SIST EN 1594:2024/oprA1:2025

SLOVENSKI STANDARD
01-junij-2025
Infrastruktura za plin - Cevovodni sistemi za najvišji delovni tlak nad 16 bar -
Funkcionalne zahteve - Dopolnilo A1
Gas infrastructure - Pipelines for maximum operating pressure over 16 bar - Functional
requirements
Gasinfrastruktur - Rohrleitungen für einen maximal zulässigen Betriebsdruck über 16 bar
- Funktionale Anforderungen
Infrastructures gazières - Canalisation pour pression maximale de service supérieure à
16 bar - Prescriptions fonctionnelles
Ta slovenski standard je istoveten z: EN 1594:2024/prA1
ICS:
91.140.40 Sistemi za oskrbo s plinom Gas supply systems
2003-01.Slovenski inštitut za standardizacijo. Razmnoževanje celote ali delov tega standarda ni dovoljeno.

DRAFT
EUROPEAN STANDARD
EN 1594:2024
NORME EUROPÉENNE
EUROPÄISCHE NORM
prA1
June 2025
ICS
English Version
Gas infrastructure - Pipelines for maximum operating
pressure over 16 bar - Functional requirements
Infrastructures gazières - Canalisation pour pression Gasinfrastruktur - Rohrleitungen für einen maximal
maximale de service supérieure à 16 bar - zulässigen Betriebsdruck über 16 bar - Funktionale
Prescriptions fonctionnelles Anforderungen
This draft amendment is submitted to CEN members for enquiry. It has been drawn up by the Technical Committee CEN/TC 234.

This draft amendment A1, if approved, will modify the European Standard EN 1594:2024. If this draft becomes an amendment,
CEN members are bound to comply with the CEN/CENELEC Internal Regulations which stipulate the conditions for inclusion of
this amendment into the relevant national standard without any alteration.

This draft amendment was established by CEN in three official versions (English, French, German). A version in any other
language made by translation under the responsibility of a CEN member into its own language and notified to the CEN-CENELEC
Management Centre has the same status as the official versions.

CEN members are the national standards bodies of Austria, Belgium, Bulgaria, Croatia, Cyprus, Czech Republic, Denmark, Estonia,
Finland, France, Germany, Greece, Hungary, Iceland, Ireland, Italy, Latvia, Lithuania, Luxembourg, Malta, Netherlands, Norway,
Poland, Portugal, Republic of North Macedonia, Romania, Serbia, Slovakia, Slovenia, Spain, Sweden, Switzerland, Türkiye and
United Kingdom.
Recipients of this draft are invited to submit, with their comments, notification of any relevant patent rights of which they are
aware and to provide supporting documentation.

Warning : This document is not a European Standard. It is distributed for review and comments. It is subject to change without
notice and shall not be referred to as a European Standard.

EUROPEAN COMMITTEE FOR STANDARDIZATION
COMITÉ EUROPÉEN DE NORMALISATION

EUROPÄISCHES KOMITEE FÜR NORMUNG

CEN-CENELEC Management Centre: Rue de la Science 23, B-1040 Brussels
© 2025 CEN All rights of exploitation in any form and by any means reserved Ref. No. EN 1594:2024/prA1:2025 E
worldwide for CEN national Members.

Contents Page
European foreword . 3
1 Addition to the foreword . 4
2 Addition to Clause 3 . 4
3 Addition to 6.1 . 4
4 Addition to 6.2 . 4
5 Modification to 7.1.1 . 5
6 Addition to 7.1.2.2 . 5
7 Addition to 7.2.1 . 5
8 Addition to 7.4.2.2 . 5
9 Addition to 7.5 . 5
10 Addition to 7.9.2 . 5
11 Addition to 7.12 . 5
12 Addition to 7.14 . 5
13 Addition to 8.1.5.1 . 6
14 Addition to 8.1.5.4 . 6
15 Addition to 8.4 . 6
16 Addition to 8.6 . 6
17 Replacement of 10.10 . 6
18 Replacement of Annex B . 8

European foreword
This document (EN 1594:2024/prA1:2025) has been prepared by Technical Committee CEN/TC 234
“Gas Infrastructure”, the secretariat of which is held by DIN.
This document is currently submitted to the CEN Enquiry.
This document has been prepared under a standardization request addressed to CEN by the European
Commission. The Standing Committee of the EFTA States subsequently approves these requests for its
Member States.
1 Addition to the foreword
In the foreword replace the 5th paragraph or add at the end of the 5th parapraph:
“The main changes between this document and the previous edition EN 1594:2024 are as follows:
— the full standard has been adapted to include hydrogen as a gas in this standard to replace the
informative annex of the previous edition,
— addition of provisions to be considered when using an existing line to transport gaseous hydrogen,
— addition of provisions on fracture mechanical verifications for gaseous hydrogen service,
— replacement of Annex B (informative) “Hydrogen gas pipelines” by Annex B (normative) “Fatigue
crack growth calculations and monitoring concepts for hydrogen service”.
2 Addition to Clause 3
In 3.11, replace title and definition by:
gas/gases
gaseous energy carrier which is in the gaseous state at a temperature of 15 °C and under an absolute
pressure of 0,1 MPa
Note 1 to entry: This includes hydrogen rich and methane rich gases, dimethyl ether (DME) and propane and
butanes and admixtures.
Add the following new definitions:
3.48
blended hydrogen operation
transmission of a gas mixture where the hydrogen partial pressure is over 2 bar
3.49
conversion
conversion of a gas pipeline as defined by this document refers to switching from the transportation of
methane-rich gases to the transportation of hydrogen gas pursuant to the scope of application
3.50
hydrogen service
operating a gas transmission system with a hydrogen pressure over 2 bar
3 Addition to 6.1
In 6.1, add as last sentence:
“For hydrogen or blended hydrogen operations, adequate monitoring for pressure cycling shall be
incorporated.”
4 Addition to 6.2
In 6.2, add as last sentence:
“For hydrogen or blended hydrogen operations, it shall be ensured that the pressure cycling shall be
within the design case.”
5 Modification to 7.1.1
In 7.1.1, in the last sentence, replace “repurposed are given in 10.6 and Annex B” with “converted
incorporated in this document”
6 Addition to 7.1.2.2
In 7.1.2.2, add after the third paragraph the second note:
“NOTE 2 For hydrogen or blended hydrogen a lower design factor can be used to accommodate larger
pressure cycles or a longer service life time.”
7 Addition to 7.2.1
In 7.2.1, renumber the “NOTE” as “NOTE 1”.
In 7.2.1, add NOTE 2 below the first note:
“NOTE 2 For hydrogen and blended hydrogen service it is recommended to not exceed the design factor
of 0,67, with the further wall thickness requirements in 7.9.2.”
8 Addition to 7.4.2.2
In 7.4.2.2, add at “relevant limit states” to item 'b Strain', after the second sentence:
“For hydrogen and blended hydrogen service the maximum limit strain is 0,5%.”
9 Addition to 7.5
In 7.5, add to the first summation at a) 2) the item iiii:
“iiii) for hydrogen or blended hydrogen service, the number and range of pressure cycles”;
10 Addition to 7.9.2
In 7.9.2, add to the fourth paragraph as last sentence:
“For hydrogen and blended hydrogen services, any differences in pressure cycling due to maintenance or
operations shall be included in the determination of the minimum wall thickness.”
11 Addition to 7.12
In 7.12, add a note after the first sentence:
“NOTE For hydrogen service or blended hydrogen service a double block and bleed design is recommended to
enable the use of an inert gas as separation between hydrogen and air.”
12 Addition to 7.14
In 7.14, add to summation as last point:
“ — Hydrogen injection stations: EN 17928-1/-2/-3”
13 Addition to 8.1.5.1
In 8.1.5.1, add after the last sentence:
“For hydrogen or blended hydrogen service a minimum value of 55 MPasqr(m) can be assumed for
fracture toughness when materials are ordered according to this document. When a larger toughness
value is used in the design of the pipeline, a proper fracture toughness test program on the pipeline
components shall be established to validate this higher value.”
14 Addition to 8.1.5.4
In 8.1.5.4, add after the last sentence:
“For hydrogen and blended hydrogen service the hardness shall not exceed 300 HV10”
15 Addition to 8.4
In 8.4, add after second sentence:
“For hydrogen or blended hydrogen service the suitability shall be taken into account, as a reference
EN ISO 11114-2: non-metallic materials can be used.”
16 Addition to 8.6
In 8.6, add after the last sentence:
“For hydrogen and blended hydrogen service this shall be included in the requisition and appropriate
design adaptions shall be included by the valve manufacturer.”
17 Replacement of 10.10
In 10.10 replace the current text by the following:
“10.10 Conversion process of existing onshore pipelines into hydrogen service
10.10.1 General
The aim of this paragraph is to provide guidance and technical requirements to gas transportation
operators to account for the effects of hydrogen on existing steel pipelines operating over 16 bar for
converting existing onshore pipelines into hydrogen service:
— existing pipelines designed, constructed, operated and maintained according EN 1594.
— existing pipelines not designed according EN 1594. Specific assessment should be done, specially for
fluids other than defined in Clause 1 of this document.
10.10.2 Checking of suitability
The conversion of gas pipelines should be carried out in accordance with the general consensus state-of
the-art that is in force at the time of conversion.
Impact and relevance of the changes between the standards as used in construction and the time of
conversion should be evaluated for the applicability and need for additional mitigation for the line to be
converted.
Specific attention should be paid to used materials, welds, the fluids that have been hitherto transported
in the pipeline, the pipeline’s former and future modes of operation, and eventually existing damaging as
well as local conditions.
It should be ensured that gas concomitant substances do not pose a hazard to the gas pipeline’s safety.
For the conversion of a gas pipeline, the tests listed in detail below shall be carried out and documented
by the operator in accordance with relevant standards with regard to installation, operation and
maintenance.
NOTE National regulations might exist for conversion of gas pipelines.
10.10.3 Documentation of Construction, Operation and Maintenance
The operator’s documentation on the construction of the gas pipeline, including all modifications, on the
previous mode of operation and on safety-relevant events should be examined for completeness and
compliance with the technical regulations and evaluated with regard to the planned conversion to
hydrogen. it should be checked whether the gas pipeline has been impaired by the previous mode of
operation with regard to the planned conversion.
Specific attention should be paid to the given items in the subsequent subclauses of 10.10.
10.10.4 Construction
When converting existing onshore pipelines into hydrogen service, specific attention should be paid to
the following items related to construction:
— current pipeline documentation (routing maps, as-built drawings, pipe book, pipe order list etc.).
— the suitability of material and the need of material testing
NOTE Certification on material tests or other technical aspects might be required by national authorities; also
third party certification might be required in some countries.
— documentation on type of product previously transported (e.g. sour service, sweet service).
— pressure test certificates.
— maintenance records (including repairs, fittings).
— current condition analysis / integrity (e.g. by inline inspection and direct assessment processes).
— results of NDT of girth welds.
10.10.5 Operation
When converting existing onshore pipelines into hydrogen service, specific attention should be paid to
the following items related to operation:
— documentation and properties of other fluids, including concomitant substances, that were
transported to date.
— pressure recordings of the operating conditions (recommended in case of suspecting large pressure
fluctuations), including corresponding analyses.
— external influences (e.g. mining activity, corrosive soil, built-up areas).
10.10.6 Maintenance
When converting existing onshore pipelines into hydrogen service, specific attention should be paid to
the following items related to maintenance:
— internal and external corrosion (condition of cathodic protection).
— Cathodic Protection report (effectiveness, electrical interferences, overprotection, etc.).
— current technical condition analysis.
If the pipeline documentation on pipeline construction is incomplete, appropriate analysis should be
made to establish alternative means and methods to provide sufficient reliance to enable the change of
fluid on the specific topics.
10.10.7 Gas Pipeline Hydrogen Suitability
10.10.7.1 General
The fracture toughness in hydrogen shall be established for the pipeline which will be transferred to
hydrogen service, together with all the relevant parameters (asset and operating conditions), shall be
used by the operator before the conversion to assess the feasibility of the change of fluid and during the
subsequent operation for the integrity assessment. Detailed description of pipeline fracture mechanics
assessment is described in Annex B.
10.10.7.2 Sampling
Detailed description of pipeline fracture mechanics assessment is described in Annex B.
10.10.8 Conversion Procedure and Report
The operator should elaborate a conversion procedure and a technical report for the potential
reconversion of an existing gas pipeline into hydrogen service.
NOTE National authorities and/or regulations and standards might require the submission of this Report for
the approval of authorities or its representatives.
10.10.9 Commissioning
The commissioning of the gas pipeline after its conversion is governed by the requirements established
in the applicable National Regulations and Standards.
10.10.10 Operation
The operation of the gas pipeline after conversion is governed by the requirements established in the
applicable National Regulations and Standards.
It is recommended to record and document the pressure load cycles of the converted pipeline. The
actually occurring load cycles should be compared to the assumed load cycles. Crack growth should be
repeatedly verified through calculation in continuous intervals.
10.10.11 Concluding Certification
Insofar substantive alterations have occurred, if explicitly stated by National Authorities and/or
Regulations and Standards, a test certificate should be issued by a Conformity Assessment-Body after the
changes and tests have been completed.
18 Replacement of Annex B
Annex B, replace by the following:
Annex B
(normative)
Fatigue crack growth calculations and monitoring concepts for hydrogen
service
B.1 Introduction and scope of application
High pressure natural gas pipelines usually are designed for predominantly static loads since barely any
significant changes in operating pressure (load cycles) occur and even sharp-edged defects that might
occur under such conditions exhibit a negligible growth rate. When operating the pipeline with hydrogen,
the fracture toughness can be lower and the steel potential fatigue crack growth rate (FCGR) larger than
the values obtained from operating with natural gas. Consequently, the operation with hydrogen usually
requires a fracture assessment for estimating its operational life or, if necessary, the operating conditions
in which fatigue crack can reasonably be expected to pose no risk to the integrity of a H2 pipeline along
its planned operational life.
This appendix shall apply for the fracture mechanical assessment of steel gas pipelines that already exist
or are projected for construction with a design pressure of more than 16 bar for the transmission or
distribution of hydrogen. Guidance is given for assessing cracks under both static loads (static strength)
and cyclic loads (fatigue strength) in H .
B.2 Crack Assessment models
In the following sections, as a rule, crack should be assumed to be a semi elliptical shape longitudinal
crack at the inner pipe wall for the purposes of a fracture mechanical assessment and can be described
by its height (a) and its length (2c) as shown in Figure B.1.

Figure B.1 — Main crack dimensions (cylinder shape)
API 579-1/ASME FFS-1 2019 (level 2) or BS 7910:2019 standards provide guidance for using fracture
mechanics to assess the static strength and the fatigue strength of a crack. Both documents are widely
used in the pipeline industry. The assessment procedures and failure assessment lines in
API 579-1/ASME FFS-1 and BS 7910 are similar and use a Failure Assessment Diagram (FAD) for crack
assessment.
The FAD is based on the principles of fracture mechanics. It considers failure by fracture and by plastic
collapse, and the relationship between the two. An example FAD is presented in Figure B.2.
The FAD has two p
...