. This film is typically 1–3 nm thick and contains both Cr(III) and Cr(VI) species. Increasing Cr content thickens the passive film, increases its Cr/Fe ratio, and raises the pitting potential — but with diminishing returns above about 22–25% Cr. The baseline coefficient of 1.0 means that all other elements are scaled relative to Cr.

Molybdenum (Coefficient 3.3): Passive Film Enrichment

Molybdenum is approximately 3.3 times more effective than Cr per weight percent at improving pitting resistance. The mechanism operates at several levels:

  • Mo enriches in the passive film as MoO₃/MoO₄²⁻ species, filling defect sites (cation vacancies) in the Cr₂O₃ lattice that would otherwise be entry points for Cl⁻ attack.
  • In active pit environments, Mo₄²⁻ ions adsorb competitively with Cl⁻ on the dissolving metal surface, reducing the active dissolution rate.
  • Mo raises the repassivation rate — the ability of the alloy to reform the passive film when it is mechanically or chemically disrupted — which is important for abrasive or erosive environments.

Nitrogen (Coefficient 16): Local pH Buffer and Film Stabiliser

Nitrogen is the most efficient element per weight percent in the PREN formula, with a coefficient of 16. Its mechanisms:

  • Local pH buffering inside pits: As metal cations hydrolyse inside a developing pit (e.g., Cr³⁺ + 3H₂O → Cr(OH)₃ + 3H⁺), the pH drops to 1–3, accelerating dissolution. Nitrogen in the alloy dissolves as NH₄⁺ in the acidic pit environment, consuming H⁺ and raising the local pH, which suppresses the active dissolution rate and favours repassivation.
  • Film stability: N substitutes for O in the passive film lattice, improving its electronic properties and reducing defect density.
  • Austenite stabilisation: In duplex steels, N partitions strongly to austenite, raising the PREN of the austenitic phase towards the PREN of the ferritic phase — critical for achieving a balanced microstructure with uniform corrosion resistance across both phases.

The 16× coefficient reflects both the high molecular efficiency of nitrogen and its very high weight-for-weight effectiveness. In practical terms, adding 0.1% N to a 316L base gives an additional 1.6 PREN — equivalent to adding 0.5% Mo or 1.6% Cr at no additional cost in most EAF steelmaking processes.

PREN Formulas: Standard, PRENw, and PRENMn

Standard PREN (most widely used):
  PREN = %Cr + 3.3×%Mo + 16×%N

PRENw (including tungsten, for W-bearing grades):
  PRENw = %Cr + 3.3×(%Mo + 0.5×%W) + 16×%N
  W coefficient = 0.5 (W is ~half as effective as Mo by weight)
  Required for: SAF 2507, Ferralium 255, Zeron 100, Uranus 65

PRENMn (research variant for lean duplex grades):
  PRENMn = %Cr + 3.3×%Mo + 16×%N − 1.5×%Mn
  (penalises Mn which reduces the N content of austenite by forming MnN)
  Useful for lean duplex 2101 (high Mn) but not widely standardised

PREW (Sedriks, alternative formulation with lower N coefficient):
  PREW = %Cr + 3.3×%Mo + 13×%N
  Less commonly used; prefer PREN (N coefficient=16) for modern alloys

Standard references:
  ISO 10272-3: 2007 (defines PREN for duplex stainless steels)
  ASTM A923 Annex A2: applies PREN ≥ 40 criterion for super duplex
  NORSOK M-001: specifies PREN requirements for North Sea service
PREN Scale — Common Grades 430 (ferritic) 17 304L 19 316L 25 317L 30 LDX 2101 26 2205 duplex 35 904L 35 SAF 2507 42 254 SMO 43 Zeron 100 46 654 SMO 60 Alloy 825 32 Alloy 625 51 C-276 65 25 35 40 Cl⁻ atm. Seawater Hot sea 0 20 40 60 Duplex 2205 — Phase PREN Balance Ferrite α (~50%) Cr: ~25%, Mo: ~3.5% N: ~0.05% PRENα ≈ 37 γ austenite PREN ≈ 33 γ austenite PREN ≈ 33 PREN ≈ 33 Austenite γ (~50%) Cr: ~21%, Mo: ~2.5% N: ~0.25% PRENγ ≈ 33 Alloy 2205 overall PREN ≈ 35 Ferrite PREN ≈ 37 (higher Cr, Mo) Austenite PREN ≈ 33 (higher N compensates) Corrosion initiates at weakest phase (γ) N partitions to γ to balance PREN across phases
Figure 2. Left: PREN scale showing common stainless steel and nickel alloy grades with service threshold lines. Grades below PREN 25 are unsuitable for seawater; PREN 35 is the minimum for ambient seawater immersion; PREN ≥ 40 is required for hot seawater and aggressive process streams. Right: schematic duplex 2205 microstructure showing the PREN balance between ferrite (α, PREN ~37) and austenite (γ, PREN ~33). Molybdenum partitions preferentially to ferrite, nitrogen to austenite — together balancing the PREN across both phases and ensuring the alloy pits at the overall PREN of the weaker phase rather than at the bulk PREN. © metallurgyzone.com

Critical Pitting and Crevice Temperatures

The critical pitting temperature (CPT) is the temperature below which a pit cannot propagate and above which spontaneous pitting occurs in a given test environment. It is a more reliable guide to service temperature limits than PREN alone, because it captures the specific interaction between the alloy composition and the electrolyte chemistry.

Test Methods

  • ASTM G48 Method A (6% FeCl₃ solution, 72 h): The most widely used test. The specimen is exposed to boiling 6% FeCl₃ for 72 hours. The CPT is the lowest 5°C increment temperature at which pitting occurs. The crevice corrosion temperature (CCT) is determined by Method B using a crevice former.
  • ISO 10272-3 (electrochemical CPT): Uses a slow potential scan in a 0.5 M NaCl solution with controlled pH; the CPT is taken as the temperature at which the pitting potential Epit equals the open-circuit potential — i.e., spontaneous pitting occurs.
  • NORSOK M-601 (seawater CPT test): Specific test for offshore oil and gas qualification using natural or synthetic seawater.

CPT and CCT Reference Values

Grade (UNS) PREN CPT (°C) in 6% FeCl₃ CCT (°C) in 6% FeCl₃ Max service Cl⁻ conc. Notes
304L (S30403)18–200–5−10 to −5<200 ppm at 20°CUnsuitable for seawater; coastal atmospheric acceptable
316L (S31603)24–2715–200–5<500 ppm at 20°CSuitable for cooling water; not seawater immersion
317L (S31703)28–3225–305–10<2,000 ppm at 30°CChemical plant mild Cl⁻ streams
904L (N08904)32–3635–4010–15<10,000 ppm at 25°CAcid mine water, phosphoric acid
2205 duplex (S31803)34–3635–4515–22Seawater to 30°CStandard North Sea piping specification
SAF 2507 (S32750)41–43≥5030–35Seawater to 45°COffshore heat exchangers, hypochlorite service
254 SMO (S31254)42–44≥5030–35Seawater heat exchangersFGD systems, bleach plant, desalination
Alloy 625 (N06625)50–54≥85≥60Hot concentrated brinesSubsea umbilicals, deep-water applications
C-276 (N10276)60–70≥102≥85Aggressive mixed acids and brinesWet scrubbers, HCl service
CPT and CCT values from ASTM G48 Method A and B data. CCT is typically 20–30°C lower than CPT. Values from multiple published sources; use actual test data per ASTM G48 or ISO 10272 for project specifications. Max Cl⁻ concentrations are approximate guidelines for uninhibited aqueous service at stated temperature.

PREN for Duplex Stainless Steels: Phase Balance and Per-Phase PREN

For duplex stainless steels, the overall bulk-composition PREN understates the complexity of corrosion performance, because the alloy consists of two phases (austenite γ and ferrite α) with different compositions due to thermodynamic partitioning of alloying elements. The actual corrosion performance is dominated by the phase with the lower PREN, since pitting will initiate in the weaker phase.

Element partitioning in duplex 2205 (typical values from EDS/EPMA measurements):

Element   Bulk    Ferrite (α)   Austenite (γ)   Partition coeff Kᵣᵠ = Xᵠ/Xᵣ
Cr         22%      25%           21%              0.84 (Cr prefers ferrite)
Mo         3.1%     3.5%          2.5%             0.71 (Mo prefers ferrite)
N          0.17%    0.05%         0.25%            5.0  (N strongly prefers austenite)
Ni         5.5%     3.5%          6.8%             1.94 (Ni prefers austenite)

Per-phase PREN:
  PREN(α) = 25 + 3.3×3.5 + 16×0.05 = 25 + 11.6 + 0.8 = 37.4
  PREN(γ) = 21 + 3.3×2.5 + 16×0.25 = 21 + 8.25 + 4.0 = 33.3

Limiting phase: austenite (PREN 33.3 < ferrite PREN 37.4)
Nitrogen is critical: its strong partitioning to austenite raises PREN(γ)
from ~29 (without N) to 33.3 (with 0.17% N) — reducing the inter-phase
PREN imbalance from 12 to 4 PREN units.

This analysis explains why nitrogen is so critical in duplex alloy design — it is the primary element that compensates for the naturally higher Cr and Mo content of ferrite by enriching austenite and raising its PREN towards parity. Modern super duplex specifications (2507, Zeron 100) target very high N content (0.24–0.32%) precisely to minimise this phase PREN imbalance. See the austenitic stainless steel guide for the effect of composition on austenite stability and PREN across the 300-series grades.

Weld HAZ Corrosion and PREN Degradation

A common misapplication of PREN is to assume that the calculated value for the parent metal applies equally to the weld and HAZ. In practice, welding can significantly reduce the effective PREN in the HAZ and weld metal through several mechanisms:

  • Sensitisation (austenitic grades): Cr₃C₆ precipitation in the 450–850°C HAZ band depletes Cr below the ~11% passivity threshold, directly reducing effective PREN in a band adjacent to grain boundaries. Prevention: use L-grade or stabilised (321/347) parent metal; control heat input to minimise time in the sensitisation range. See the HAZ microstructure guide.
  • Sigma phase precipitation (duplex grades): At 600–1,000°C, intermetallic sigma (σ) phase precipitates preferentially at ferrite-austenite boundaries, drawing Cr and Mo from the matrix and reducing local PREN significantly. Prevention: limit heat input to <1.5 kJ/mm; ensure interpass temperature below 150°C; water quench root run if permitted.
  • Nitrogen loss from weld pool: N has high vapour pressure and can be lost from the weld pool if insufficient N₂ is added to the shielding gas. Nitrogen content <0.10% in duplex weld metal is a common cause of austenite fraction imbalance and reduced corrosion performance. NORSOK M-601 specifies 1–3% N₂ in back purge Ar for duplex welds.
  • Iron contamination of surface: Iron particles from carbon steel tools, grinding wheels, or wire brushes embed in the stainless surface and form galvanic pitting cells. This is a fabrication problem rather than a metallurgical one but reduces effective corrosion performance on the surface regardless of PREN.
PREN is a bulk material property of wrought, solution-annealed stainless steel. It does not apply to sensitised microstructure, sigma-containing HAZ, or contaminated surfaces. All PREN-based material selection decisions should specify the condition of supply (solution annealed per ASTM A240/A790) and include weld procedure qualification corrosion testing (ASTM A262, ASTM A923) as part of the scope.

PREN in Design Codes and Standards

  • NORSOK M-001 (Materials Selection for the Norwegian Oil Industry): Specifies minimum PREN for piping, equipment, and structural components in offshore service as a function of chloride concentration and temperature. 2205 (PREN ≥35) is the minimum for uncoated subsea piping; 2507 or 25Cr-W alloys (PREN ≥40) for hot seawater service above 35°C.
  • ISO 15156 / NACE MR0175 (Sour Service): Specifies that stainless steel components in H₂S-containing environments must meet hardness limits (≤22 HRC) and minimum PREN values to resist sulphide stress cracking (SSC) and chloride SCC simultaneously.
  • ASTM A923 Annex: Uses PREN ≥ 40 as the pass/fail criterion for super duplex weld procedure qualification corrosion tests, confirming that sigma-phase-containing weld metal (which fails the PREN criterion from Cr/Mo depletion) is unacceptable.
  • EN 10088 (Stainless Steel — Technical Delivery Conditions): Lists PREN as an informative parameter in the grade tables, allowing material comparison but not specifying minimum PREN requirements for specific applications.

Frequently Asked Questions

What is the PREN formula and what does each coefficient mean?
PREN = %Cr + 3.3×%Mo + 16×%N. Each coefficient reflects the relative effectiveness of the element in stabilising the passive film against chloride attack. Chromium (1.0) is the base passive film former (Cr₂O₃). Molybdenum (3.3) enriches the film as MoO₃/MoO₄²⁻ species and reduces active dissolution at pit sites. Nitrogen (16) dissolves as NH₄⁺ in pit environments, raising local pH and suppressing active dissolution. The coefficients are empirical from regression analysis of critical pitting temperature data on large alloy databases. For alloys containing tungsten, use PRENw = %Cr + 3.3×(%Mo + 0.5×%W) + 16×%N. See the pitting corrosion guide for the electrochemical mechanism of pit initiation and growth.
What is PRENw and when should it be used instead of PREN?
PRENw = %Cr + 3.3×(%Mo + 0.5×%W) + 16×%N includes a tungsten contribution, treating W as half as effective as Mo per weight percent. It should be used for any alloy containing W > 0.2%: SAF 2507 (some heats contain up to 0.5% W), Ferralium 255 (W 0.5–2%), Zeron 100 (W 0.5–1%), Uranus 65, and Alloy 22. Standard PREN would underestimate pitting resistance for these grades by 2–5 PREN units. The W coefficient of 0.5 reflects tungsten’s higher atomic mass versus molybdenum (184 vs 96 g/mol) — on a molar (atomic) basis, W is approximately as effective as Mo, but since PREN uses weight percent, the correction factor is needed.
What PREN value is needed for seawater service?
Ambient temperature seawater (≤25°C, splash and immersion) requires PREN ≥ 32–34 — duplex 2205 (PREN ~35) is the standard specification. For warm seawater (>35°C) or any crevice geometry, PREN ≥ 40 is required — super duplex 2507 (PREN ~42) or 254 SMO (PREN ~43). Grade 316L (PREN ~25) is entirely unsuitable for unprotected seawater immersion and will develop pitting within months of exposure at ambient temperature. For submerged pipeline systems with cathodic protection, lower PREN grades may be acceptable because CP suppresses pitting by lowering the potential below Eprot. NORSOK M-001 provides definitive minimum PREN requirements by application type for North Sea offshore service.
How does the critical pitting temperature (CPT) relate to PREN?
In 6% FeCl₃ solution, CPT correlates approximately with PREN: CPT (°C) ≈ PREN − 20 for austenitic grades. For 316L (PREN ~25): CPT ≈ 5°C. For 2507 (PREN ~42): CPT ≈ 22°C. This correlation is an approximate guide — actual CPT depends on the specific electrolyte, surface condition, and specimen geometry. The 6% FeCl₃ test (ASTM G48) is a very aggressive accelerated test; service CPT in real environments is substantially higher than the test CPT. For design decisions, use CPT from direct ASTM G48 testing, not the PREN-based estimate. See the pitting corrosion article for CPT measurement methodology and interpretation.
Why is crevice corrosion more aggressive than open-surface pitting?
Crevice corrosion initiates at lower temperatures and chloride concentrations than free-surface pitting because the restricted crevice geometry creates ideal electrochemical conditions: oxygen depletion (preventing cathodic repassivation), acidification by metal cation hydrolysis, and chloride concentration by migration for charge neutrality. The critical crevice temperature (CCT) is typically 20–30°C lower than the CPT for the same alloy. For 2205 (CPT ~40°C), CCT is ~15–22°C — meaning crevice corrosion can initiate at ambient temperature in seawater at flange faces, under gaskets, and at bolt holes. This is why offshore specifications often require super duplex (CCT ~30–35°C) where duplex flanges or tubesheet crevices are exposed to seawater. The corrosion mechanisms guide covers crevice electrochemistry in detail.
What is the difference between austenitic, duplex, and super duplex stainless steels in terms of pitting resistance?
Standard austenitic grades (304L, PREN 18–20; 316L, PREN 24–27) provide general corrosion resistance in mild environments but are unsuitable for seawater. Duplex 2205 (PREN 34–36) has a 50/50 ferrite-austenite microstructure providing good pitting resistance for ambient seawater plus much better chloride SCC resistance than austenitic grades — the ferritic phase impedes SCC crack propagation at phase boundaries. Super duplex (SAF 2507, PREN 41–43) and super austenitic (254 SMO, PREN 42–44) meet the PREN ≥ 40 threshold for warm seawater and aggressive process streams. See the austenitic stainless steel guide for the full austenitic grade family.
How does weld heat-affected zone affect pitting corrosion resistance?
The weld HAZ is typically the most corrosion-susceptible zone because of: (1) sensitisation in austenitic grades (450–850°C range precipitates Cr₃C₆, depleting Cr below 11% passivity threshold) — prevented by L-grades or stabilised grades (321/347); (2) sigma phase precipitation in duplex grades at 600–1,000°C (depletes Mo and Cr from matrix, reducing effective PREN) — prevented by low heat input (<1.5 kJ/mm) and controlled interpass temperature; (3) nitrogen loss from duplex weld pool without N₂-enriched shielding gas. ASTM A923 testing and corrosion test per ASTM A262 are mandatory for critical corrosion service welds. See the HAZ microstructure guide for the complete thermal cycle and microstructural development analysis.
Can PREN be used to compare nickel alloys with stainless steels?
PREN was validated for iron-based stainless steels. Applying it to nickel alloys (Alloy 625, C-276, Alloy 59) gives approximately correct rankings for relative comparison but the coefficients have not been formally validated for nickel-matrix alloys. High-Mo nickel alloys produce very high PREN values (C-276 ≈ 65) that broadly correspond to their excellent pitting resistance. However, some nickel alloys contain additional pitting-resistance elements not in PREN (Cu in Alloy 825, W in Alloy 22, Nb in Alloy 625) whose contributions are not fully captured. For nickel alloys, CPT testing per ASTM G48 and published corrosion data from alloy manufacturers are more reliable than calculated PREN for making specific material selection decisions.
What PREN value does seawater desalination plant equipment typically require?
Seawater desalination represents some of the most demanding service environments. In MSF/MED plants with brine temperatures to 130°C and chlorides to 70,000 ppm, even super duplex (PREN ~42) is insufficient — titanium Grade 2 or super austenitic 654 SMO (PREN ~67) is required for hot brine stages. SWRO systems operate at ambient temperature with concentrated seawater; super duplex 2507 and 254 SMO are standard for pressure vessels and piping. Flash evaporator condenser tubes in MSF use titanium for maximum reliability since no stainless grade provides acceptable life in hot brine at 90–130°C. The combination of high temperature, high chloride, and stagnant flow in MSF/MED plants makes CPT testing more reliable than PREN alone for material qualification. See the corrosion mechanisms guide for electrochemical background on pitting and crevice attack in concentrated chloride brines.

Recommended Technical References

Corrosion of Stainless Steels — Sedriks (2nd Ed.)

The standard reference for PREN development, pitting corrosion mechanisms, and corrosion data for all stainless steel and nickel alloy families.

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Duplex Stainless Steels — Gunn

Comprehensive treatment of duplex and super duplex metallurgy, welding, corrosion performance, per-phase PREN, and offshore applications.

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ASM Handbook Vol. 13A — Corrosion: Fundamentals, Testing, and Protection

Definitive reference for pitting and crevice corrosion test methods (ASTM G48, G61), critical temperatures, and PREN evaluation methodology.

View on Amazon

Stainless Steel — The Role of Molybdenum — Lula (AISI)

Classic AISI monograph on Mo’s passive film role and the derivation of the 3.3×Mo coefficient in the PREN formula.

View on Amazon

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