EN 777-4:2009

SLOVENSKI STANDARD
01-julij-2009
1DGRPHãþD
SIST EN 777-4:1999
SIST EN 777-4:1999/A1:2002
SIST EN 777-4:1999/A2:2002
SIST EN 777-4:1999/A3:2003
6WURSQDFHYQDVHYDOD]YHþSOLQVNLPLJRULOQLNL]DQHVWDQRYDQMVNHSURVWRUHGHO
6LVWHP+9DUQRVW
Multi-burner gas-fired overhead radiant tube heater systems for non-domestic use - Part
4: System H - Safety
Gas-Systeme-Heizstrahler - Dunkelstrahlersysteme mit mehreren Brennern mit Gebläse
für gewerbliche und industrielle Anwendung - Teil 4: System H - Sicherheit
Tubes radiants suspendus a multi-bruleurs utilisant les combustibles gazeux a usage
non-domestique - Partie 4 : Systeme H - Sécurité
Ta slovenski standard je istoveten z: EN 777-4:2009
ICS:
97.100.20 Plinski grelniki Gas heaters
2003-01.Slovenski inštitut za standardizacijo. Razmnoževanje celote ali delov tega standarda ni dovoljeno.

EUROPEAN STANDARD
EN 777-4
NORME EUROPÉENNE
EUROPÄISCHE NORM
March 2009
ICS 91.140.40 Supersedes EN 777-4:1999
English Version
Multi-burner gas-fired overhead radiant tube heater systems for
non-domestic use - Part 4: System H - Safety
Tubes radiants suspendus à multi-brûleurs utilisant les Gasgeräte-Heizstrahler Dunkelstrahlersysteme mit
combustibles gazeux à usage non-domestique - Partie 4 : mehreren Brennern mit Gebläse für gewerbliche und
Système H - Sécurité industrielle Anwendung - Teil 4: System H - Sicherheit
This European Standard was approved by CEN on 24 January 2009.
CEN members are bound to comply with the CEN/CENELEC Internal Regulations which stipulate the conditions for giving this European
Standard the status of a national standard without any alteration. Up-to-date lists and bibliographical references concerning such national
standards may be obtained on application to the CEN Management Centre or to any CEN member.
This European Standard exists 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 Management Centre has the same status as the
official versions.
CEN members are the national standards bodies of Austria, Belgium, Bulgaria, Cyprus, Czech Republic, Denmark, Estonia, Finland,
France, Germany, Greece, Hungary, Iceland, Ireland, Italy, Latvia, Lithuania, Luxembourg, Malta, Netherlands, Norway, Poland, Portugal,
Romania, Slovakia, Slovenia, Spain, Sweden, Switzerland and United Kingdom.
EUROPEAN COMMITTEE FOR STANDARDIZATION
COMITÉ EUROPÉEN DE NORMALISATION
EUROPÄISCHES KOMITEE FÜR NORMUNG
Management Centre: Avenue Marnix 17, B-1000 Brussels
© 2009 CEN All rights of exploitation in any form and by any means reserved Ref. No. EN 777-4:2009: E
worldwide for CEN national Members.

Contents Page
Foreword . 4
1 Scope. 5
2 Normative references . 5
3 Terms and definitions . 6
3.1 System and its constituent parts . 6
3.2 Combustion circuit . 8
3.3 Adjusting, control and safety devices . 9
3.4 System operation . 10
3.5 Gases. 13
3.6 Conditions of operation and measurement. 14
3.7 Country of destination . 14
4 Classification of systems . 15
4.1 Classification according to the nature of the gases used (categories) . 15
4.2 Classification according to the gases capable of being used . 15
4.3 Classification according to the mode of evacuation of the combustion products . 17
5 Constructional requirements . 17
5.1 General . 17
5.2 Requirements for adjusting, control and safety devices . 22
5.3 Ignition devices . 26
5.4 Main burners . 27
5.5 Pressure test points . 27
5.6 Injectors . 27
6 Operational requirements . 28
6.1 Soundness . 28
6.2 Heat inputs . 28
6.3 Limiting temperatures . 28
6.4 Ignition, cross-lighting and flame stability . 29
6.5 Pressure regulator . 29
6.6 Combustion . 29
6.7 Prolonged performance. 30
6.8 Measurements of oxides of Nitrogen, NO . 31
x
7 Test methods . 31
7.1 General . 31
7.2 Construction and design . 38
7.3 Safety of operation . 39
7.4 Other pollutants . 53
8 Marking and instructions . 56
8.1 Marking of the system and the packaging . 56
8.2 Instructions . 60
8.3 Presentation . 64
9 Evaluation of conformity of POCEDs and their associated terminals . 64
9.1 General . 64
9.2 Type testing . 64
9.3 Factory production control (FPC) . 65
Annex A (informative) National situations . 67
A.1 General . 67
A.2 Categories listed in the body of the standard and marketed in different countries . 67
A.3 Appliance supply pressures corresponding to the categories given in A.2 . 69
A.4 Special categories marketed nationally or locally . 71
A.5 Test gases corresponding to the special categories given in A.4 . 75
A.6 Gas connections in the various countries . 76
A.7 Flue connections in the various countries . 78
Annex B (informative) System H . 79
Annex C (informative) Equivalence rules . 80
C.1 Conversion to categories within a restricted Wobbe Index range . 80
C.2 Conversion to categories within an identical Wobbe Index range . 80
C.3 Conversion to categories within a wider Wobbe Index range. 81
Annex D (informative) Calculation of the mass flow rate of flue gases . 82
D.1 Flue gas mass flow rate. 82
D.2 Quantity of air in the flue gas . 82
D.3 Flue gas excess air ratio (λ) . 83
D.4 Quantity of water vapour in the flue gas . 83
D.5 Quantity of Nitrogen in the flue gas . 83
D.6 Quantity of Oxygen in the flue gas . 83
D.7 Dry quantity of flue gas . 84
D.8 Quantity of carbon dioxide in the flue gas . 84
Annex E (informative) Identification of gas types in use in various countries . 86
Annex F (normative) Special national conditions . 87
F.1 General . 87
Annex G (informative) Example of calculation of the weighting factors for a system with
several rates . 88
G.1 Appliance rates . 88
G.2 Weighting of Q = 20 . 88
pi,%
G.3 Weighting of Q = 40 . 88
pi,%
G.4 Weighting of Q = 60 . 88
pi,%
G.5 Weighting of Q = 70 . 89
pi,%
G.6 Total weighting . 89
Annex H (informative) Calculation of conversions of NO . 90
x
H.1 NO emission conversion factors. 90
x
H.2 NO Conversion — Calculation . 91
x
Annex I (informative) National situations of countries whose national bodies are CEN
associate members . 93
Annex J (informative) An example of sampling plans . 94
J.1 Sampling plans . 94
J.2 Inspection levels and procedures . 95
Annex K (informative) Flue determination . 96
K.1 General conditions of test . 96
K.2 Test conditions . 96
K.3 Test procedure . 96
K.4 Accuracy of measurement . 98
K.5 Calculation of Flue Loss. 98
Annex ZA (informative) Clauses of this European Standard addressing essential
requirements or other provisions of EU Directives . 101
Annex ZB (informative) Clauses of this European Standard addressing the provisions of
the EU Construction Products Directive . 104
ZB.1 Scope and relevant characteristics . 104
ZB.2 Procedure(s) for attestation of conformity of [construction products] . 106
ZB.3 CE marking and labelling . 109
Bibliography . 111

Foreword
This document (EN 777-4:2009) has been prepared by Technical Committee CEN/TC 180 “Domestic
and non-domestic gas fired air heaters and non-domestic gas fired overhead radiant heaters”, the
secretariat of which is held by AFNOR.
This European Standard shall be given the status of a national standard, either by publication of an
identical text or by endorsement, at the latest by September 2009, and conflicting national standards
shall be withdrawn at the latest by September 2009.
Attention is drawn to the possibility that some of the elements of this document may be the subject of
patent rights. CEN [and/or CENELEC] shall not be held responsible for identifying any or all such
patent rights.
This document supersedes EN 777-4:1999.
This revision modifies EN 777-4:1999. It has been prepared to incorporate requirements for
combustion products evacuation ducts, POCEDs, supplied as an integral part of the system to
support the EU Directive 89/106/EEC on construction products under mandate M/105. To this end the
systems within the scope of this standard are now defined as Type B rather than Type B .
52 22
Furthermore, the opportunity presented by this revision has been taken to update the standard in
respect to EN 437:2003.
This document has been prepared under a mandate given to CEN by the European Commission and
the European Free Trade Association, and supports essential requirements of EC Directive(s).
For relationship with EC Directive(s), see informative Annexes ZA and ZB, which are integral parts of
this document.
According to the CEN/CENELEC Internal Regulations, the national standards organizations of the
following countries are bound to implement this European Standard: Austria, Belgium, Bulgaria,
Cyprus, Czech Republic, Denmark, Estonia, Finland, France, Germany, Greece, Hungary, Iceland,
Ireland, Italy, Latvia, Lithuania, Luxembourg, Malta, Netherlands, Norway, Poland, Portugal, Romania,
Slovakia, Slovenia, Spain, Sweden, Switzerland and the United Kingdom.
1 Scope
This European Standard specifies the requirements and test methods for the construction, safety,
classification and marking of non-domestic gas-fired overhead radiant tube systems incorporating two or
more burner units with each burner under the control of an automatic burner control system, and
operated by a single fan providing a single flue outlet, called system H and referred to in the body of the
text as the “system”.
This standard is applicable to Type B systems (see 4.3) intended for use in other than domestic
dwellings, in which the supply of combustion air and the evacuation of the products of combustion is
achieved by mechanical means. This standard is applicable only to such systems that have fully pre-
mixed gas/air burners.
This standard is not applicable to:
a) systems designed for use in domestic dwellings;
b) outdoor systems;
c) systems of heat input in excess of 120 kW (based on the net calorific value of the appropriate
reference test gas);
d) systems having a draught diverter;
e) systems that are designed for continuous condensation within the flue system under normal
operating conditions;
f) systems having combustion products evacuation ducts that are non-metallic.
This standard is applicable to systems which are intended to be type tested. It also includes requirements
concerning the evaluation of conformity, including factory production control, but these requirements only
apply to POCEDs and their associated terminals.
NOTE Requirements for systems which are not intended to be type tested would need to be subject to
further consideration.
Requirements concerning the rational use of energy have not been included in this European Standard.
2 Normative references
The following referenced documents are indispensable for the application of this document. For dated
references, only the editions cited applies. For undated references, the latest edition of the referenced
document (including any amendments) applies.
EN 88-1:2007, Pressure regulators and associated safety devices for gas appliances - Part 1:
Pressure regulators for inlet pressures up to and including 500 mbar
EN 126:2004, Multifunctional controls for gas burning appliances
EN 161:2007, Automatic shut-off valves for gas burners and gas appliances
EN 257, Mechanical thermostats for gas-burning appliances
EN 298:2003, Automatic gas burner control systems gas burners and gas burning appliances with or
without fans
EN 437:2003, Test gases - Test pressures - Appliance categories
EN 10226-1:2004, Pipe threads where pressure tight joints are made on the threads – Part 1: Taper
external threads and parallel internal threads - Dimensions, tolerances and designation
EN 10226-2:2005, Pipe threads where pressure tight joints are made on the threads – Part 2: Taper
external threads and taper internal threads - Dimensions, tolerances and designation
EN 60335-1:2002, Household and similar electrical appliances – Safety - Part 1: General
requirements
EN 60335-2-102:2006, Household and similar electrical appliances – Safety - Part 2-102: Particular
requirements for gas, oil and solid-fuel burning having electrical connections
EN 60529:1992, Degrees of protection provided by enclosures (IP code)
EN 60584-1:1995, Thermocouples — Part 1: Reference tables
EN 60584-2:1993, Thermocouples — Part 2: Tolerances
EN ISO 228-1:2003, Pipe threads where pressure-tight joints are not made on the threads - Part 1:
Dimensions, tolerances and designation (ISO 228-1:2000)
EN ISO 3166-1:2006, Codes for the representation of names of countries and their subdivisions –
Part 1: Country codes (ISO 3166-1:2006)
EN ISO 6976:2005, Natural gas - Calculation of calorific values, density, relative density and Wobbe
index from composition (ISO 6976:1995 including Corrigendum 1:1997, Corrigendum 2:1997 and
Corrigendum 3:1999)
ISO 7005-1:1992, Metallic flanges - Part 1: Steel flanges
ISO 7005-2:1988, Metallic flanges - Part 2: Cast iron flanges
ISO 7005-3:1988, Metallic flanges - Part 3: Copper flanges and composite flanges
CR 1404:1994, Determination of emissions from appliances burning gaseous fuels during type testing
3 Terms and definitions
For the purposes of this standard the following terms and definitions apply.
3.1 System and its constituent parts
3.1.1
overhead radiant tube heater
gas fired appliance intended for installation above head level which is designed to heat the space
beneath by radiation by means of a tube or tubes, heated by the internal passage of combustion products
3.1.2
multi-burner systems
those radiant tube heater systems which employ two or more burner units with each unit incorporating
independent flame monitoring.
NOTE The units may be located in one or more sections of tubing. One or more fans may be used to assist in the
evacuation of products of combustion or the supply of combustion air
System H: system in which individual units without fans are connected to a common duct with a fan. One
or more burner units are situated in each branch tube (see Annex B).
3.1.3
branch tube
for the purposes of this part, a tube in which one or more burner units is/are situated and which only
contains the products of combustion generated by this, or these, burners
3.1.4
common duct
duct which receives products of combustion from two or more branch tubes for the purposes of
evacuation to the outside
3.1.5
individual burner unit
unit comprising a main burner and, if appropriate, an ignition burner. In addition, such components which
are necessary to ignite the burner(s), monitor the flame and control the gas supply to the burner(s) are
included in the unit
3.1.6
inlet connection
part of the system intended to be connected to the gas supply
3.1.7
mechanical joint
means of ensuring the soundness of an assembly of several parts e.g. metal to metal joints, conical
joints, toroidal sealing rings (“O” rings), flat joints without the use of liquids (e.g. pastes and tapes)
3.1.8
gas circuit
part of the burner unit that conveys or contains the gas between the burner unit gas inlet connection and
the burner(s)
3.1.9
restrictor
device with an orifice, which is placed in the gas circuit so as to create a pressure drop and thus reduce
the gas pressure at the burner to a predetermined value for a given supply pressure and rate
3.1.10
gas rate adjuster
component allowing an authorised person to set the gas rate of the burner to a predetermined value
according to the supply conditions
NOTE 1 Adjustment can be progressive (screw adjuster) or in discrete steps (by changing restrictors).
NOTE 2 The adjusting screw of an adjustable regulator is regarded as a gas rate adjuster.
NOTE 3 The action of adjusting this device is called “adjusting the gas rate”.
NOTE 4 A factory sealed gas rate adjuster is considered to be non-existent.
3.1.11
setting an adjuster
immobilizing a gas rate adjuster by such means as e.g. a screw, after the gas rate has been adjusted by
the manufacturer or installer
3.1.12
sealing an adjuster
term applied to any arrangement in respect of the adjuster such that any attempt to change the
adjustment breaks the sealing device or sealing material and makes this interference apparent
NOTE 1 A factory sealed adjuster is considered to be non-existent.
NOTE 2 A regulator is considered to be non-existent if it has been factory sealed, i.e. by the system
manufacturer in a position such that it is not operational in the range of the normal supply pressure corresponding
to the system category.
3.1.13
putting an adjuster or a control out of service
adjuster or a control (e.g. of temperature or pressure) is said to be “put out of service” if it is put out of
action and sealed in this position; the burner unit then functions as if this device has been removed
3.1.14
injector
component that admits the gas into a burner
3.1.15
main burner
burner that is intended to ensure the thermal function of the system and is generally called the burner
3.1.16
ignition device
means (e.g. flame, electrical ignition device or other device) used to ignite the gas at the ignition burner or
at the main burner
NOTE This device can operate intermittently or permanently.
3.1.17
ignition burner
burner whose flame is intended to ignite another burner
3.1.18
fully pre-mixed gas/air burner
pre-aerated burner system in which gas is mixed in a pre-determined and adjustable ratio with all of the
air necessary for combustion
3.1.19
aeration orifice
device in a burner unit enabling a volume of combustion air to enter the burner or point of combustion
consistent with the gas flow through the gas orifice and variable with downstream negative pressure
3.1.20
primary aeration adjuster
device enabling the primary air to be set at the desired value according to the supply conditions
3.1.21
system aeration adjuster
one or more devices enabling the air flow condition within a branch tube or common duct to be set to
design values
3.2 Combustion circuit
3.2.1
combustion chamber
enclosure inside which combustion of the air-gas mixture takes place
3.2.2
flue outlet
part of a Type B system that connects with a flue to evacuate the products of combustion
3.2.3
draught diverter
device placed in the combustion products circuit to reduce the influence of flue-pull and that of down-
draught on the burner performance and combustion
3.2.4
POCED
combustion products evacuation duct that is intended to be used only with a specific appliance/system;
this duct being either supplied with the appliance/system or specified in the manufacturer's instructions
3.3 Adjusting, control and safety devices
3.3.1
automatic burner control system
system comprising at least a programming unit and all the elements of a flame detector device
NOTE The various functions of an automatic burner control system may be in one or more housings.
3.3.2
programming unit
device which reacts to signals from control and safety devices, gives control commands, controls the
start-up sequence, supervises the burner operation and causes controlled shut-down, and if necessary
safety shut-down and lock-out.
NOTE The programming unit follows a predetermined sequence of actions and always operates in conjunction with
a flame detector device
3.3.3
programme
sequence of control operations determined by the programming unit involving switching on, starting up,
supervising and switching off the burner
3.3.4
flame detector
device by which the presence of a flame is detected and signalled
NOTE it can consist of a flame sensor, an amplifier and a relay for signal transmission. These parts, with the
possible exception of the actual flame sensor, may be assembled in a single housing for use in conjunction with a
programming unit
3.3.5
flame signal
signal given by the flame detector device, normally when the flame sensor senses a flame
3.3.6
flame simulation
condition which occurs when the flame signal indicates the presence of a flame when in reality no flame
is present
3.3.7
pressure regulator
device which maintains the outlet pressure constant independent of the variations in inlet pressure within
defined limits
3.3.8
adjustable pressure regulator
regulator provided with means for changing the outlet pressure setting
3.3.9
flame supervision device
device that, in response to a signal from the flame detector, keeps the gas supply open and shuts it off in
the absence of the supervised flame
3.3.10
range-rating device
component on the burner unit intended to be used by the installer to adjust the heat input of the burner
unit, within a range of heat inputs stated by the manufacturer, to suit the actual heat requirements of the
installation
This adjustment may be progressive (e.g. by use of a screw adjuster) or in discrete steps (e.g. by
changing restrictors).
3.3.11
zero regulator
device which maintains a specified downstream pressure between it and a gas orifice at zero pressure
within fixed limits independent of variation within a given range of upstream pressure and negative
pressure downstream of the gas orifice
3.3.12
automatic vacuum regulator
device which maintains a constant negative pressure at a specified position within the tube both at start-
up and at thermal equilibrium conditions
3.3.13
automatic shut-off valve
device that automatically opens, closes or varies the gas rate on a signal from the control circuit and/or
the safety circuit
3.4 System operation
3.4.1
heat input
Q
quantity of energy used in unit time corresponding to the volumetric or mass flow rates; the calorific value
used being the net or gross calorific value
NOTE The heat input is expressed in kilowatts (kW) (EN 437:2003).
3.4.2
nominal heat input
Q
n
the value of the heat input (kW) declared by the manufacturer

The term “regulator” is used in this case and for a volume regulator.
3.4.3
volume flow rate (V)
V
volume of gas consumed by the appliance in unit time during continuous operation
NOTE The volume flow rate is expressed in cubic metres per hour (m /h), litres per minute (l/min), cubic
3 3
decimetres per hour (dm /h) or cubic decimetres per second (dm /s) (EN 437:2003).
3.4.4
mass flow rate
M
mass of gas consumed by the appliance in unit time during continuous operation
NOTE The mass flow rate is expressed in kilograms per hour (kg/h) or grams per hour (g/h) (EN 437:2003).
3.4.5
flame stability
characteristic of flames which remain on the burner ports or in the flame reception zone intended by the
construction
3.4.6
flame lift
total or partial lifting of the base of the flame away from the burner port or the flame reception zone
provided by the design; flame lift may cause the flame to blow out (i.e. extinction of the air-gas mixture)
3.4.7
light-back
entry of a flame into the body of the burner
3.4.8
light-back at the injector
ignition of the gas at the injector, either as a result of light-back into the burner or by the propagation of a
flame outside the burner
3.4.9
sooting
phenomenon appearing during incomplete combustion and characterized by deposits of soot on the
surfaces or parts in contact with the combustion products or with the flame
3.4.10
yellow tipping
yellowing of the tip of the blue cone of an aerated flame
3.4.11
purge
forced introduction of air through the combustion chamber and flue passages in order to displace any
remaining fuel/air mixture and/or products of combustion
3.4.11.1
pre-purge
purge which takes place between the start signal and the energising of the ignition device
3.4.11.2
post-purge
purge which takes place immediately following shut-down
3.4.12
first safety time
interval between the ignition burner valve, the start gas valve or main gas valve, as applicable, being
energized and the ignition burner valve, start gas valve or main gas valve, as applicable, being de-
energized if the flame detector signals the absence of a flame at the end of this interval
3.4.13
second safety time
where there is a first safety time applicable to either an ignition burner or start gas flame only, the second
safety time is the interval between the main gas valve being energized and the main gas valve being de-
energized if the flame detector signals the absence of a flame at the end of this interval
3.4.14
extinction safety time
time which elapses between the moment when the supervised flame is extinguished and the moment
when the automatic burner control system initiates shut-down of the burner by removing power to the
automatic gas shut-off valves
3.4.15
start-gas flame
flame established at the start-gas rate either at the main burner or at a separate ignition burner
3.4.16
running condition of the system
condition in which the burner is in normal operation under the supervision of the programming unit and its
flame detector device
3.4.17
controlled shut-down
process by which the power to the gas shut-off valve(s) is removed immediately, e.g. as a result of the
action of a controlling function
3.4.18
safety shut-down
process which is effected immediately following the response of a safety control or sensor or the
detection of a fault in the automatic burner control system and which puts the burner unit out of
operation by immediately removing the power to the gas shut-off valve(s) and the ignition device
3.4.19
non-volatile lock-out
safety shut-down condition of the system, such that a restart can only be accomplished by a manual reset
of the system and by no other means
3.4.20
volatile lock-out
safety shut-down condition of the system, such that a restart can only be accomplished by either the
manual reset of the system, or a failure of the mains electrical supply and its subsequent restoration
3.4.21
spark restoration
process by which, following the loss of the flame signal, the ignition device will be switched on again
without the total interruption of the gas supply
NOTE This process ends with the restoration of the running condition or if there is no flame signal at the end
of the safety time, with volatile or non-volatile lock-out.

Where there is no second safety time, this is called the safety time.
3.4.22
automatic recycling
process by which, after a safety shut-down, a full start-up sequence is automatically repeated
NOTE This process ends with the restoration of the running condition or, if there is no flame signal at the
end of the safety time, or if the cause of the accidental interruption has not disappeared, with volatile or non-
volatile lock-out.
3.5 Gases
3.5.1
calorific value
quantity of heat produced by the complete combustion, at a constant pressure equal to 1 013,25 mbar, of
a unit volume or mass of gas, the constituents of the combustible mixture being taken at reference
conditions and the products of combustion being brought back to the same conditions
A distinction is made between:
a) the gross calorific value H in which the water produced by combustion is assumed to be
s
condensed
b) the net calorific value H in which the water produced by combustion is assumed to be in the
i
vapour state
NOTE The calorific value is expressed either in MJ/m of dry gas at the reference conditions or in MJ/kg of
dry gas (EN 437:2003).
3.5.2
relative density
d
ratio of the masses of equal volumes of dry gas and dry air at the same conditions of temperature and
pressure
3.5.3
Wobbe index
gross Wobbe index: W and net Wobbe index: W .
s i
ratio of the calorific value of a gas per unit volume and the square root of its relative density under the
same reference conditions. The Wobbe index is said to be gross or net according to whether the calorific
value used is the gross or net calorific value
NOTE The Wobbe index is expressed either in MJ/m of dry gas at the reference conditions or in MJ/kg of
dry gas (EN 437:2003).
3.5.4
test pressure
gas pressures used to verify the operational characteristics of appliances using combustible gases; they
consist of normal and limit pressures
NOTE Test pressures are expressed in mbar. 1 mbar = 10 Pa (EN 437:2003).
3,5.5
normal pressure
p
n
pressure under which the appliances operate in nominal conditions when they are supplied with the
corresponding reference gas
(EN 437:2003)
3.5.6
limit pressure
maximum limit pressure p and minimum limit pressure p
max min
pressures representative of the extreme variations in the appliance supply conditions

(EN 437:2003)
3.45.7
pressure couple
combination of two distinct gas distribution pressures applied by reason of the significant difference
existing between the Wobbe indices within a single family or group in which:
a) the higher pressure corresponds only to gases of low Wobbe index
b) the lower pressure corresponds to gases of high Wobbe index

(EN 437:2003)
3.6 Conditions of operation and measurement
3.6.1
reference conditions
in this standard the following reference conditions apply:
a) for calorific values, temperature: 15 °C;
b) for gas and air volumes dry, brought to 15 °C and to an absolute pressure of 1 013,25 mbar
3.6.2
cold condition
condition of the installation required for some tests and obtained by allowing the unlit burner unit to attain
thermal equilibrium at room temperature
3.6.3
hot condition
condition of the installation required for some tests and obtained by heating to thermal equilibrium at
nominal heat input
3.6.4
equivalent resistance
resistance to flow in mbar, measured at the outlet of the system, which is equivalent to that of the actual
flue
3.6.5
thermal equilibrium
operating state of the system corresponding to a particular setting of the input in which the flue gas
temperature does not change by more than ± 2 % (in °C) over a period of 10 min
3.7 Country of destination
3.7.1
direct country of destination
country for which the system has been certified and which is specified by the manufacturer as the
intended country of destination. At the time of putting the system on the market and/or installation, the
system shall be capable of operating, without adjustment or modification, with one of the gases
distributed in the country concerned, at the appropriate supply pressure
More than one country can be specified if the system, in its current state of adjustment, can be used in
each of these countries.
3.7.2
indirect country of destination
country for which the system has been certified, but for which, in its present state of adjustment, it is not
suitable. Subsequent modification or adjustment shall be made in order that it can be utilized safely and
correctly in this country
4 Classification of systems
4.1 Classification according to the nature of the gases used (categories)
Gases are classified into three families, possibly divided into groups according to the value of the
Wobbe index. Table 1 specifies the families and groups of gas used in this standard.
Table 1 — Gas classification
Gas Gas Group Gross Wobbe index
family (MJ/m ) at 15 °C and
1 013,25 mbar
Minimum Maximum
First A 22,4 24,8
Second 39,1 54,7
H 45,7 54,7
L 39,1 44,8
E 40,9 54,7
Third 72,9 87,3
B/P 72,9 87,3
P 72,9 76,8
B 81,8 87,3
4.2 Classification according to the gases capable of being used
4.2.1 Category I
Systems of Category I are designed exclusively for the use of gases of a single family or of a single
group.
a) Systems designed for use on first family gases only:
Category I : systems using only gases of Group A of the first family at the prescribed pressure (this
1a
category is not used).
b) Systems designed for use on second family gases only:
Category I : systems using only gases of Group H of the second family at the prescribed supply
2H
pressures.
Category I : systems using only gases of Group L of the second family at the prescribed pressures.
2L
Category I : systems using only gases of Group E of the second family at the prescribed pressures.
2E
Category I : systems using only gases of Group E of the second family, and operating with a
2+
pressure couple without adjustment on the system. The system gas regulator, if it exists, is not
operative in the range of the two normal pressures of the pressure couple.
c) Systems designed for use on third family gases only:
Category I : systems capable of using the third family gases (propane and butane) at the
3B/P
prescribed supply pressure.
Category I : systems capable of using the third family gases (propane and butane) and operating
3+
with a pressure couple without adjustment of the system. However, for certain types of system
specified in the particular standards adjustment of the primary combustion air may be permitted when
changing from propane to butane and vice versa. No gas pressure regulating device is permitted on
the system.
Category I : systems using only gases of Group P of the third family (propane) at the prescribed
3P
pressure.
4.2.2 Category II
Systems of Category II are designed for use on gases of two families.
a) Systems designed for use on ga
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