BRITISH STANDARD BS EN 60695 5 1 2003 Fire hazard testing — Part 5 1 Corrosion damage effects of fire effluent — General guidance The European Standard EN 60695 5 1 2003 has the status of a British St[.]
Trang 1Fire hazard testing —
The Eur opean Stand rd EN 6 6 5-5-1:20 3 has the status of a
BritishStand rd
ICS 2 0 0
Trang 2Th is Br itish Stan ard was
publshed u der the authority
of the St an ards Polcy an
Strate y Commite on
2 Ju e2 0
© BSI 2 Ju e 0 3
ISBN 0 5 04 0 6 8
This British Stand rd is th e oficial Eng lish lang uag e v er ion of
EN6 6 5-5-1:20 3 It is identical with IEC6 6 5-5-1:20 2 It super ed es
BSEN6 6 5-5-1:19 3 which is withdrawn
The UK p rticip tion in its prep ration was entrusted to Tech ical Commit e
GEL/89, Fir e hazar d testing, which has the responsibi ty to:
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request to its sec etary
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This d ocument comprises a f ont cov er, an inside f ont cov er, the EN title p g e,
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Trang 3EUROPÄ ISCHE NORM February 2003
Euro e n Commite for Electrotec nic al St an ardiz at ion
Comité Euro é n de Normalsation Elec trotec hniq e
Euro äis hes Komite für Elek trot echnis he Normu g
Ce ntra l Secreta ria t: ru d Sta ssa rt 35, B - 105 0 Bru sels
© 2 0 CENELEC - A ll rig t s of e ploit at io in a y form a d b a y me n re erv ed worldwid for CENELEC memb rs
Es ais relat ifs aux risques du feu
Part ie 5-1: Efet s des dommages
de corosio d s efluent s du feu
-Guide général
(CEI 606 5-5-1:20 2)
Prüfungen z r Beurt eiung
der Brandg fa r
Tei 5-1: Kor osions c hädigung
durc h R auc h und/ oder Brandgase
-A llgemeiner Leitfaden
(IEC 60695-5-1:2002)
T his Euro e n Stan ard was a prov ed b CENELEC o 2 0 -0 -01 CENELEC memb rs are b u d to
comply wit h the CEN/ CENELEC Intern l Reg latio s which s p late t he con itio s for givin t his Euro e n
St an ard the st atus of a n tio al stan ard witho t a y alt erat io
Up-t o-d te lsts a d biblo ra hical refere ces concernin su h n t io al st an ards ma b o tain d o
a plcatio t o the Ce tral Sec retariat or to a y CENELEC memb r
This Euro e n St an ard e ists in thre oficial v rsio s (En lsh, Fre c , Germa ) A v rsio in a y other
la g a e ma e b t ra slatio u d r t he resp nsibi ty of a CENELEC memb r into its own la g a e a d
n t ifie to the Ce tral Secretariat h s t he same st atus as the oficial v rsio s
CENELEC memb rs are t he n t io al ele t rot ec hnic l c mmit tees of Aust ria, Belgium, Czech Rep blc ,
De mark, Finla d, Fra ce, Germa y, Gre ce, Hu g ry, Ic ela d, Irela d, Italy, L x mb urg, Malta,
Netherla ds, Norwa , Portug l, Slo a ia, Sp in, Swe e , Switz erla d a d United Kin d m
Trang 4The tex t of doc ument 8 /5 6/FDIS, fut ure edit ion 2 of IEC 6 6 5-5-1, pre ared by IEC TC 8 , Fire
hazard t estin , was s bmitt d to the IEC-CENELEC p ralel vote an was a prov ed by CENELEC as
EN 6 6 5-5-1 on 2 0 -0 -01
This Euro e n Stan ard s p rsedes EN 6 6 5-5-1:19 3
The folowin dates were fix ed:
– latest date by whic h the EN has t o b implement ed
at national level by publc ation of an identical
– latest date by whic h the national st an ard c onflc t in
This Euro e n St an ard s ould b re d in conju ct ion w it h IEC 6 6 5-5-2 an IEC 6 6 5-5-3
An ex es desig at ed "normat iv e" are p rt of t he b d of t he st an ard
In t his st an ard, an e ZA is normat iv e
An e ZA has b en ad ed by CENELEC
Endorseme t not ic
The t ex t of t he Int ernat ional St an ard IEC 6 6 5-5-1:2 0 was a prov ed by CENELEC as a
Euro e n Stan ard w it hout an modificat ion
In t he oficial v ersion, for Biblogra h , t he folow in not e has t o b ad ed for t he st an ard in icat ed:
ISO 7 8 NOT E Harmo ize as EN ISO 7 8 :19 5 (n t mo ifie )
Trang 5INTRODUCTION 4
1 Sco e 5
2 Normative ref eren es .5
3 Definition 6
4 Fire s enarios an f ire models 7
5 General asp cts of the cor osivity of f ire eff l ent 8
5.1 Cor osion damage s enarios 8
5.2 Typ s of cor osion damage ef fects .9
5.2.1 Metal los 9
5.2.2 Movin p rts b comin immo i e 9
5.2.3 Brid in of con u tor circ its 9
5.2.4 Formation of a non-con u tin layer on contact s r aces 9
5.3 Factors af fectin cor osivity .10 5.3.1 The nature of f ire eff l ent 10 5.3.2 The cor osion en ironment .1
6 Prin iples of cor osion damage me s rement .1
6.1 Introd ction .1
6.2 Generation of the f ire ef fluent .12 6.2.1 Selection of the test sp cimen whic is to b burned .12 6.2.2 Selection of the fire model 12 6.3 The as es ment of cor osive p tential 12 6.3.1 General .12 6.3.2 In irect as es ment .12 6.3.3 Simulated prod ct testin 13 6.3.4 Prod ct testin 13 6.4 Con ideration of cor osivity test method 14 7 Relevan e of data to hazard as es ment .16 An ex ZA (normative) Normative referen es to international publcation with their cor esp n in Euro e n publ cation 17 Bibl ogra h 19 Fig re 1 – Dif ferent stages in the develo ment of a fire within a comp rtment .8
Fig re 2 – Evaluation an con ideration of cor osion damage test method 15 Ta le 1 – General clas if i ation of fires (ISO/TR 912 -1) 8
Ta le 2 – Summary of cor osivity test method 13
Trang 6INTRODUCTION
The ris of fire s ould b con idered in any electrical circ it With regard to this ris , the
circ it an eq ipment desig , the selection of comp nents an the c oice of materials s ould
contribute toward red cin the lkel ho d of f ire even in the event of f orese a le a normal
u e, malf un tion or fai ure The practical aim s ould b to prevent ig ition cau ed by electrical
malfu ction but, if ig ition an fire oc ur, to control the fire prefera ly within the b u d of the
en los re of the electrotec nical prod ct
Al fire ef f luent is cor osive to some degre an the level of p tential to cor ode de en s on
the nature of the fire, the combination of combu tible materials in olved in the f ire, the nature
of the s bstrate u der atac , an the temp rature an relative h midity of the en ironment in
whic the cor osion damage is takin place There is no eviden e that fire eff l ent f rom
electrotec nical prod cts of fers gre ter ris of cor osion damage than the f ire ef fluent f rom other
prod cts s c as f urnis in s, bui din materials, etc
The p r orman e of electrical an electronic comp nents can b ad ersely aff ected by
cor osion damage when s bjected to fire ef f luent A wide variety of combination of smal
q antities of ef fluent gases, smoke p rticles, moisture an temp rature may provide
con ition for electrical comp nent or s stem fai ures f rom bre kage, overhe tin or s ortin
Evaluation of p tential cor osion damage is p rtic larly imp rtant for hig value an saf
ety-related electrotec nical prod cts an in talation
Tec nical commite s resp n ible for the prod cts wi c o se the test s) an sp cify the level
of severity
The stu y of cor osion damage req ires an interdis iplnary a pro c in olvin c emistry,
electricity, ph sic , mec anical en ine rin , metal urg an electroc emistry In the
pre-p ration of this part of IEC 6 69 -5, al of the a ove have b en con idered
IEC 6 6 5-5-1 defines the s o e of the g idan e an in icates the field of a pl cation
IEC 6 6 5-5-2 provides a s mmary of test method in lu in relevan e an u ef ulnes
IEC 6 6 5-5-3 provides detais of a smal -s ale test method f or the me s rement of le kage
c r ent an metal los cau ed by fire ef fluent
Trang 7a) general asp cts of cor osion damage test method ;
b) method of me s rement of cor osion damage;
c) con ideration of test method ;
d) relevan e of cor osion damage data to hazard as es ment
One of the resp n ibi ties of a tec nical commite is, wherever a plca le, to make u e of
b sic safety publcation in the pre aration of its publ cation
2 Normative references
The f ol owin ref eren ed doc ments are in isp n a le f or the a plcation of this doc ment
For dated ref eren es, only the edition cited a pl es F r u dated ref eren es, the latest edition
of the referen ed doc ment (in lu in an amen ments) a pl es
IEC 6 6 5-1-1:19 9, Fire h z rd test ing – Part 1-1: Guid an e for a s s ing the fire h z rd
of el ectrotec nic l produ ts – Ge eral g id el i e
IEC/TS 6 6 5-5-2:2 0 , Fire h z rd te t in – Part 5-2: Coro ion dama e efe ts of fire
eflu nt – Summary a d relevan e of test methods
IEC/TS 6 6 5-5-3, Fire h z rd testing – P art 5-3: Coro ion d ama e efe ts of fire eflu nt –
L akag c r e t a d metal l os te t method
1
IEC 6 7 4-1:19 4, Te t o g s s evolved d uring c mb st io of materials fom c bl es –
Part 1: Determinat ion of t he amo nt of h log n a id g s
IEC 6 7 4-2:19 1, Te t o g s s evolv d d uring c mb st ion of ele tric c ble – P art 2:
Determination of d egre ofa id ity of g s s evolved during t he c mb st ion of mat erials tak en
fom el ectric c bl es b me s ring pH a d c nd uctivity
IEC 6 7 4-2, Amen ment 1 (19 7)
ISO/TR 912 -1:19 9, Toxicity test ing of fire eflu nts – P art 1: Ge eral
ISO 1 9 7-2:19 5, Pl astic – Smo e g n ratio – Determin t ion of the c ro ivity of fire
eflu nts – P art 2: St atic met hod
ISO 1 9 7-3:19 8, Pl astic – Smo e g n ratio – Determin t ion of the c ro ivity of fire
eflu nts – P art 3: Dy amic dec mp si tion method u in a travell ing furn c
_ _ _ _ _ _
1
To b p bls e
Trang 8ISO 1 9 7-4:19 8, Pl astic – Smo e g n rat io – Det erminati on of the c ro ivity of fire
eflu nts – P art 4: Dy amic de omp sition method u ing a c nic l rad i ant h ater
ISO/IEC 13 4 :2 0 , Fire s fety – Vo a ulary
ASTM D 2 71 – 0 , St andard Te t Methods for He t-Shrinkabl e Tu ing for Elect ric l U se
cor osion target
sen or u ed to determine the degre of cor osion damage, u der specif ied con ition
NOT This s n or ma b a pro u t, a c mp n nt, or a refere c materialu e to simulate th m
[ISO/IEC 13 4 , def i ition 2 ]
3.3
critic l relativ h midity
level of relative h midity that cau es le kage c r ent to ex e d a value defined in the prod ct
f ire ef flue t de a c ara teristic
ph sical an /or c emical c an es in f ire eff l ent d e to time an tran p rt
detai ed des ription of con ition , in lu in en ironmental, of one or more stages f om b f ore
ig ition to after completion of combu tion in an actual fire at a sp cific location or in a re
l-s ale simulation
[ISO/IEC 13 4 , def i ition 5 ]
Trang 9[ISO/IEC 13 4 , definition 15 ]
4 Fire scenarios and f ire models
Durin recent ye rs, major ad an es have b en made in the analy is of f ire eff l ents It is
recog ized that the comp sition of the mixture of combu tion prod cts is p rtic larly
de en ent up n the nature of the combu tin materials, the prevai n temp ratures an the
ventiation con ition , esp cial y ac es of ox gen to the se t of the fire Ta le 1 s ows how
the diff erent stages of a fire relate to the c an in atmosphere Con ition for u e in
la oratory s ale tests can b derived fom the ta le in order to cor esp n , as far as p s ible,
to ful s ale f ires
Fire in olves a complex an inter elated ar ay of ph sical an c emical phenomena As a
res lt, it is diff i ult to simulate al asp cts of a re l fire in la oratory s ale a p ratu This
pro lem of f ire model valdity is p rha s the sin le most p rplexin tec nical pro lem
as ociated with al f ire testin
General g idan e f or as es in the fire hazard of electrotec nical prod cts is given in
IEC 6 6 5-1-1
Af ter ig ition, fire develo ment may oc ur in diff erent way de en in on the en ironmental
con ition , as wel as on the ph sical ar an ement of the combu tible materials However, a
general p t ern can b esta l s ed for fire develo ment within a comp rtment, where the
general temp rature-time c rve s ows thre stages, plu a decay stage (se Fig re 1)
Stage 1 (non-f lamin decomp sition) is the in ipient stage of the fire prior to s stained
f lamin , with l t le rise in the fire ro m temp rature Ig ition an smoke generation are the
main hazard d rin this stage
Stage 2 (develo in f ire) starts with ig ition an en s with a ra id rise in f ire ro m
temp rature Spre d of f lame an he t rele se are the main hazard in ad ition to smoke
d rin this stage
Stage 3 (f ul y develo ed fire) starts when the s race of al of the combu tible contents of the
ro m has decomp sed to s c an extent that s d en ig ition oc urs al over the ro m, with a
ra id an large in re se in temp rature (flas over)
At the en of Stage 3, the combu tibles an /or ox gen have b en largely con umed an
hen e the temp rature decre ses at a rate whic de en s on the venti ation an the he t an
mas tran fer c aracteristic of the s stem This is k own as the decay stage
Trang 10In e c of these stages, a diff erent mixture of decomp sition prod cts may b f ormed an
this, in turn, influen es the cor osive p tential of the fire ef fluent prod ced d rin that stage
Figure 1 – Dif f ere t sta e in the de elo me t of a fire within a compartme t
Table 1 – Ge eral cla sif ic tion of f ire (ISO/TR 9122-1)
Sta e 3 Fuly d v lo e f ire (lamin )
a) Relativ ly low v ntiatio 1 to 5 <10 6 0 to 9 0 4 to 7
b) Relativ ly hig v ntiatio 5 to 10 <10 6 0 to 1 2 0 5 to 15
* Ge eral e viro me tal c n itio (a era e) within c mp rtme t
* Me n v lu in f ire plumen ar to f ire
* * In id nt ir a ia c o to te t s e ime (a era e)
5 General aspe ts of the cor osivity of f ire ef f luent
5.1 Cor osion dama e s e arios
With resp ct to electrotec nical eq ipment an s stems, there are thre cor osion damage
s enarios whic are of con ern These are where cor osion damage is cau ed by f ire ef fluent
in the folowin situation :
a) within electrotec nical eq ipment an s stems when exp sed to fire ef fluent cau ed by
u u ual, local zed, internal sources of ex es ive he t an ig ition;
Trang 11b) within electrotec nical eq ipment an s stems when exp sed to fire eff l ent cau ed by
external sources of flame or ex es ive he t;
c) within bui din stru tures when exp sed to f ire ef fluent emited f om electrotec nical
eq ipment an s stems
5.2 Type of cor osion dama e ef fe ts
Four typ s of cor osion damage efect are recog ized These are
a) metal los ,
b) movin p rts b comin immo i e,
c) brid in of con u tor circ its,
d) f ormation of a non-con u tin layer on contact s rf aces
5.2.1 Metal los
Metal los is cau ed by oxidation of elemental metal to a p sitive oxidation state One of the
simplest re ction of this typ is with an acid to f orm a metal salt an water, an this is wh
e rly ef f orts to comb t p tential cor osion were directed at red cin the acid gas prod ction
in fire ef f luent
However, it is not neces ary for an acid to b present for oxidation to oc ur If a metal is in
contact with an electricaly con u tive solution, the f re ion of the solution can faci tate
cor osion of contactin metals by either re ctin directly with the metal or by de olarizin the
are arou d the re ctin metal The rate of cor osion wi de en on the are of metal
af fected, the temp rature, an on the mag itu e of the dif feren e b twe n the electrode
p tentials of the oxidizin an red cin couples Metals hig er in the electroc emical series
are more prone to cor osion
Metal los can cau e man u desired eff ects In buidin s it can res lt in a we kenin or
fai ure of stru tural elements In electrical eq ipment it can cau e a decre se in electrical
con u tivity or ultimately the bre kin of a circ it
5.2.2 Movin parts be oming immobi e
Fire ef f luent can cau e movin p rts in mec anical or electromec anical eq ipment to
b come immo i e, e.g a b l b arin or p rts in a circ it bre ker This may b b cau e of the
de osition of stic y p rtic late mater or b cau e of the f ormation of c emical cor osion
prod cts b twe n s r aces
5.2.3 Bridgin of cond ctor circ its
Fire ef f luent may contain con u tive p rtic lates, e.g gra hitic carb n or ionic sp cies Metal
cor osion also prod ces ionic sp cies These con u tive sp cies can brid e the smal ga s
b twe n the co p r trac s on circ it b ard cau in u desired le kage c r ents This is of
p rtic lar con ern with digital telecommu ication eq ipment
5.2.4 Formation of a non-con ucting la er on conta t s rfa e
This is a p rtic lar case of metal los Cor osion at the interf ace of a metal contact can res lt
in the formation of a layer of non-con u tin material res ltin in the los of the circ it This is
p rtic larly l kely if the contact is b twe n dis imi ar metals b cau e they wi f orm an
electroc emical cel when in contact with a con u tive medium