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.

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.

EN 13445-1 §1: "This European Standard specifies requirements for the design, fabrication, testing and inspection of unfired pressure vessels. These vessels are made of steel and are intended to be used in industrial applications."

Key scope boundaries:

2. Part 1 — General: Vessel Categories and Essential Requirements

EN 13445-1 · 36 chunks

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 CategoryConformity Assessment RouteNotified Body InvolvementTypical Application
Category IModule A (internal production control)None — manufacturer self-certifiesLow-pressure vessels, Group 2 fluids, low PS×V
Category IIModule A1, D1, or E1Surveillance of manufacturing or QMS auditMedium PS×V, Group 2 fluids
Category IIIModule B+D, B+F, B+E, G, or H1Type examination + QMS or individual verificationHigh PS×V or Group 1 fluids
Category IVModule G (individual verification) or H1Full individual inspection and test witnessHighest 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.

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PED vs. EN 13445 relationship: The PED is EU law — you cannot substitute it with EN 13445. EN 13445 is a harmonised standard that, when applied in full, creates a presumption of conformity with the PED's essential safety requirements. If you deviate from EN 13445 you must separately demonstrate PED compliance through the Notified Body. Using EN 13445 plus a Notified Body for Cat III/IV vessels is the standard route — not a choice between one or the other.

3. Part 2 — Materials: Grouping, Impact Testing, and Elevated Temperature

EN 13445-2 · 81 chunks

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:

GroupSteel TypeTypical Grades
1.1Normalised carbon-manganese steel, Re ≤ 275 MPaP235GH, S235JR, P265GH
1.2Fine-grain C-Mn, Re 275–360 MPaP275NH, P355NH, S355J2+N
1.3Normalised C-Mn, Re 360–460 MPaP380NH, S420N
4Low-alloy vanadium or Cr–Mo for elevated temperature13CrMo4-5, 10CrMo9-10
8.1Austenitic stainless (Cr-Ni, low C or stabilised)1.4301, 1.4307, 1.4404, 1.4571
10Duplex (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).

Impact test temperature selection (EN 13445-2 §4.4)
Timpact ≤ MDT (minimum design temperature)
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:

Allowable stress at elevated temperature (EN 13445-3 §6.1, informed by Part 2)
f = min(Rp0.2/T / 1.5 , Rm/20 / 2.4 , Ru/T / 1.5 )
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

EN 13445-3 · 459 chunks

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:

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):

Cylindrical shell — minimum wall thickness (EN 13445-3 §7.4.2)
es = (Pc × Di) / (2 × f × z − Pc)

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 CategorySymbolDescriptionAllowable Limit
Primary membranePmGeneral stress maintaining equilibrium with pressure and mechanical loads — does not redistribute if plastic≤ f
Primary bendingPbBending stress from primary loads (self-limiting by redistribution at limit load)≤ 1.5 f
SecondaryQStress from structural discontinuity or thermal gradient — self-limiting (shakedown governs)Pm + Pb + Q ≤ 3f (shakedown)
PeakFLocal stress concentration — relevant for fatigue onlyAssessed 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:

Fatigue damage — EN 13445-3 §18 (Miner's rule)
D = Σ (ni / NAi) ≤ 1.0

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 zExamination RequiredApplicable NDT
z = 1.0100% volumetric examination (RT or UT) of butt weldsRT or UT 100% + VT + PT/MT as required
z = 0.85Spot 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

EN 13445-5 · 43 chunks

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 GroupMinimum NDT — Butt WeldsTypical 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
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Group a vs group b economics: Specifying group a increases NDT cost (typically +20–40% on weld inspection) but allows z=1.0, reducing wall thickness. For thick-walled vessels in expensive alloy steels (duplex, Cr-Mo), the material savings from thinner walls can outweigh the NDT cost. The calculation is worth running at FEED for any vessel with wall thickness >40 mm or expensive material grade.

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:

Pressure test requirements

Part 5 §10 requires a hydrostatic pressure test before the vessel enters service. The test pressure is:

Hydrostatic test pressure (EN 13445-5 §10.2.3.2)
PT = 1.25 × PS × (f20 / fT)

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

StandardInterface with EN 13445
PED 2014/68/EUThe 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 10204Material 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 9606-1Welder qualification for steel — required by Part 2 §4.5
EN ISO 15614-1Welding procedure specification and qualification (WPQR) — required before production welding
ISO/TR 15608Material grouping system — Part 2 adopts Groups 1–11 for WPS/WPQR qualification coverage
NORSOK M-001Material 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 13480Industrial 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

Inspection and documentation errors

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Fatigue screening shortcut that fails: EN 13445-3 §18.2 provides simplified fatigue screening criteria — if the equivalent number of full pressure cycles is below a threshold, detailed fatigue analysis is not required. The most common error is applying the screening at design pressure without checking thermal cycles separately. On heat exchangers, the thermal cycle count frequently exceeds the screening limit even when the pressure cycle count does not. Both must independently clear the screening threshold, or the full §18 fatigue assessment applies.

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.

💡 Try asking: "What inspection category applies to a pressure vessel with a weld joint coefficient of 0.85?"