Why Nozzle Openings Need Reinforcement

A storage tank shell under hydrostatic pressure carries hoop stress — circumferential tension that keeps the cylindrical wall in equilibrium. When a nozzle opening is cut into the shell, the plate that carried that stress is removed. The load does not disappear; it redistributes into the material immediately surrounding the hole, creating a local stress concentration at the nozzle edge.

API 650 §5.7 addresses this through the replacement area method: the cross-sectional area of metal removed by the opening must be replaced by an equal area of metal located within a defined reinforcement zone around the nozzle. The principle is straightforward — any excess metal already present in the shell or nozzle neck can count toward this requirement, and if it is insufficient, a reinforcing pad (repad) must be added.

The check applies to all nozzles, manways, and other shell penetrations. It does not apply to openings in the roof or bottom that carry no shell hoop stress, though those components have their own design requirements. For every nozzle in the shell, the three-step procedure below must be completed before the nozzle can be considered adequately reinforced.

Step 1: Calculate the Area Removed

The area removed by the nozzle opening is the plan area of metal cut from the shell plate. API 650 §5.7 defines this as:

Aremoved = d × (treq − CA)

where d is the finished inside diameter of the nozzle opening (the hole in the shell, not the nozzle pipe OD), treq is the required shell thickness at the nozzle location calculated by the design formula (one-foot or variable-point method), and CA is the corrosion allowance applied to the shell.

The subtraction of CA from treq reflects that the design thickness already includes corrosion allowance — the net structural thickness that carries load is treq − CA. Using the full required thickness without subtracting CA overstates the area removed and is overly conservative, but the error in the opposite direction — using the ordered (as-built) shell thickness instead of the required thickness for treq — is far more common and much more dangerous.

The most common error in this step: substituting tordered (the plate thickness actually purchased, which is always ≥ treq) for treq in the formula. This makes the area removed appear smaller, which in turn makes the available reinforcement look adequate when it may not be. Always use the design-required thickness — the output of the thickness formula for that shell course — not the ordered plate thickness.

Aₐₑₘₒ𝙛𝙞𝙝 = d × (tₑ𝚊ₕ − CA) d = finished inside diameter of nozzle opening (mm) tₑ𝚊ₕ = required shell thickness at nozzle location (design formula result) CA = corrosion allowance applied to shell plate Aₐ𝘼ₐₐₐₐₐₐₐₐₐ = Aₐ𝘴ₐ𝘺ₐₐ + Aₐₐₐ𝘻𝘻ₐₐ + Aₐ𝘱ₐ𝘲 ≥ Aₐₑₘₒ𝙛𝙞𝙝
The replacement area balance: total available area from shell excess, nozzle neck, and repad must equal or exceed the area removed by the opening.

Step 2: Identify Available Reinforcing Area

Before a repad is considered, API 650 §5.7 counts two sources of area that are already present in the assembly. Both must be within the reinforcement zone (see Section 5 below) to count.

Area from Shell Excess Thickness

If the shell plate ordered is thicker than the required thickness, the excess metal on either side of the nozzle provides reinforcement area without any additional material. This area is:

Ashell = (tordered − treq) × d

This is the excess thickness multiplied by the opening diameter. For a shell course where the ordered plate is, for example, 10 mm and the required thickness is 8 mm, every millimetre of nozzle diameter translates to 2 mm² of free reinforcement. On thick lower shell courses with small nozzles, this excess area alone can be sufficient to meet the entire reinforcement requirement — no repad is needed.

Note that this calculation uses the ordered thickness for the available area but the required thickness for the removed area. This asymmetry is correct and intentional: tordered is what you actually have, while treq is the structural minimum that must be maintained around the opening.

Area from Nozzle Neck

For set-on nozzles (nozzle welded to the outside surface of the shell plate), the nozzle neck wall that projects outward from the shell face and the portion that projects inward into the tank both contribute available area. However, only the portions within the vertical reinforcement zone count — specifically, the wall area within a distance of 2.5 × the nozzle neck thickness (tn) measured from each face of the shell plate.

For set-in (flush) nozzles, where the nozzle is inserted into the shell opening and the nozzle OD is flush with or inside the shell plate, the available area contribution differs because the nozzle neck does not project beyond the shell face in the same way. The calculation must correctly account for the nozzle type; treating a set-in nozzle as a set-on nozzle overestimates the available neck area and can result in a non-compliant design that passes on paper.

The nozzle neck area used in the calculation must also account for corrosion allowance. The nozzle wall thickness used is the net available wall thickness after corrosion allowance (tn − CA), not the nominal wall thickness of the nozzle pipe as ordered.

Step 3: When Is a Reinforcing Pad Required?

A reinforcing pad is required only when the combined area from shell excess and nozzle neck falls short of the area removed:

Apad required = Aremoved − Ashell − Anozzle neck

The repad is a flat annular plate welded to the shell around the nozzle. Its contributing area is:

Apad = (Wpad − Dnozzle OD / 2) × tpad

where Wpad is the outer radius of the repad from the nozzle centreline, Dnozzle OD/2 is the nozzle outside radius (the inner edge of the repad), and tpad is the repad plate thickness. API 650 limits the repad width to a maximum of 2 × the nozzle OD, measured from the nozzle centreline. Area contributed by a repad extending beyond this limit does not count, regardless of how thick the repad is.

When Does the Shell Self-Reinforce?

For small nozzles (inside diameter roughly 200 mm or less) placed on thick lower shell courses, it is common for the shell excess area alone to satisfy the entire reinforcement requirement. Engineers who default to specifying a repad on every nozzle without performing the reinforcement check are often adding unnecessary cost and weld joints. Each repad adds two circumferential fillet welds, a telltale hole requirement, and a stress concentration at the pad-to-shell interface. If the shell self-reinforces, none of that is needed.

The check is simple: if Ashell ≥ Aremoved, no repad is required. This should always be verified before specifying a repad, particularly for nozzles on lower shell courses where plate thickness is greatest.

Limits of the Reinforcement Zone

API 650 §5.7.3 defines a rectangular reinforcement zone centred on the nozzle opening. Only metal within this zone can be counted as available reinforcing area. The zone boundaries are:

  • Horizontal (circumferential) limit: d from the edge of the opening on each side — a total horizontal extent of 3d centred on the nozzle (d on each side of the opening, plus d for the opening itself).
  • Vertical (meridional) limit: 2.5 × tshell above and below the centreline of the opening — specifically, 2.5 times the shell plate thickness on each side.

The reinforcement zone has hard limits — horizontal d each side of the opening, vertical 2.5t above and below. Any metal outside this box, no matter how thick, contributes nothing to the reinforcement calculation.

The vertical limit is particularly significant for large-diameter nozzles and manways: as d increases, the horizontal extent of the zone grows proportionally, but the vertical extent is fixed by the shell thickness. For a 16 mm shell plate, the reinforcement zone extends only 40 mm above and below the shell mid-plane. Shell area further from the opening — even on the same shell course — does not count.

A common error is counting repad area that extends beyond the horizontal limit. If the repad outer diameter exceeds d on each side of the nozzle edge (total repad outer extent > nozzle OD + 2d), the excess repad area must be excluded from the calculation even though it is physically welded in place.

Practical Tips and Common Errors

After the three-step procedure, several recurring calculation errors are worth addressing explicitly:

  • Using ordered shell thickness for treq in the removed area formula. This is the most frequent compliance error and it always works in the non-conservative direction, making the reinforcement appear more available than it is. Required thickness must come from the design calculation for that shell course.
  • Counting uncorroded nozzle neck thickness. API 650 requires that the nozzle neck wall used for available area be the corroded wall — tnozzle − CA. Using the nominal pipe wall thickness as-ordered overstates the available area over the design life of the tank.
  • Counting repad area outside the reinforcement zone. If the repad is wider than d each side from the nozzle edge, clip the area at the zone boundary. Software that uses the full repad width without checking the zone limit will overstate available area for large repads.
  • Set-in versus set-on nozzle geometry. Flush (set-in) nozzles contribute nozzle neck area differently because no neck protrudes outside the shell surface. Using a set-on formula for a set-in nozzle is non-compliant and results in overstated available area.
  • Large manways and insert plates. For nozzles with inside diameter ≥ 600 mm, the area removed is large and the repad width limit (2 × nozzle OD measured from centreline) typically cannot provide sufficient repad area on its own. In these cases, a thicker insert plate — a locally thickened shell plate region around the nozzle — is the correct solution. A standard repad on a 600 mm manway will almost certainly be insufficient without the shell also being locally thickened.
  • Nozzle placement near shell course welds. API 650 §5.7.2 restricts how close nozzle edges can be to shell-to-shell welds. A nozzle placed too close to a horizontal seam can disqualify the shell excess area in the adjacent course from counting, since that area falls outside the reinforcement zone for the course being reinforced.

TankCode 650 runs the full replacement area check for every nozzle — computing area removed from the correct required shell thickness, adding shell excess and nozzle neck contributions within the zone limits, and flagging when a repad is required with the minimum pad dimensions needed. The shell thickness module feeds the required thickness directly into the nozzle check, eliminating the manual transcription error that drives most compliance failures. For corrosion allowance strategy, see our article on CA selection under API 650.

Related reading: Continue with Corrosion Allowance Strategy, Shell Course Thickness Design, and Bottom Plate and Annular Ring to keep the full API 650 design workflow connected.

Check nozzle reinforcement in seconds

TankCode 650 runs the replacement area check for every nozzle — shell excess, nozzle neck, and repad — with corrosion allowance applied correctly.

Launch App →