EN 13445 is the harmonised European standard for unfired pressure vessels — the primary design and fabrication reference for process vessels, heat exchangers, reactors, separators, and accumulators intended for the European market. It is the standard your PED conformity assessment is built on. With 619 chunks across Parts 1, 2, 3 and 5 in the Leide Navigator, this guide covers the complete design chain: from vessel categorisation and material selection through design calculations, weld joint quality, and final inspection requirements.
- Scope and PED Alignment
- Part 1 — General: Vessel Categories and Essential Requirements
- Part 2 — Materials: Grouping, Impact Testing, and Elevated Temperature
- Part 3 — Design: DBF vs DBA, Stress Categories, Fatigue
- Weld Joint Coefficients and NDE in Part 3
- Part 5 — Inspection: Groups, NDT Extent, Pressure Test
- Cross-Standard Reference Map
- Common Engineering Errors Across All Parts
1. Scope and PED Alignment
EN 13445 applies to unfired pressure vessels — vessels not subject to direct flame exposure — made primarily from steel, with design pressure PS > 0.5 bar gauge. It provides the technical means to demonstrate conformity with the Pressure Equipment Directive (PED) 2014/68/EU, which governs vessels placed on the EU market.
Key scope boundaries:
- IN scope: Fixed pressure vessels ≥ PS 0.5 barg, operating temperatures from cryogenic to ≥ 500°C, carbon and alloy steels, austenitic stainless and duplex grades covered by EN 10028
- OUT of scope: Fired vessels, boilers, transportable pressure equipment (covered by TPED), pipelines (EN 13480), offshore pressure vessels under DNV class where the DNV rules govern (though EN 13445 is often used by reference)
- ASME relationship: EN 13445 uses design-by-formula (Part 3) with allowable stress at 2/3 Re or 1/2.4 Rm; ASME VIII Div.1 uses 1/3.5 Rm — the different safety margins mean direct code substitution without recalculation is not acceptable
2. Part 1 — General: Vessel Categories and Essential Requirements
Part 1 establishes the overall framework and maps to the PED's risk-based vessel classification. The PED categorises pressure equipment into Categories I through IV based on fluid group (Group 1 = dangerous; Group 2 = other) and the product of maximum allowable pressure PS × volume V (for vessels) or PS × nominal size DN (for piping).
| PED Category | Conformity Assessment Route | Notified Body Involvement | Typical Application |
|---|---|---|---|
| Category I | Module A (internal production control) | None — manufacturer self-certifies | Low-pressure vessels, Group 2 fluids, low PS×V |
| Category II | Module A1, D1, or E1 | Surveillance of manufacturing or QMS audit | Medium PS×V, Group 2 fluids |
| Category III | Module B+D, B+F, B+E, G, or H1 | Type examination + QMS or individual verification | High PS×V or Group 1 fluids |
| Category IV | Module G (individual verification) or H1 | Full individual inspection and test witness | Highest risk: high PS, large volume, Group 1 dangerous fluids |
Part 1 also defines the minimum qualification requirements for personnel (welders per EN ISO 9606, NDE operators per EN ISO 9712), the documentation structure (Manufacturer's Design Report, MDR), and the required traceability of materials throughout fabrication.
3. Part 2 — Materials: Grouping, Impact Testing, and Elevated Temperature
Part 2 governs material selection and qualification. It does not specify which steel to use — that is in the EN 10028 product standards — but it defines how materials are grouped, what impact test evidence is required, and how properties at elevated temperature are used in design.
Material grouping
EN 13445-2 adopts the ISO/TR 15608 grouping scheme (Groups 1–11), which controls welding procedure qualification. A welding procedure qualification (WPQ) for a higher group covers lower groups within the same group range. Key groups for pressure vessel work:
| Group | Steel Type | Typical Grades |
|---|---|---|
| 1.1 | Normalised carbon-manganese steel, Re ≤ 275 MPa | P235GH, S235JR, P265GH |
| 1.2 | Fine-grain C-Mn, Re 275–360 MPa | P275NH, P355NH, S355J2+N |
| 1.3 | Normalised C-Mn, Re 360–460 MPa | P380NH, S420N |
| 4 | Low-alloy vanadium or Cr–Mo for elevated temperature | 13CrMo4-5, 10CrMo9-10 |
| 8.1 | Austenitic stainless (Cr-Ni, low C or stabilised) | 1.4301, 1.4307, 1.4404, 1.4571 |
| 10 | Duplex (austenitic-ferritic) | 1.4462 (2205), 1.4410 (2507) |
Impact testing requirements
Part 2 §4.4 defines the minimum design temperature (MDT) and requires Charpy impact testing at or below that temperature. The acceptance criterion is 27 J minimum average (minimum individual 20 J) for most ferritic grades. For vessels operating below −10°C, the impact sub-grade must match: JR (0°C), J0 (−20°C), J2 (−40°C), K2 (−40°C, higher energy).
For ferritic steel: KVavg ≥ 27 J at Timpact; KVmin ≥ 20 J
Thickness correction: for t > 25 mm, Timpact shifted up by Δ (table lookup)
Properties at elevated temperature
When the design temperature exceeds ~300°C for carbon steel or ~400°C for austenitic stainless, the allowable stress must use elevated-temperature values. Part 2 Annex B provides yield strength Rp0.2/T and creep rupture strength Ru/T for standard grades. The design allowable is the lower of:
Where Ru/T = average stress to rupture at temperature T in 100,000 hours
For austenitic stainless at temperatures above 500°C, the creep term controls — and the long-time creep rupture values (Annex B) diverge significantly from short-time tensile properties. Using room-temperature yield strength for a high-temperature austenitic vessel is a critical error.
4. Part 3 — Design: DBF vs DBA, Stress Categories, and Fatigue
Part 3 is the engineering core of EN 13445 — it contains the design-by-formula (DBF) rules for shells, heads, nozzles, and flanges, the design-by-analysis (DBA) methods for complex geometry, and the fatigue assessment approach. It is the largest part of the standard by far. Two separate deep-dive articles cover specific aspects:
- EN 13445-3: Design by Formula — shells, heads, nozzles, flanges
- EN 13445-3: DBF vs DBA — when to use each method
This section summarises the key concepts across Part 3.
Design by formula (DBF) — shell wall thickness
The fundamental shell wall thickness formula (§7.4.2 for cylindrical shells under internal pressure):
Where:
Pc = calculation pressure (barg)
Di = inside diameter (mm)
f = nominal design stress = min(Re/T/1.5, Rm/20/2.4) [MPa]
z = weld joint coefficient (0.85 or 1.0 — depends on inspection group)
Design by analysis (DBA) — stress categories
When geometry is too complex for DBF formulas (branch intersections, non-standard head shapes, supports with combined loading), DBA per EN 13445-3 Annex B uses linear elastic stress analysis categorised into:
| Stress Category | Symbol | Description | Allowable Limit |
|---|---|---|---|
| Primary membrane | Pm | General stress maintaining equilibrium with pressure and mechanical loads — does not redistribute if plastic | ≤ f |
| Primary bending | Pb | Bending stress from primary loads (self-limiting by redistribution at limit load) | ≤ 1.5 f |
| Secondary | Q | Stress from structural discontinuity or thermal gradient — self-limiting (shakedown governs) | Pm + Pb + Q ≤ 3f (shakedown) |
| Peak | F | Local stress concentration — relevant for fatigue only | Assessed in fatigue per §18 |
Fatigue assessment (Part 3 §18)
EN 13445-3 §18 provides a fatigue assessment method for vessels subjected to cyclic pressure, thermal cycling, or mechanical loading. The method uses fatigue curves (S-N curves) categorised by weld detail class, with cycles to failure NA as a function of equivalent stress range Δσeq:
ni = applied cycles at stress range Δσi
NAi = allowable cycles from fatigue curve at Δσi
Weld class W assigned from Table 18-4 (butt weld, fillet, nozzle, etc.)
The standard provides separate fatigue curves for unwelded material, butt welds, and fillet/attachment welds. The weld curves have a characteristic knee point at ~2×10⁶ cycles and a slope change. For vessels with low cycle counts but high stress ranges (pressure cycling > 5% of design pressure over hundreds of cycles), Part 3 §18 fatigue screening must confirm that simplified assessment criteria are met before omitting the full analysis.
5. Weld Joint Coefficients and NDT in Part 3
Part 3 §8 defines weld joint coefficients z that directly affect the calculated wall thickness. The coefficient reflects the quality of weld examination — a lower z means less NDT, requiring thicker walls to compensate:
| Weld Joint Coefficient z | Examination Required | Applicable NDT |
|---|---|---|
| z = 1.0 | 100% volumetric examination (RT or UT) of butt welds | RT or UT 100% + VT + PT/MT as required |
| z = 0.85 | Spot examination (typically 25% or less by length) | Spot RT or UT + VT |
The choice of z=0.85 vs z=1.0 must be consistent with the inspection group selected in Part 5. In practice: inspection group a → z=1.0; groups b/c → z=0.85 is permissible (but check Part 5 §6.6 for details of extent required at each group).
6. Part 5 — Inspection: Groups, NDT Extent, and Pressure Test
Part 5 governs manufacturing inspection and testing — the activities that verify the vessel meets the design. It defines inspection groups, NDT extent by joint type and group, and the pressure test requirements.
Inspection groups
Part 5 §6 assigns each vessel to an inspection group (a, b, or c) based on the material group (from Part 2), design temperature, and fluid hazard. The inspection group controls the minimum NDT extent for each weld category:
| Inspection Group | Minimum NDT — Butt Welds | Typical Conditions |
|---|---|---|
| Group a (most stringent) | 100% RT or UT of all butt welds (z = 1.0 permitted) | Group 1 hazardous fluids, high temperature, thick wall, or Cat IV PED |
| Group b | 25% spot RT or UT of longitudinal welds; 100% of circumferential weld intersection areas | Most Cat II/III vessels with Group 2 non-dangerous fluids |
| Group c (least stringent) | VT only for most welds; spot RT/UT only at junctions | Low-pressure Cat I/II, Group 2 fluids, low temperature |
NDT methods and acceptance criteria
Part 5 §7 specifies the NDT methods acceptable for each weld type and requires acceptance criteria per the relevant NDT product standard:
- Radiographic testing (RT): EN ISO 17636-1/2 — acceptance per EN ISO 10675-1 or as specified in Part 5
- Ultrasonic testing (UT): EN ISO 17640 + TOFD per EN ISO 10863 — acceptance per EN ISO 11666
- Magnetic particle testing (MT): EN ISO 17638 — surface and near-surface indications
- Penetrant testing (PT): EN ISO 3452 — surface-breaking indications for non-magnetic materials (austenitic, duplex)
Pressure test requirements
Part 5 §10 requires a hydrostatic pressure test before the vessel enters service. The test pressure is:
Where:
PS = maximum allowable pressure (barg)
f20 = allowable stress at 20°C
fT = allowable stress at design temperature T
(ratio > 1.0 when design temperature exceeds ~250–300°C — test pressure exceeds 1.25×PS)
Where a hydrostatic test would damage the vessel (e.g. cryogenic liners, ceramic-lined vessels), a pneumatic test at 1.1 × PS is permitted per Part 5 §10.2.4 — subject to additional precautions (pressure relief valve, personnel exclusion zone, risk assessment). Pneumatic tests carry higher stored energy than hydrostatic and require NB witness for Cat III/IV.
7. Cross-Standard Reference Map
| Standard | Interface with EN 13445 |
|---|---|
| PED 2014/68/EU | The legal framework — EN 13445 harmonised against it; vessel categories I–IV defined here |
| EN 10028 (all parts) | Material product standards: Part 2 (P-grades, C-Mn), Part 3 (Ni-alloyed for low temp), Part 7 (austenitic/duplex for pressure — 1.4301, 1.4404, 1.4462) |
| EN 10204 | Material inspection document types: 2.1 (declaration of compliance), 2.2 (test report), 3.1 (inspection certificate), 3.2 (witnessed). Cat III/IV pressure parts typically require 3.1 minimum |
| EN ISO 9606-1 | Welder qualification for steel — required by Part 2 §4.5 |
| EN ISO 15614-1 | Welding procedure specification and qualification (WPQR) — required before production welding |
| ISO/TR 15608 | Material grouping system — Part 2 adopts Groups 1–11 for WPS/WPQR qualification coverage |
| NORSOK M-001 | Material selection for offshore — austenitic/duplex grades overlapping with EN 13445-2 used for offshore process vessels; NORSOK adds duplex weldability and HISC restrictions beyond EN 13445 |
| EN 13480 | Industrial piping — sister standard to EN 13445; vessels connected to piping must be assessed at the nozzle interface for combined loading |
8. Common Engineering Errors Across All Parts
Design and material selection errors
- Selecting allowable stress at design temperature from room-temperature data — for carbon steel above ~300°C and austenitic stainless above ~400°C, the elevated-temperature properties (Rp0.2/T, Ru/T) from Part 2 Annex B are lower and control the design; ignoring this produces non-conservative wall thicknesses
- Using z = 1.0 in the DBF calculation without committing to group a NDT in the Inspection and Test Plan — the weld joint coefficient must match the actual NDT that will be performed; specifying z = 1.0 and then carrying out only spot RT (group b) is non-conforming
- Impact testing not repeated for parent material if a repair weld results in local heat treatment beyond the original PWHT temperature — Part 2 §4.4.6 requires retesting when PWHT parameters change material toughness
Inspection and documentation errors
- MDR (Manufacturer's Design Report) issued without referencing the Notified Body's type examination certificate for Cat III/IV vessels — the MDR must reference the NB reference number; a CE-marked vessel without this traceability is non-compliant regardless of the technical content of the calculations
- Pressure test performed with the vessel partially assembled (insulation, internals) so inspectors cannot access the welds during the hold — Part 5 §10.2 requires visual inspection of all accessible welds during the pressure hold; hidden welds must be confirmed accessible before test or inspected before closure
- Pneumatic test used for cost savings without the required risk assessment and exclusion zone — Part 5 §10.2.4 permits pneumatic testing only where hydrostatic is damaging or impractical; using it to avoid draining a water-sensitive vessel is not a valid justification without documented risk assessment and NB concurrence
Ask the Leide Navigator about EN 13445
EN 13445 Parts 1 (36 chunks), 2 (81 chunks), 3 (459 chunks), and 5 (43 chunks) are fully loaded in the Leide Navigator — 619 chunks total. Ask about inspection group requirements, fatigue screening criteria, allowable stress at elevated temperature, weld joint coefficients, or specific clause interpretations. Cited answers in under 3 seconds.