3.2 Pitting Evaluation & Corroded Area Limits

Key Takeaways

  • Under API 510 Section 7.4.3, widely scattered pits are acceptable if the remaining wall thickness at the bottom of every pit is at least 50% of the required thickness (t_pit_rem ≥ 0.5 * t_required + CA_future).

  • The cumulative linear dimension of pitting along any straight 8.0-inch (200 mm) line drawn in any direction must not exceed 2.0 inches (50 mm), representing a 25% linear limit.

  • The cumulative surface area of all pits within any 100 square inch (650 cm²) area of the vessel wall must not exceed 7.0 square inches (45 cm²), representing a 7% surface area limit.

  • Pitting occurring directly within weld seams or heat-affected zones (HAZs) cannot be evaluated under widely scattered pitting rules due to severe stress intensification and cracking susceptibility.

  • Linear grooving, canal corrosion, and flow-induced erosion cannot be evaluated as widely scattered pitting and must be treated as local thin areas (LTAs) or notch-like flaws under API 579.

Last updated: August 2026

Pitting Evaluation & Corroded Area Limits

Pitting corrosion is an extremely localized degradation mechanism characterized by cavities, pinholes, or localized depressions on the metal surface. Unlike uniform corrosion, which thins large surface areas at a steady, predictable rate, pitting can penetrate deep into a vessel wall while consuming very little overall metal volume. In refining, chemical processing, and upstream production, pitting frequently develops under insulation (CUI), beneath deposits or sludge (under-deposit corrosion), from stagnant halide solutions (chlorides), or via microbiological activity (MIC).

Because pits act as localized geometric stress risers, the inspector must evaluate whether the pitting can be classified as widely scattered pitting under API 510 Section 7.4.3 or whether it threatens the pressure-retaining integrity of the vessel.


1. API 510 Section 7.4.3 Three-Part Acceptance Criteria

API 510 provides a straightforward, highly tested three-part screening standard for evaluating widely scattered pitting. To be accepted without requiring pressure derating or weld repair, the pitted area must satisfy all three of the following criteria simultaneously:

+-----------------------------------------------------------------------------------------+
|                   API 510 WIDELY SCATTERED PITTING ACCEPTANCE CRITERIA                  |
|                                                                                         |
|   CRITERION 1: REMAINING THICKNESS BELOW PIT BOTTOM (DEPTH LIMIT)                       |
|   - Remaining wall thickness beneath ANY pit must be AT LEAST 50% of required thickness |
|   - Formula: t_pit_rem ≥ (0.50 * t_required) + CA_future                                |
|                                                                                         |
|   CRITERION 2: LINEAR PITTING LIMIT (8-INCH LINE TEST)                                  |
|   - Total sum of pit lengths along ANY straight 8-inch (200 mm) line must NOT exceed    |
|     2.0 inches (50 mm) in ANY orientation                                               |
|   - Formula: Σ L_pit ≤ 2.0 in. (along any 8.0 in. line)  --> [Max 25% linear]           |
|                                                                                         |
|   CRITERION 3: SURFACE AREA LIMIT (100 SQUARE INCH GRID TEST)                           |
|   - Total cumulative area of all pits in ANY 100 sq. in. (650 cm²) area must NOT exceed |
|     7.0 square inches (45 cm²)                                                          |
|   - Formula: Σ A_pit ≤ 7.0 sq. in. (in any 100 sq. in. window) --> [Max 7% area]        |
+-----------------------------------------------------------------------------------------+

Criterion 1: Maximum Pit Depth / Remaining Wall Thickness

The remaining thickness of the vessel wall at the bottom of the deepest pit (tpit, remt_{\text{pit, rem}}) cannot be less than one-half (50%50\%) of the minimum required wall thickness (trequiredt_{\text{required}}), plus the corrosion allowance (CACA) required until the next scheduled inspection:

tpit, rem=tactual−dpit≥0.50⋅trequired+CAfuturet_{\text{pit, rem}} = t_{\text{actual}} - d_{\text{pit}} \ge 0.50 \cdot t_{\text{required}} + CA_{\text{future}}

Where:

  • tactualt_{\text{actual}} = actual thickness of the unpitted surrounding plate (in.)
  • dpitd_{\text{pit}} = depth of the deepest pit measured with a pit gauge or depth micrometer (in.)
  • trequiredt_{\text{required}} = minimum required shell/head thickness calculated per ASME code formulas (in.)
  • CAfutureCA_{\text{future}} = estimated metal loss prior to the next inspection (CR×years until next inspectionCR \times \text{years until next inspection})

Criterion 2: Linear Pitting Limit (The 8-Inch Rule)

An inspector draws a straight line measuring 8.0 in.8.0\text{ in.} (200 mm200\text{ mm}) in length in any direction across the pitted region. The sum of the dimensions of all pits intersected by this 8-inch line must not exceed 2.0 in.2.0\text{ in.} (50 mm50\text{ mm}):

∑i=1nLi≤2.0 in.(along any 8.0 in. line)\sum_{i=1}^{n} L_i \le 2.0\text{ in.} \quad (\text{along any } 8.0\text{ in. line})

This represents a maximum linear density of 25%25\%. If pits coalesce or form a continuous linear chain exceeding 2.0 in.2.0\text{ in.}, stress concentration shifts from 3D localized hemispherical dispersion to a 2D planar notch, which significantly increases crack initiation risk.

Criterion 3: Total Area Limit (The 100 Square Inch Rule)

In any 100 sq. in.100\text{ sq. in.} (650 cm2650\text{ cm}^2) area of the shell or head (e.g., a 10 in.×10 in.10\text{ in.} \times 10\text{ in.} square or an 11.28 in.11.28\text{ in.} diameter circle), the cumulative surface area of all pits must not exceed 7.0 sq. in.7.0\text{ sq. in.} (45 cm245\text{ cm}^2):

∑i=1nAi≤7.0 sq. in.(in any 100 sq. in. region)\sum_{i=1}^{n} A_i \le 7.0\text{ sq. in.} \quad (\text{in any } 100\text{ sq. in. region})

This represents a maximum surface area density of 7%7\%. If more than 7%7\% of the surface is pitted, the damage is no longer considered "widely scattered" and must instead be evaluated as general metal loss or a locally thinned area (LTA).


2. Pitting vs. Grooving vs. Localized Erosion

Inspectors must distinguish between different forms of localized metal loss because the code rules governing each mechanism differ substantially.

Damage ClassificationMorphological DescriptionTypical CausesCode Evaluation Standard
Widely Scattered PittingIsolated, spherical, or conical depressions dispersed across base metalCUI, stagnant halides, low-flow oxygen attackAPI 510 Section 7.4.3 (50% depth, 2 in./8 in. line, 7 sq. in./100 sq. in.)
Linear Grooving / Canal CorrosionContinuous, elongated, narrow channels running along flow paths or weld toesAcid condensate run-down, vapor-line reflux, boiler wash-downAPI 510 Section 7.4.2 (LTA) or API 579-1 Part 5 / Part 9 (Crack-like notch)
Localized Erosion / ImpingementSmooth, scalloped, horseshoe-shaped thinning opposite nozzles or inlet bafflesHigh-velocity slurry, droplet impingement, turbulent flashingAPI 510 Section 7.4.2 (Corrosion Averaging) or API 579-1 Part 4/5
Weld Seam PittingPitting concentrated directly along weld cap, root, or HAZ boundaryGalvanic difference between weld metal and base plate, preferential HAZ attackAPI 579-1 Part 6 / Engineering Review (Cannot use basic 7.4.3 base metal rules)
+-----------------------------------------------------------------------------------------+
|                         DAMAGE MORPHOLOGY VISUAL COMPARISON                             |
|                                                                                         |
|   [WIDELY SCATTERED PITTING]            [LINEAR GROOVING]         [LOCALIZED EROSION]   |
|   +-----------------------+           +-----------------------+   +-------------------+ |
|   |   ( )       ( )       |           |      |   |            |   |   ~~~~~~~         | |
|   |         ( )       ( ) |           |      |   |            |   |  ( ~~~~~~~ )      | |
|   |   ( )          ( )    |           |      |   |            |   |   ( ~~~~~ )       | |
|   |       ( )    ( )      |           |      |   |            |   |     ~~~~          | |
|   +-----------------------+           +-----------------------+   +-------------------+ |
|   - 3D isolated cavities              - 2D stress concentration   - Smooth scallops   | |
|   - Governed by 7.4.3                 - Governed by LTA / FFS     - Governed by LTA   | |
+-----------------------------------------------------------------------------------------+

3. Pitting in Weld Seams vs. Base Metal

Pitting in or adjacent to weld seams presents severe structural risks that do not apply to base metal pitting:

  1. High Stress Concentration (KtK_t): Welds already contain residual tensile stresses from solidification and shrinkage (unless fully post-weld heat treated). A pit in the weld creates a compound stress riser.
  2. Microstructural Vulnerability in the HAZ: The heat-affected zone often possesses coarse grain structures or untempered martensite, making it susceptible to environmental cracking mechanisms (e.g., wet H2S\text{H}_2\text{S} sulfide stress cracking, caustic cracking, or chloride stress corrosion cracking) that nucleate at pit roots.
  3. Volumetric Weld Flaws: Pitting that intersects subsurface weld porosity or lack of fusion creates a direct leakage path or crack initiation site.

Caution

Critical Inspection Rule: The widely scattered pitting rules in API 510 Section 7.4.3 apply strictly to base metal and general vessel surfaces. If pitting is concentrated along a longitudinal or circumferential weld seam, the inspector must not use the 50% depth rule; instead, the weld must be evaluated by a pressure vessel engineer using API 579-1 / ASME FFS-1 Part 6 or repaired in accordance with API 510 Section 8.


4. Detailed Step-by-Step Pitting Evaluation Example

Let us evaluate an in-service vessel shell to determine if an area of corrosion satisfies API 510 pitting limits.

Vessel Data:

  • Nominal Shell Thickness (tnomt_{\text{nom}}): 0.750 in.0.750\text{ in.}
  • Calculated Required Thickness (trequiredt_{\text{required}}): 0.500 in.0.500\text{ in.}
  • Future Corrosion Allowance (CAfutureCA_{\text{future}}): 0.050 in.0.050\text{ in.}
  • Current Unpitted Base Plate Thickness (tactualt_{\text{actual}}): 0.700 in.0.700\text{ in.}

Inspection Findings in a 10 in.×10 in.10\text{ in.} \times 10\text{ in.} Area (100 sq. in.100\text{ sq. in.}):

  • Pit depths measured with a needle-point depth gauge range from 0.150 in.0.150\text{ in.} to 0.380 in.0.380\text{ in.}
  • The deepest pit measures dpit, max=0.380 in.d_{\text{pit, max}} = 0.380\text{ in.}
  • The total sum of pit diameters along the worst-case 8-inch straight line is 1.65 in.1.65\text{ in.}
  • The total cumulative surface area of all pits in the 100 sq. in.100\text{ sq. in.} window is 5.20 sq. in.5.20\text{ sq. in.}

Evaluation Step 1: Check Remaining Thickness Below Deepest Pit

Calculate actual remaining thickness below the pit bottom:

tpit, rem=tactual−dpit, max=0.700 in.−0.380 in.=0.320 in.t_{\text{pit, rem}} = t_{\text{actual}} - d_{\text{pit, max}} = 0.700\text{ in.} - 0.380\text{ in.} = \mathbf{0.320\text{ in.}}

Calculate the minimum allowable thickness below the pit under API 510 Section 7.4.3:

tpit, limit=(0.50⋅trequired)+CAfuture=(0.50⋅0.500 in.)+0.050 in.=0.250+0.050=0.300 in.t_{\text{pit, limit}} = (0.50 \cdot t_{\text{required}}) + CA_{\text{future}} = (0.50 \cdot 0.500\text{ in.}) + 0.050\text{ in.} = 0.250 + 0.050 = \mathbf{0.300\text{ in.}}

Depth Check Result:

tpit, rem(0.320 in.)≥tpit, limit(0.300 in.)→PASSEDt_{\text{pit, rem}} (0.320\text{ in.}) \ge t_{\text{pit, limit}} (0.300\text{ in.}) \quad \rightarrow \quad \mathbf{PASSED}

Evaluation Step 2: Check Linear Pitting Limit Along 8-Inch Line

  • Measured cumulative pit length along worst-case line: Lpits=1.65 in.L_{\text{pits}} = 1.65\text{ in.}
  • API 510 maximum allowable limit along an 8-inch line: Lallowable=2.00 in.L_{\text{allowable}} = 2.00\text{ in.}

Linear Check Result:

1.65 in.≤2.00 in.→PASSED1.65\text{ in.} \le 2.00\text{ in.} \quad \rightarrow \quad \mathbf{PASSED}

Evaluation Step 3: Check Cumulative Surface Area in 100 sq. in.

  • Measured cumulative pit surface area: Apits=5.20 sq. in.A_{\text{pits}} = 5.20\text{ sq. in.}
  • API 510 maximum allowable area in 100 sq. in.100\text{ sq. in.}: Aallowable=7.00 sq. in.A_{\text{allowable}} = 7.00\text{ sq. in.}

Area Check Result:

5.20 sq. in.≤7.00 sq. in.→PASSED5.20\text{ sq. in.} \le 7.00\text{ sq. in.} \quad \rightarrow \quad \mathbf{PASSED}

Final Determination:

Because the pitted area satisfies all three API 510 criteria, the shell is acceptable for continued operation at full design MAWP without requiring immediate repair or derating.


5. Common Exam Pitfalls & Code Traps

Exam Scenario / QuestionCommon TrapCorrect API 510 Rule
Depth Limit BaseCalculating 50% of the nominal thicknessPit depth is calculated against 50% of the minimum required thickness (trequiredt_{\text{required}}), not nominal.
Forgetting Future CALeaving out the corrosion allowance in the depth checkThe remaining thickness must be ≥0.5treq+CAfuture\ge 0.5 t_{\text{req}} + \mathbf{CA_{\text{future}}}.
8-Inch Line vs 100 Sq. In.Mixing up 2 inches in 8 inches with 7 sq. in. in 100 sq. in.Linear limit =2.0 in.= 2.0\text{ in.} per 8.0 in.8.0\text{ in.} (25%25\%); Area limit =7.0 sq. in.= 7.0\text{ sq. in.} per 100 sq. in.100\text{ sq. in.} (7%7\%).
Grooving in WeldsApplying pitting rules to longitudinal groovingLinear grooving is a planar notch that must be evaluated under LTA / FFS rules, never scattered pitting rules.
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API 510 Widely Scattered Pitting Evaluation Process
Test Your Knowledge

A cylindrical vessel has a minimum required shell thickness of 0.600 inches and a future corrosion allowance of 0.050 inches. What is the absolute minimum acceptable remaining wall thickness permitted below the bottom of any widely scattered pit under API 510 Section 7.4.3?

A

0.300 inches

B

0.650 inches

C

0.250 inches

D

0.350 inches

Test Your Knowledge

When evaluating widely scattered pitting on a pressure vessel shell under API 510, what is the maximum cumulative length of pitting permitted along any straight 8.0-inch line drawn on the shell surface?

A

2.0 inches (50 mm)

B

1.0 inch (25 mm)

C

4.0 inches (100 mm)

D

0.5 inches (12.5 mm)

Test Your Knowledge

During an internal inspection of a 0.500-inch nominal wall vessel, an inspector identifies an area of pitting in the shell base metal. In a 100 square inch evaluation grid, the cumulative surface area of the pits is measured to be 8.5 square inches. How should the inspector evaluate this condition under API 510 Section 7.4.3?

A

Acceptable, because 8.5 square inches is less than the 10.0 square inch (10%) maximum area threshold.

B

Acceptable, provided the remaining wall thickness below all pits exceeds 25% of the nominal thickness.

C

Unacceptable under widely scattered pitting rules, because the cumulative area exceeds the 7.0 square inch maximum limit for a 100 square inch window.

D

Acceptable only if the vessel is operated at a 10% reduction in operating temperature.

Test Your Knowledge

An inspector discovers a continuous, 12-inch-long narrow groove running parallel to the toe of a longitudinal weld on a distillation column. Why is it inappropriate to evaluate this defect using the widely scattered pitting rules of API 510 Section 7.4.3?

A

Because pitting rules apply only to external atmospheric corrosion, not internal process corrosion.

B

Because linear grooving creates a continuous stress-concentrating notch along a welded joint, requiring evaluation as a locally thinned area (LTA) or crack-like flaw under API 579-1 rather than scattered 3D pitting.

C

Because grooving on a distillation column is always acceptable without engineering review if the vessel is insulated.

D

Because API 510 forbids the evaluation of any flaws longer than 6 inches on welded vessels.

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