Pressure Vessel Wall Thickness Calculator

Minimum shell thickness for internal pressure, with joint efficiency and corrosion allowance — a first estimate before the code calculation.

Calculator

MPa
mm
MPa

Double-welded butt joint: 1.00 full radiography, 0.85 spot, 0.70 none (ASME Table UW-12).

mm

Not a design or code calculation. Pressure vessels and piping must be designed by a qualified engineer to the applicable code (such as ASME Section VIII or B31.3, in the edition adopted where they are installed) and inspected as that code requires.

Example Result

Your result will appear here

The calculated result will appear here after you press Calculate.

About the Pressure Vessel Wall Thickness Calculator

Internal pressure tries to split a cylindrical shell along its length, so the hoop stress sets the wall thickness. The ASME Section VIII, Division 1 formula t = P R ÷ (S E − 0.6 P) turns that into a minimum thickness from the design pressure P, the inside radius R, the material's allowable stress S at design temperature and the efficiency E of the longitudinal weld; the corrosion allowance is added on top. Enter those values to get the required thickness, a check of the longitudinal (circumferential-seam) formula and, at high pressures, the thick-wall result. A pipe mode applies the ASME B31.3 formula to outside diameter and adds mill tolerance. The examples below show how joint efficiency and corrosion allowance move the answer and where the thin-wall formula stops applying.

How to Use the Pressure Vessel Wall Thickness Calculator

  1. 1

    Choose the vessel shell or the pipe mode, and SI (MPa, mm) or Imperial (psi, in).

  2. 2

    Enter the design pressure and the inside radius (shell) or outside diameter (pipe).

  3. 3

    Enter the allowable stress at the design temperature from the code's material tables.

  4. 4

    Enter the joint efficiency (shell: 1.00 full radiography, 0.85 spot, 0.70 none for a double-welded butt joint) and the corrosion allowance.

  5. 5

    Press Calculate. The result shows which formula was used; outside the formulas' range no result is shown.

Pressure Vessel Wall Thickness Calculator Examples

Frequently Asked Questions

What is the ASME formula for shell thickness?

t = P R ÷ (S E − 0.6 P) for hoop stress, with R the inside radius in the corroded condition; add the corrosion allowance.

When do I need the thick-wall formula?

When P exceeds 0.385 S E or the thickness exceeds half the inside radius; the calculator then uses the Appendix 1-2 equation. When P reaches S E no thickness works and no result is shown.

What joint efficiency should I use?

For a double-welded butt joint: 1.00 with full radiography, 0.85 with spot radiography, 0.70 with none (ASME Table UW-12); seamless shells have their own rules.

Why is corrosion allowance added to the radius as well?

The code checks the vessel in its corroded state, when the bore is larger and the wall thinner.

How is pipe wall thickness different?

Pipe uses outside diameter, the B31.3 Y coefficient and a mill under-tolerance, usually 12.5%.

Is this a code calculation?

No. It is a first estimate; the final design must be made and checked by a qualified engineer against the current edition of the applicable code.

By O.E. — Partner, chairman of the board and CEO of a metal products manufacturer for 21 years; the company exports to 45 countries.

Drafted with AI assistance; calculations checked against primary sources and tested with the site's own code. About FlowUtil

Last reviewed

The shell formulas and their limits

Hoop stress (longitudinal seams), ASME Section VIII Division 1 UG-27: t = P R ÷ (S E − 0.6 P), while t ≤ R/2 and P ≤ 0.385 S E. Longitudinal stress (circumferential seams): t = P R ÷ (2 S E + 0.4 P). Above those limits the thick-shell equation of Mandatory Appendix 1-2 applies: t = R (√Z − 1), Z = (S E + P) ÷ (S E − P). When P reaches S E no thickness satisfies the equation, and the calculator shows no result. R is the inside radius in the corroded condition — the nominal radius plus the corrosion allowance — because the code checks the vessel at the end of its life; the corrosion allowance is then added to the thickness.

SymbolMeaning
PInternal design pressure (gauge)
RInside radius + corrosion allowance
SMaximum allowable stress at the design temperature
EJoint efficiency (Table UW-12)

A shell, a big vessel and a thick one

  1. 11.5 MPa (about 218 psi), inside radius 300 mm, S = 130 MPa, seamless or fully radiographed (E = 1.0), corrosion allowance 3 mm.

    Corroded R = 303 mm; limit 0.385 S E = 50.1 MPa; 1.5 × 303 ÷ (130 − 0.9)

    Hoop 3.52 mm · longitudinal 1.74 mm · required 6.52 mm with corrosion

    The plate is then ordered at the next standard thickness that still meets 6.52 mm after any plate under-tolerance.

  2. 2Thick shell: 100 MPa, R = 100 mm, S = 130 MPa, E = 1.0.

    P > 0.385 S E = 50 MPa → Z = 230 ÷ 30

    176.9 mm (Appendix 1-2)

    The thin-shell formula would give 142.9 mm — not conservative at this pressure. Below the limit the two agree closely: at 30 MPa and S = 150 MPa the UG-27 formula's 22.7 mm stands.

  3. 3US shell: 250 psi, 30 in inside diameter (R = 15 in), S = 20,000 psi, spot radiography (E = 0.85), 1/8 in corrosion allowance.

    250 × 15.125 ÷ (17,000 − 150)

    0.224 in + 0.125 = 0.349 in — a 3/8 in plate

Joint efficiency changes everything

2 MPa, inside radius 500 mm, S = 138 MPa, corrosion allowance 3 mm, double-welded butt joint:

Radiography of the longitudinal seamE (Table UW-12)Required thickness
Full1.0010.35 mm
Spot0.8511.66 mm
None0.7013.55 mm

Paying for radiography is often cheaper than 30% more steel.

Pipe: the ASME B31.3 form

Process piping is specified by outside diameter and ordered with a mill under-tolerance, typically 12.5% of the nominal wall. ASME B31.3 uses t = P D ÷ [2 (S E W + P Y)], ordered wall ≥ (t + c) ÷ 0.875, with W the weld strength reduction factor (1.0 below the creep range), Y = 0.4 for ferritic and austenitic steels at moderate temperature, and c the corrosion and thread allowance; the formula applies while t < D/6. For 10 MPa in a 114.3 mm (4 in NPS) seamless pipe at S = 138 MPa: t = 4.03 mm, plus 1.5 mm = 5.53 mm, ÷ 0.875 = 6.31 mm minimum nominal wall. The simple Barlow formula P D ÷ 2 S gives 4.14 mm because it ignores the Y term.

What this calculator does not cover

  • Heads and nozzlesEllipsoidal, torispherical and hemispherical heads have their own formulas, and openings need reinforcement.
  • External pressure and vacuumA shell can buckle inwards at a fraction of its internal-pressure rating.
  • Allowable stressTake S from the code's material tables at the design temperature; it falls as temperature rises.
  • Code complianceIn most jurisdictions pressure vessels above certain sizes and pressures must be designed, built, inspected and stamped to a recognised code. This is a first estimate; the final thickness must be checked by a qualified engineer against the current edition of the code.

Sources

  1. ASME Boiler and Pressure Vessel Code, Section VIII, Division 1 — UG-27, Mandatory Appendix 1-2, Table UW-12 — code text not accessed; limits as quoted in secondary training and software documentation
  2. ASME B31.3, Process Piping — para. 304.1.2 — code text not accessed

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