ISO/FDIS 27913
(Main)Carbon dioxide capture, transportation and geological storage — Pipeline transportation systems
Carbon dioxide capture, transportation and geological storage — Pipeline transportation systems
ISO 27913:2016 specifies additional requirements and recommendations not covered in existing pipeline standards for the transportation of CO2 streams from the capture site to the storage facility where it is primarily stored in a geological formation or used for other purposes (e.g. for EOR or CO2 use). ISO 27913:2016 applies to - rigid metallic pipelines, - pipeline systems, - onshore and offshore pipelines for the transportation of CO2 streams, - conversion of existing pipelines for the transportation of CO2 streams, - pipeline transportation of CO2 streams for storage or utilization, and - transportation of CO2 in the gaseous and dense phases. The system boundary (see Figure 1) between capture and transportation is the point at the inlet valve of the pipeline, where the composition, temperature and pressure of the CO2 stream is within a certain specified range by the capture process or processes to meet the requirements for transportation as described in this document. The boundary between transportation and storage is the point where the CO2 stream leaves the transportation pipeline infrastructure and enters the storage infrastructure. ISO 27913:2016 also includes aspects of CO2 stream quality assurance, as well as converging CO2 streams from different sources. Health, safety and environment aspects specific to CO2 transport and monitoring are considered.
Captage, transport et stockage géologique du dioxyde de carbone — Systèmes de transport par conduites
ISO 27913:2016 spécifie des exigences et recommandations supplémentaires non mentionnées dans les normes existantes sur les conduites, applicables au transport de flux de CO2 du site de captage jusqu'à l'installation de stockage où il est principalement stocké dans des formations géologiques ou utilisé à d'autres fins (par exemple, pour une récupération assistée des hydrocarbures (EOR) ou une utilisation du CO2). ISO 27913:2016 s'applique: - aux conduites métalliques rigides; - aux systèmes de conduites; - aux conduites terrestres et en mer destinées au transport de flux de CO2; - à la conversion de conduites existantes pour le transport de flux de CO2; - au transport par conduites de flux de CO2 en vue d'un stockage ou d'une utilisation; et - au transport de CO2 en phase gazeuse et en phase dense. La limite du système (voir Figure 1) entre le captage et le transport est le point au niveau de la vanne d'entrée de la conduite, où la composition, la température et la pression du flux de CO2 sont régulées dans une certaine plage spécifiée par le ou les processus de captage afin de satisfaire aux exigences de transport décrites dans le présent document. La limite entre le transport et le stockage est le point au niveau duquel le flux de CO2 quitte l'infrastructure de conduites de transport et entre dans l'infrastructure de stockage. ISO 27913:2016 inclut également des aspects d'assurance qualité du flux de CO2 et traite de la convergence de flux de CO2 provenant de différentes sources. Les aspects de santé, de sécurité et environnementaux relatifs à la surveillance et au transport du CO2 sont pris en compte.
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FINAL DRAFT
International
Standard
ISO/TC 265
Carbon dioxide capture,
Secretariat: SCC
transportation and geological
Voting begins on:
storage — Pipeline transportation
2024-06-11
systems
Voting terminates on:
2024-08-06
Captage, transport et stockage géologique du dioxyde de
carbone — Systèmes de transport par conduites
RECIPIENTS OF THIS DRAFT ARE INVITED TO SUBMIT,
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TO BE CONSIDERED IN THE LIGHT OF THEIR POTENTIAL
TO BECOME STAN DARDS TO WHICH REFERENCE MAY BE
MADE IN NATIONAL REGULATIONS.
Reference number
FINAL DRAFT
International
Standard
ISO/TC 265
Carbon dioxide capture,
Secretariat: SCC
transportation and
Voting begins on:
geological storage — Pipeline
transportation systems
Voting terminates on:
Captage, transport et stockage géologique du dioxyde de
carbone — Systèmes de transport par conduites
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 SUPPOR TING DOCUMENTATION.
© ISO 2024
IN ADDITION TO THEIR EVALUATION AS
All rights reserved. Unless otherwise specified, or required in the context of its implementation, no part of this publication may
BEING ACCEPTABLE FOR INDUSTRIAL, TECHNO
LOGICAL, COMMERCIAL AND USER PURPOSES, DRAFT
be reproduced or utilized otherwise in any form or by any means, electronic or mechanical, including photocopying, or posting on
INTERNATIONAL STANDARDS MAY ON OCCASION HAVE
the internet or an intranet, without prior written permission. Permission can be requested from either ISO at the address below
TO BE CONSIDERED IN THE LIGHT OF THEIR POTENTIAL
or ISO’s member body in the country of the requester.
TO BECOME STAN DARDS TO WHICH REFERENCE MAY BE
MADE IN NATIONAL REGULATIONS.
ISO copyright office
CP 401 • Ch. de Blandonnet 8
CH-1214 Vernier, Geneva
Phone: +41 22 749 01 11
Email: copyright@iso.org
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Published in Switzerland Reference number
ii
Contents Page
Foreword .vi
Introduction .vii
1 Scope . 1
2 Normative references . 1
3 Terms and definitions . 1
4 Symbols, abbreviated terms and units . 5
4.1 Symbols .5
4.2 Abbreviated terms .5
5 Properties of CO , CO streams and the mixing of CO streams that influence pipeline
2 2 2
transportation . 6
5.1 General .6
5.2 Pure CO .6
5.2.1 Thermodynamics .6
5.2.2 Chemical reactions and corrosion .6
5.3 CO streams .7
5.3.1 Thermodynamics .7
5.3.2 Chemical reactions .7
6 Concept development and design criteria . 7
6.1 General .7
6.2 Safety philosophy .7
6.3 Reliability and availability of CO stream pipeline systems .8
6.4 Short-term storage reserve .8
6.5 Access to the pipeline system . .8
6.6 System design principles .9
6.6.1 General .9
6.6.2 CO stream specification .9
6.6.3 Pressure control and protection system .10
6.7 General principles to avoid internal pipeline corrosion .10
6.7.1 Particular aspects related to CO and CO streams .10
2 2
6.7.2 Maximum water content .10
6.7.3 Avoidance of hydrate formation .10
6.7.4 Measurement of water content in the CO stream .11
6.8 Flow assurance .11
6.8.1 General .11
6.8.2 Operation under single-phase flow conditions during normal operation .11
6.8.3 Pipeline operation under multi-phase flow conditions during transient
operations . . 12
6.8.4 Planned and unscheduled pipeline pressure release . 12
6.8.5 Reduced flow capacity. 13
6.8.6 Available transport capacity . 13
6.8.7 Flow coating . 13
6.8.8 External thermal insulation .14
6.8.9 Leak detection .14
6.8.10 Fugitive emissions .14
6.8.11 Impurities .14
6.9 Pipeline layout.14
6.9.1 Vent stations .14
6.9.2 Block valve stations . 15
6.9.3 Pumping and compressor stations . 15
6.9.4 In-line inspection . 15
6.9.5 Onshore vent facility design . . 15
6.9.6 Offshore vent facilities .16
iii
7 Materials and pipeline design .16
7.1 General .16
7.2 Internal corrosion .16
7.3 Pipeline system materials .17
7.3.1 Steel selection .17
7.3.2 External coating .17
7.3.3 Non-metallic materials .17
7.3.4 Lubricants .17
8 Wall thickness calculations .18
8.1 Calculation principles .18
8.1.1 Design loads .18
8.1.2 Minimum wall thickness
...
ISO/TC 265/WG 2
Secretariat: SCC
Date: 2024-02-1605-27
Carbon dioxide capture, transportation and geological storage —
Pipeline transportation systems
Captage du dioxide de carbone, transport et stockage géologique du dioxyde de carbone — Systèmes
de transport par conduites
FDIS stage
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A model manuscript of a draft International Standard (known as “The Rice Model”) is available at
© ISO #### – All rights reserved
ISO #####-#:####(X)
2 © ISO #### – All rights reserved
All rights reserved. Unless otherwise specified, or required in the context of its implementation, no part of this publication
may be reproduced or utilized otherwise in any form or by any means, electronic or mechanical, including photocopying,
or posting on the internet or an intranet, without prior written permission. Permission can be requested from either ISO
at the address below or ISO’s member body in the country of the requester.
ISO copyright office
CP 401 • Ch. de Blandonnet 8
CH-1214 Vernier, Geneva
Phone: + 41 22 749 01 11
EmailE-mail: copyright@iso.org
Website: www.iso.orgwww.iso.org
Published in Switzerland
iii
Contents
Foreword . vii
Introduction . ix
1 Scope . 1
2 Normative references . 1
3 Terms and definitions . 1
4 Symbols, abbreviated terms and units . 5
4.1 Symbols . 5
4.2 Abbreviated terms . 6
5 Properties of CO , CO streams and the mixing of CO streams that influence pipeline
2 2 2
transportation . 6
5.1 General . 6
5.2 Pure CO . 7
5.2.1 Thermodynamics . 7
5.2.2 Chemical reactions and corrosion . 7
5.3 CO streams . 7
5.3.1 Thermodynamics . 7
5.3.2 Chemical reactions . 7
6 Concept development and design criteria . 8
6.1 General . 8
6.2 Safety philosophy . 8
6.3 Reliability and availability of CO stream pipeline systems . 8
6.4 Short-term storage reserve . 9
6.5 Access to the pipeline system . 9
6.6 System design principles . 9
6.6.1 General . 9
6.6.2 CO stream specification . 9
6.6.3 Pressure control and protection system . 11
6.7 General principles to avoid internal pipeline corrosion . 11
6.7.1 Particular aspects related to CO and CO streams . 11
2 2
6.7.2 Maximum water content . 11
6.7.3 Avoidance of hydrate formation . 11
6.7.4 Measurement of water content in the CO stream . 12
6.8 Flow assurance . 12
6.8.1 General . 12
6.8.2 Operation under single-phase flow conditions during normal operation . 12
6.8.3 Pipeline operation under multi-phase flow conditions during transient operations . 13
6.8.4 Planned and unscheduled pipeline pressure release . 13
6.8.5 Reduced flow capacity . 14
6.8.6 Available transport capacity . 14
6.8.7 Flow coating . 14
6.8.8 External thermal insulation . 15
6.8.9 Leak detection . 15
6.8.10 Fugitive emissions . 15
6.8.11 Impurities . 15
6.9 Pipeline layout . 16
6.9.1 Vent stations . 16
6.9.2 Block valve stations . 16
6.9.3 Pumping and compressor stations . 16
6.9.4 In-line inspection . 16
iv
6.9.5 Onshore vent facility design. 17
6.9.6 Offshore vent facilities . 18
7 Materials and pipeline design . 18
7.1 General . 18
7.2 Internal corrosion . 18
7.3 Pipeline system materials . 18
7.3.1 Steel selection . 18
7.3.2 External coating . 18
7.3.3 Non-metallic materials . 19
7.3.4 Lubricants . 19
8 Wall thickness calculations . 19
8.1 Calculation principles . 19
8.1.1 Design loads . 19
8.1.2 Minimum wall thickness . 20
8.1.3 Minimum wall thickness against internal pressure . 20
8.1.4 Minimum wall thickness against dynamic pressure alterations . 20
8.1.5 Minimum wall thickness, t , against running ductile fracture for gas phase pipelines 20
minDF
8.1.6 Minimum wall thickness, tminDF, against running ductile fracture for dense phase
pipelines . 21
8.1.7 Fracture toughness . 21
8.1.8 Overview of the different aspects of wall thickness determination . 21
8.2 Additional measures . 26
8.2.1 Dynamic loads due to operation (alternating operation pressure) . 26
8.2.2 Topographical profile . 26
8.2.3 Fracture arrestors . 26
8.2.4 Offshore pipelines . 26
9 Construction . 26
9.1 General . 26
9.2 Pipeline pre-commissioning . 27
9.2.1 Overview . 27
9.2.2 Pipeline dewatering and drying . 27
9.2.3 Preservation before pipeline commissioning . 27
10 Operation . 27
10.1 General . 27
10.2 Pipeline commissioning . 27
10.2.1 Initial or baseline inspection . 27
10.
...
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