Design cylindrical shells according to Boiler & Pressure Vessel Code. Computes minimum required thickness, design thickness (with corrosion allowance), and Maximum Allowable Working Pressure (MAWP).
This calculator implements the cylindrical shell thickness formula under internal pressure per ASME Boiler and Pressure Vessel Code, Section VIII, Division 1, Paragraph UG-27(c)(1). For a cylindrical vessel, the minimum required wall thickness (excluding corrosion allowance) is:
Where: P = design pressure (MPa), R = inside radius (mm), S = maximum allowable stress from ASME Section II Part D (MPa), E = weld joint efficiency based on radiography status. The 0.6P factor in denominator accounts for stress redistribution in the shell wall and is characteristic of the ASME code. After computing tmin, the design thickness includes corrosion allowance (CA): tdes = tmin + CA. The MAWP (Maximum Allowable Working Pressure) is back-calculated using the chosen nominal thickness (rounded up plate).
Engineers must also consider external pressure, wind/seismic loads, nozzle reinforcement, and fatigue if cyclic service. The tool serves for preliminary sizing and educational insight.
| Material | 100°C (MPa) | 200°C (MPa) | 300°C (MPa) | Typical Use |
|---|---|---|---|---|
| SA-516 Gr.70 (Carbon Steel) | 138 | 138 | 128 | General pressure vessels |
| SA-240 304 (Stainless) | 115 | 105 | 92 | Corrosive / sanitary |
| SA-508 Cl.3 (Alloy Steel) | 190 | 185 | 175 | High-pressure reactors |
| SA-106 Gr.B (Pipe) | 118 | 110 | 100 | Small bore vessels |
While ASME uses the factor 0.6P in the denominator for cylindrical shells, EN 13445 (European standard) employs a slightly different formula based on mean diameter. Both are widely accepted; ASME is predominant in North America, Asia, and many international projects. Our calculator strictly follows ASME rules to ensure global code alignment.
1. Shell thickness (this tool) → 2. Head thickness (ellipsoidal, hemispherical, or torispherical per UG-32) → 3. Nozzle reinforcement (UG-36 to UG-43) → 4. External pressure (UG-28) → 5. Hydrotest pressure (UG-99). For a complete design, all components must be verified. This calculator focuses on the cylindrical shell, which is the most critical element.
Tip: For head thickness, use thead = P·D / (2·S·E – 0.2·P) for 2:1 ellipsoidal heads, typically slightly thicker than the shell.
Incorrect thickness can lead to catastrophic rupture, leakage, or non-compliance with jurisdictional regulations. Pressure vessel failures account for significant industrial hazards — precise design according to recognized standards (ASME, EN 13445) ensures safety, longevity, and operational reliability. This calculator respects code rules and provides a solid basis for vessel specification, material procurement, and fabrication drawings.
A chemical plant required a horizontal cylindrical vessel: ID = 2400 mm, design pressure = 2.8 MPa, material SA-516 Gr.70 (S = 138 MPa at 50°C), joint efficiency 0.85, corrosion allowance 4 mm. Using our calculator: tmin = (2.8×1200)/(138×0.85 - 0.6×2.8) = 3360/(117.3 - 1.68) = 3360/115.62 ≈ 29.05 mm. Adding CA = 33.05 mm. Next standard plate = 34 mm. The MAWP based on 34 mm plate reached 3.05 MPa, providing adequate margin.
| Material / Grade | Allowable Stress (MPa) @ 150°C | Typical Use |
|---|---|---|
| SA-516 Gr.70 (Carbon Steel) | 138 | Pressure vessels, process drums |
| SA-240 304 (Stainless) | 115 | Corrosive / sanitary services |
| SA-508 Cl.3 (Alloy Steel) | 190 | High-pressure reactors |
| SA-106 Gr.B (Pipe) | 118 | Small bore vessels |
Joint Efficiency (E): Full radiography = 1.0 (highest integrity); Spot radiography = 0.85; No radiography = 0.7 (only for non-lethal service). Selection impacts thickness directly.