SIST EN ISO 21805:2023

SLOVENSKI STANDARD
oSIST prEN ISO 21805:2021
01-julij-2021
Navodilo za projektiranje, izbiro in vgradnjo prezračevalnih naprav za
zagotavljanje strukturne integritete namestitvenih prostorov, zaščitenih s sistemi
za gašenje s plinom (ISO/DIS 21805:2021)
Guidance on design, selection and installation of vents to safeguard the structural
integrity of enclosures protected by gaseous fire-extinguishing systems (ISO/DIS
21805:2021)
Anleitung für die Konstruktion, Auswahl und Installation von Entlüftungen zur
Gewährleistung der strukturellen Integrität von Gehäusen, die durch ortsfeste
Gaslöschanlagen geschützt sind (ISO/DIS 21805:2021)
Lignes directrices pour la conception, la sélection et l'installation d'évents pour préserver
l'intégrité structurelle des enceintes protégées par des systèmes fixes de lutte contre
l'incendie à gaz (ISO/DIS 21805:2021)
Ta slovenski standard je istoveten z: prEN ISO 21805
ICS:
13.220.10 Gašenje požara Fire-fighting
91.140.30 Prezračevalni in klimatski Ventilation and air-
sistemi conditioning systems
oSIST prEN ISO 21805:2021 en,fr,de
2003-01.Slovenski inštitut za standardizacijo. Razmnoževanje celote ali delov tega standarda ni dovoljeno.

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oSIST prEN ISO 21805:2021

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oSIST prEN ISO 21805:2021
DRAFT INTERNATIONAL STANDARD
ISO/DIS 21805
ISO/TC 21/SC 8 Secretariat: SA
Voting begins on: Voting terminates on:
2021-05-20 2021-08-12
Guidance on design, selection and installation of vents to
safeguard the structural integrity of enclosures protected
by gaseous fire-extinguishing systems
Lignes directrices pour la conception, la sélection et l'installation d'évents pour préserver l'intégrité
structurelle des enceintes protégées par des systèmes fixes de lutte contre l'incendie à gaz
ICS: 91.140.30; 13.220.10
THIS DOCUMENT IS A DRAFT CIRCULATED
This document is circulated as received from the committee secretariat.
FOR COMMENT AND APPROVAL. IT IS
THEREFORE SUBJECT TO CHANGE AND MAY
NOT BE REFERRED TO AS AN INTERNATIONAL
STANDARD UNTIL PUBLISHED AS SUCH.
IN ADDITION TO THEIR EVALUATION AS
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BEING ACCEPTABLE FOR INDUSTRIAL,
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STANDARDS MAY ON OCCASION HAVE TO
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POTENTIAL TO BECOME STANDARDS TO
WHICH REFERENCE MAY BE MADE IN
Reference number
NATIONAL REGULATIONS.
ISO/DIS 21805:2021(E)
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. ISO 2021

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oSIST prEN ISO 21805:2021
ISO/DIS 21805:2021(E)

COPYRIGHT PROTECTED DOCUMENT
© ISO 2021
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
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oSIST prEN ISO 21805:2021
ISO/DIS 21805:2021(E)

Contents Page
Foreword .iv
Introduction .v
1 Scope . 1
2 Normative references . 1
3 Terms and definitions . 1
4 Symbols and abbreviated terms . 2
5 Use and limitations . 3
6 Safety . 4
6.1 Structural safety . 4
6.2 Personnel safety . 4
7 System design — Pressure-relief venting . 4
7.1 General . 4
7.2 Extinguishant characteristics . 4
7.2.1 Pressure graphs . 5
7.3 Enclosure characteristics . 5
7.4 Pressure-relief vent paths . 6
7.5 Types of pressure-relief vents . 6
7.5.1 General. 6
7.5.2 Gravity vents . 6
7.5.3 Counterweighted flap vent . 7
7.5.4 Electrically operated vents . 7
7.5.5 Pneumatically operated vent . 8
7.5.6 Vent accessories . 8
7.6 Pressure-relief vent characteristics . 9
7.6.1 Vent efficiency . 9
7.6.2 Minimum opening pressure .10
7.6.3 Minimum closing pressure .10
7.6.4 Fire rating.10
7.7 Vent location and mounting .11
7.7.1 Vent location .11
7.7.2 Vent mounting .11
7.8 Pressure-relief vent area calculations .12
7.8.1 Use of agent-specific equations .12
7.8.2 Vent area requirement (non-liquefiable gases and CO ) .13
2
7.8.3 Vent area requirements (liquefiable gases) .16
7.8.4 Leakage .21
7.9 Cascade venting calculations .21
7.9.1 Example calculation 3 . .23
7.9.2 Cascade vent arrangements .24
7.9.3 Venting into adjacent enclosures .24
8 System design — Post-discharge venting .26
9 Acceptance .27
10 Service and maintenance .27
Annex A (informative) Development of Agent Specific Equations for Liquefiable Gases .28
Annex B (normative) Method for Development of Agent Specific Equations for Liquefiable
Gases .32
Bibliography .34
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oSIST prEN ISO 21805:2021
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Foreword
ISO (the International Organization for Standardization) is a worldwide federation of national standards
bodies (ISO member bodies). The work of preparing International Standards is normally carried out
through ISO technical committees. Each member body interested in a subject for which a technical
committee has been established has the right to be represented on that committee. International
organizations, governmental and non-governmental, in liaison with ISO, also take part in the work.
ISO collaborates closely with the International Electrotechnical Commission (IEC) on all matters of
electrotechnical standardization.
The procedures used to develop this document and those intended for its further maintenance are
described in the ISO/IEC Directives, Part 1. In particular, the different approval criteria needed for the
different types of ISO documents should be noted. This document was drafted in accordance with the
editorial rules of the ISO/IEC Directives, Part 2 (see www .iso .org/ directives).
Attention is drawn to the possibility that some of the elements of this document may be the subject of
patent rights. ISO shall not be held responsible for identifying any or all such patent rights. Details of
any patent rights identified during the development of the document will be in the Introduction and/or
on the ISO list of patent declarations received (see www .iso .org/ patents).
Any trade name used in this document is information given for the convenience of users and does not
constitute an endorsement.
For an explanation of the voluntary nature of standards, the meaning of ISO specific terms and
expressions related to conformity assessment, as well as information about ISO's adherence to the
World Trade Organization (WTO) principles in the Technical Barriers to Trade (TBT), see www .iso .org/
iso/ foreword .html.
This document was prepared by Technical Committee ISO/TC 21, Equipment for fire protection and
firefighting, Subcommittee SC 8, Gaseous media and firefighting systems using gas.
This edition cancels and replaces ISO/TS 21805: 2018, which has been technically revised.
Any feedback or questions on this document should be directed to the user’s national standards body. A
complete listing of these bodies can be found at www .iso .org/ members .html.
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oSIST prEN ISO 21805:2021
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Introduction
The guidance presented here is based on the results of a joint research program conducted in 2006 and
2007 by several fire protection system manufacturers and interested parties. The program of work
consisted of several series of tests to evaluate the peak pressure response and pressure-relief vent
area effects for each agent addressed in this document. The key data used in the development of this
document were the values of peak enclosure pressure response (PMAX) at each value of the volume-
normalized pressure-relief vent area of the test enclosure, hereinafter referred to as the “leakage-to-
volume ratio” or LVR. Other test parameters (enclosure temperature, agent quantity, discharge time,
and humidity) were held constant or varied in a specified manner. For each test series employing a
single agent, the several pairs of LVR and resultant PMAX values were graphically analysed, and a best-
fit correlation curve was determined.
The LVR vs. PMAX correlation curve for each agent or system forms the basis of the associated
equations in cases where the discharge of the agent results in cooling the air temperature below its
dew point. (See Humidity effects and humidity correction factor below.) In most cases, only halocarbon
agents cause sufficient cooling to cause humidity related effects on the peak enclosure pressure. Thus,
a correction for humidity effects is included in the equations for estimating vent area and maximum
pressure on the discharge of the following agents:
— FK-5-1-12
— HFC-23
— HFC-125
— HFC-227ea
The humidity corrections used in this document are based on the results of tests conducted with HFC-
227ea at different conditions of humidity.
The resulting values for humidity correction will be assumed to be equally applicable to the agents FK-
5-1-12, HFC-125 and HFC-23 until further data or analysis indicate otherwise.
The correlations of LVR to maximum negative pressure and maximum positive pressure were based
on test work performed in a test chamber at a relative humidity (RH) of approximately 38 %. If the RH
in a protected enclosure differs from 38 % then a correction to the estimated maximum negative and
positive pressures may be required. See 7.8 and 7.9 for further information on the effect of humidity.
The temperature of the test enclosure was 21°CF (nominal) for all tests that form the basis of the
estimating methods given in this document.
In conducting the research program, described above, a large number of different venting arrangements
were created in the test enclosure. The equivalent leakage area (ELA) for each test was determined by
a “door fan test” and data analysis. The average enclosure pressure in effect during the many door fan
tests varied from test to test. All values of ELA were normalized to an equivalent enclosure differential
pressure of 125 Pa. The resulting enclosure correlations of peak pressure vs. LVR, and any resulting
estimate of enclosure pressure-relief vent area, reflect a pressure-relief vent area calculated at an
effective enclosure pressure of 125 Pa for a vent with a discharge coefficient of 0,61.
The effectiveness of a gaseous total flooding firefighting system depends, in part, on retention of
the air-extinguishant mixture within the protected volume for a period of time. Retention of the
extinguishant-air mixture requires that gas exchange (“leakage”) between the enclosure and the
ambient environment be restricted. To limit the rate of gas exchange the enclosure boundary should
have a high degree of integrity. To put it another way, the total of the areas of the various penetrations
in an enclosure’s bounding surfaces should be low, at least during the gas-retention period (hold time)
after the end of the extinguishant discharge.
The addition of a gaseous firefighting extinguishant to an enclosure having limited pressure-relief vent
area will naturally result in a change of pressure therein. If the enclosure is sealed too tightly during the
extinguishant discharge, i.e. too little pressure-relief vent area, the pressure change could exceed the
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oSIST prEN ISO 21805:2021
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structural strength of one or more of its bounding surfaces — windows, doors, walls, ceiling. Conversely,
if the enclosure has too much pressure-relief vent area then gas exchange with the ambient atmosphere
will occur rapidly, leading to a short retention time of the extinguishant within the protected volume.
Thus, the use of gaseous firefighting systems should address two performance considerations:
a) Pressure management within the protected volume during the period of extinguishant
discharge, and;
b) Retention of the extinguishant-air mixture within the enclosure for a specified period of time after
the completion of the discharge.
This document provides guidance for limiting pressure extremes in an enclosure during the discharge
of a clean agent fire extinguishing system. This document does not provide the information necessary to
determine all of the requirements related to the design, installation, service, maintenance, inspection,
test, and/or requalification of fire suppression systems.
Some limitations and restrictions apply to the use of the equations contained in this document. Please
refer to the text and notes that follow.
The information in this document does not supersede the manufacturer’s guidance. The information
contained in this document is presented as supplementary to the guidance provided by the respective
system manufacturers. Guidance from the system manufacturer should always be followed and used
for purposes of system design, installation, operation, and maintenance.
It has been assumed in the preparation of this document that the execution of its provisions is entrusted
to people appropriately qualified and experienced in the specification, design, installation, testing,
approval, inspection, operation and maintenance of systems and equipment, for whose guidance it has
been prepared, and who can be expected to exercise a duty of care to avoid unnecessary release of
extinguishant.
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oSIST prEN ISO 21805:2021
DRAFT INTERNATIONAL STANDARD ISO/DIS 21805:2021(E)
Guidance on design, selection and installation of vents to
safeguard the structural integrity of enclosures protected
by gaseous fire-extinguishing systems
1 Scope
This document provides guidance on fulfilling the requirements contained in ISO 6183:2009, 6.4.1 and
7.4.1 and ISO 14520-1:2015, 5.2.1 (h) and 5.3 (h), in respect to over and under pressurization venting
and post-discharge extract.
It considers the design, selection and installation of vents to safeguard the structural integrity of
enclosures protected by fixed gaseous extinguishing systems and the post-discharge venting provisions
where used.
2 Normative references
The following documents are referred to in the text in such a way that some or all of their content
constitutes requirements of this document. For dated references, only the edition cited applies. For
undated references, the latest edition of the referenced document (including any amendments) applies.
ISO 14520-1, Gaseous fire-extinguishing systems — Physical properties and system design — Part 1:
General requirements
EN 15004-1, Fixed firefighting systems — Gas extinguishing systems — Part 1: Design, installation, and
maintenance
3 Terms and definitions
For the purposes of this document, the following terms and definitions apply.
ISO and IEC maintain terminological databases for use in standardization at the following addresses:
— ISO Online browsing platform: available at https:// www .iso .org/ obp
— IEC Electropedia: available at https:// www .electropedia .org/
Note 1 to entry For the purposes of this document, the term “bar” signifies “gauge”, unless otherwise indicated.
Concentrations or quantities expressed in percentages (%) signify by volume unless otherwise indicated.
3.1
back pressure
pressure downstream of a vent
3.2
fire damper
device designed to prevent the spread of fire
3.3
free pressure-relief vent area
sum of the free pressure-relief vent areas of the pressure-relief vents provided
Note 1 to entry: Note to entry: This is determined by the gross pressure-relief vent area x the vent efficiency.
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3.4
gross pressure-relief vent area
total area of the pressure-relief vent
3.5
negative pressure
pressure in the protected room which is lower than the pressure immediately outside the enclosure
boundary
3.6
peak pressure
maximum pressure (positive and negative) generated within an enclosure caused by the discharge of
the gaseous agent
3.7
positive pressure
pressure immediately outside the enclosure boundary
3.8
enclosure strength
specified differential pressure limit for the protected enclosure
3.9
pressure-relief area
sum of the free pressure-relief vent area and the enclosure leakage area
3.10
pressure-relief vent
device that provides a flow path through an enclosure boundary to limit the pressure therein
4 Symbols and abbreviated terms
2 2
A pressure-relief vent area to limit negative pressure to a specified P , cm (in )
N N
2 2
A pressure-relief vent area to limit positive pressure to a specified P , cm (in )
P P
C agent design concentration, in percent by volume
M is the molecular weight of air = 0,029 (kg/mol)
AIR
M the molecular weight of the agent, (kg/mol)
AGT
Q minimum design quantity of agent (kg)
P pressure (Pa)
P negative pressure, psf (Pa)
N
P positive pressure, psf (Pa)
P
P and P represent either
N P
— Design pressure limits for estimating A or A , or
N P
— Estimates of maximum values of P or P for given values of A or A
N P N P
R gas law constant, 8,314 (J/mol-K)
% RH relative humidity in hazard space at 21 °C (70 °F), %
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3
s the specific volume of the agent at the design temperature (m /kg)
3
s the specific volume of the homogenous agent-air mixture (m /kg), which is the inverse of the density
H
t agent discharge time, s
3
V the volume of the protected space (m )
3
ρ agent-air mixture density (kg/m )
H
5 Use and limitations
This document is for the use by those competent in the design, installation, servicing, and maintenance
of fixed gaseous firefighting systems. It also serves as guidance for those involved in the design,
construction, and operation of buildings in which such systems are installed.
It does not replace the need for the person responsible for the design, construction, and operation of the
building to fulfil their obligations in respect to providing adequate structural provisions.
There may be other trades and services involved in the complete system and the document is limited to
providing the guidance outlined in the document and does not purport to be an expert in all areas.
After applying the enclosure peak pressure and pressure-relief vent area analysis of this document,
the user may conclude that an enclosure may require additional pressure-relief vent area to avoid
exceeding specified maximum pressure values upon discharge of a gaseous agent system. If that is the
case, it is recommended that the user advise the supplier of a supplemental venting device that such
device be specified and selected by use of this document.
The maximum pressure developed in an enclosure on the discharge of a clean agent fire extinguishing
system is affected by several characteristics of the system itself and the enclosure being protected. Of
particular importance are the thermodynamic properties of the agent and the discharge characteristics
of the hardware. Each of the following sections contains correlation equations that are specific to the
agent type and manufacturer’s hardware. The equations can be used to make estimates of the following:
a) enclosure pressure-relief vent area given a specified enclosure pressure limit;
b) maximum positive or negative pressure developed in an enclosure given a stated or calculated
pressure-relief vent area.
NOTE The formulae in this document for halocarbon agents have a limited range of applicability based on the
parametric limitations of the data from which they were derived. Table 1 indicates the applicable limits of design
concentration, discharge time, and enclosure pressure response for the use of this document. The maximum
peak pressure estimates (both positive and negative) based on data obtained for each agent are given in Table 1.
Caution: It is physically possible to develop pressures greater than those covered by this document
during system discharges.
Table 1 — Summary of equation application limits
Agent Minimum Maximum Minimum Maximum Maximum Maximum
agent agent discharge discharge over-pres- under pres-
time time sure pfs (Pa) sure pfs (Pa)
Conc Conc
% vol % vol
FK-5–1-12 4,2 6 6 10 5 (239) 25 (1 197)
HFC-23 18 30 6 10 30 (1 437) n/a
HFC-125 8 10,5 6 10 10 (479) 10 (479)
HFC-227ea 6,25 10,5 6 10 8 (383) 20 (958)
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6 Safety
6.1 Structural safety
The provision of correctly designed and engineered pressure venting of enclosures protected by gaseous
fire-extinguishing systems is essential to prevent the possibility of failure of structural integrity. This is
essential to mitigate forces exerted by the changes in enclosure pressure when gaseous fighting media
are discharged into an enclosure.
6.2 Personnel safety
The operation of pressure-relief vents or extract systems requires the displacement of mixtures
of air/gaseous media from a protected enclosure to the atmosphere or another area not necessarily
protected. The safety issue may arise due to exposures to the extinguishants themselves or products of
combustion and/or extinguishant breakdown products. Also, any hazards arising from the operation of
the over/under pressurization vents themselves should be considered.
7 System design — Pressure-relief venting
7.1 General
The basic design principle is to limit the pressure excursions imposed on the structure of the protected
enclosure by the discharge of gaseous extinguishant to that within the limits the enclosure can
withstand.
A room integrity test can be used to determine the equivalent leakage area, or simply the” vent” area
that exists at the time of evaluation. The methods of this document can use the known or estimated
pressure-relief vent area to estimate the maximum pressure that will be developed on the discharge
of a clean agent system. If the estim
...